TW201120269A - Polishing pad and chemical mechanical polishing method - Google Patents
Polishing pad and chemical mechanical polishing method Download PDFInfo
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- TW201120269A TW201120269A TW99136694A TW99136694A TW201120269A TW 201120269 A TW201120269 A TW 201120269A TW 99136694 A TW99136694 A TW 99136694A TW 99136694 A TW99136694 A TW 99136694A TW 201120269 A TW201120269 A TW 201120269A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24B—MACHINES, DEVICES, OR PROCESSES FOR GRINDING OR POLISHING; DRESSING OR CONDITIONING OF ABRADING SURFACES; FEEDING OF GRINDING, POLISHING, OR LAPPING AGENTS
- B24B37/00—Lapping machines or devices; Accessories
- B24B37/11—Lapping tools
- B24B37/20—Lapping pads for working plane surfaces
- B24B37/24—Lapping pads for working plane surfaces characterised by the composition or properties of the pad materials
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/42—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
- D04H1/4282—Addition polymers
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/42—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
- D04H1/4326—Condensation or reaction polymers
- D04H1/435—Polyesters
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/40—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
- D04H1/44—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling
- D04H1/46—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/0002—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the substrate
- D06N3/0004—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof characterised by the substrate using ultra-fine two-component fibres, e.g. island/sea, or ultra-fine one component fibres (< 1 denier)
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/04—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D06N3/10—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds with styrene-butadiene copolymerisation products or other synthetic rubbers or elastomers except polyurethanes
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N2211/00—Specially adapted uses
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Finish Polishing, Edge Sharpening, And Grinding By Specific Grinding Devices (AREA)
- Mechanical Treatment Of Semiconductor (AREA)
Abstract
Description
201120269 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種用於被硏磨基材之平坦化或鏡面化 之硏磨墊、及使用該硏磨墊之化學機械硏磨方法。詳言之, 例如較佳使用於半導體晶圓表面之表面硏磨、或配線基板 之硏磨等之不織布型硏磨墊。 【先前技術】 .近年來,隨著積體電路之高積體化及多層配線化,正 尋求在形成有積體電路之半導體晶圓上之高平坦度。 用以硏磨半導體晶圓之硏磨法係廣泛採用化學機械硏 磨(CMP) 。CMP係藉由一邊將硏磨糊滴於旋轉中的被硏 磨基材之表面,一邊使行星齒輪狀旋轉中的硏磨墊接觸而 進行硏磨的方法。 習知CMP所用之硏磨墊係由如具有下列專利文獻1至 4所揭示的獨立氣泡構造之高分子發泡成形體所構成的硏 磨墊;或如下列專利文獻5至18所揭示的不織布型硏磨墊。 例如,由發泡成形體所構成的硏磨墊係藉由進行二液 硬化型聚胺甲酸酯之澆鑄發泡成形所製造。如此之硏磨墊 係利用不織布型硏磨墊也具有高的剛性。因此,於硏磨時, 由於對被硏磨基材之凸部變得容易選擇性地施加載重,硏 磨速率(硏磨速度)較高。然而,由發泡成形體所構成的 硏磨墊係具有如下之缺點:所凝聚的硏磨粒存在於硏磨面 之情形下,由於也對於所凝聚的硏磨粒選擇性地施加載 重,變得容易在硏磨面上造成刮傷。因而,也如非專利文 獻1所揭示,具有如下之缺點:在具有容易被刮傷之銅配 201120269 線的基材 '或硏磨界面接著性弱的低介電常數材料之情形 下’特別容易發生刮傷或界面剝離。另外,於澆鑄發泡成 形下,由於難以獲得均質地發泡之發泡成形體,具有硏磨 面內之硏磨不均一性容易變高的缺點。 另一方面,例如不織布型硏磨墊係含有不織布、與不 織布內部所賦予的聚胺甲酸酯樹脂等之高分子彈性體。如 此之不織布型硏磨墊也較由發泡成形體所構成的硏磨墊更 具有優異的柔軟性。因此,所凝聚的硏磨粒即使存在於硏 磨面之情形下,載重也難以選擇性地施加於所凝聚的硏磨 粒,不易對硏磨面造成刮傷。然而,不織布型硏磨墊具有 得不到夠高的平坦化性能之問題。認爲此係如下之原因: 由於不織布型硏磨墊柔軟,於硏磨時,隨著被硏磨基材之 表面形狀而變形、或硏磨特性將隨時間經過而改變,應力 將局部集中於纖維所存在的部分。另外,不織布型硏磨墊 也具有硏磨速率低的問題。 另外,下列專利文獻1 5至1 8係揭示以實現較習知還 高精確度的硏磨加工作爲目的,使用由極細纖維之纖維束 所形成的不織布之不織布型硏磨墊。具體而言,例如專利 文獻15係揭示纏繞平均纖度爲0.0001至0.01分特克斯 (dtex)之聚酯極細纖維之纖維束所形成的不織布、與由存在 於此不織布內部空間之以聚胺甲酸酯爲主成分的高分子彈 性體所構成的片狀物而成之硏磨墊。 專利文獻1 :日本專利特開2000-1 7 83 74號公報 專利文獻2 :日本專利特開2000-24 803 4號公報 專利文獻3 :日本專利特開2 0 0 1 - 8 9 5 4 8號公報 .201120269 專利文獻4:日本專利特開平11-322878號公報 專利文獻5:曰本專利特開2002-9026號公報 專利文獻6 :日本專利特開平1 1 -99479號公報 專利文獻7 :日本專利特開2005 -2 1 20 5 5號公報 專利文獻8 :日本專利特開平3 -2 3 447 5號公報 專利文獻9:日本專利特開平10-128674號公報 專利文獻10:日本專利特開2004-311731號公報 專利文獻1 1 :日本專利特開平1 0 - 2 2 5 8 6 4號公報 專利文獻12:日本專利特表2005-518286號公報 專利文獻13:日本專利特開2003-201676號公報 專利文獻14:日本專利特開2005-334997號公報 專利文獻1 5 :日本專利特開2 0 0 7 - 5 4 9 1 0號公報 專利文獻16:日本專利特開2003-170347號公報 專利文獻17:日本專利特開2004-130395號公報 專利文獻18:日本專利特開2002-172555號公報 非專利文獻1:柏木正弘等、「CMP之科學」、Science Foram 股份有限公司、1997年8月20日、p. 113至119 【發明內容】 發明所欲解決之技術問題 如上所述,雖然使用由發泡成形體所構成的硏磨墊之 CMP係具有優異的硏磨速率,但是具有容易造成刮傷 '硏 磨面內之硏磨不均一性容易變高之問題。另外,使用不織 布型硏磨墊的CMP難以給予刮傷,但是具有硏磨速率低, 另外,由於耐磨損性低,具有壽命短的問題。 本發明係爲了解決如此之問題,目的在於提供一種具 .201120269 有優異的耐割傷性的不織布型硏磨墊,其可以獲得高的 磨速率,在硏磨面內之硏磨不均一性低,另外,能夠實 不易造成刮傷之CMP。 解決問題之技術手段 本發明之一形態係一種硏磨墊,其係含有由平均橫 面積爲0.1至30//m2之極細纖維的纖維束所形成的不 布、與在不織布內部所賦予的高分子彈性體;於厚度方 之縱截面,從第一表面起而朝厚度方向20%以內之厚度 域中之纖維束橫截面的平均數量密度〇1爲1000至5000 /mm2 ; Di與從對向於第一表面之第二表面起而朝厚度方 2 0 %以內之厚度區域中之纖維束橫截面的平均數量密度 之比(Di/Dz )爲1 .3至5。 另外,本發明之另一形態係一種化學機械硏磨方法 其係基材之化學機械硏磨方法;一邊將硏磨糊滴於基材 表面,一邊使該硏磨墊的第一表面接觸於該基材表面而 磨。 本發明之目的、特徵、形態及優點係藉由以下之詳 說明及所附上的圖式,變得更明白。 發明之效果 藉由使用本發明之硏磨墊而硏磨基材表面,能夠以 的硏磨速率而實現高精確度的硏磨加工。另外,在所硏 的基材表面,刮傷不易殘留。再者,硏磨墊之硏磨面的 磨損性高。 【實施方式】 針對關於本發明之硏磨墊之一實施形態,一邊參照 硏 現 截 織 向 區 個 向 D2 之 硏 細 高 磨 耐 圖 .201120269 示且一邊詳加說明。第1圖係本實施形態的硏磨墊1 〇之示 意縱截面圖。於第1圖中,1係由平均橫截面圖〇.丨至30//m2 之極細纖維la之纖維束lb所形成的不織布,2係在不織 布1之內部所賦予的高分子彈性體,3係硏磨墊1〇之第一 表面的硏磨面,4係硏磨墊10之第二表面的固定面。另外, Ri係從硏磨面3之表面起而朝厚度方向20%以內之厚度區 域,R·2係從對向於硏磨面3之固定面4的表面起而朝厚度 方向20%以內之厚度區域。又,R3是從硏磨面3表面起而 朝厚度方向40至60%之厚度區域。還有,硏磨面3係於硏 磨時接觸於被硏磨基材之面,固定面4係使用雙面黏著膠 帶等固定在CMP裝置之旋轉固定盤的面。 如第1圖所示,硏磨墊10係含有由極細纖維1之纖維 束lb所形成的不織布1、與在不織布1之內部所賦予的高 分子彈性體2的複合片。硏磨墊之厚度係按照用途加以適 當選擇,例如,較佳約爲0.5至3mm,進一步較佳約爲0.7 至2 mm。而且,硏磨墊1〇之厚度方向的縱截面,從硏磨 面3之表面起而朝厚度方向20%以內之厚度區域中之纖維 束橫截面的平均數量密度D,爲1 000至5 000個/mm2。平均 數量密度D!、與從對向於硏磨面3之固定面4的表面起而 朝厚度方向20%以內之厚度區域中之纖維束橫截面的平均 數量密度D2之比()爲1 .3至5。如此方式,存在於 硏磨墊10之硏磨面3表面附近的纖維束lb之密度係較存 在於固定面4之表面附近的纖維束lb之密度還高。藉由使 存在於硏磨面3之表面附近的纖維束lb之密度成爲高密 度’能夠使硏磨面3側之剛性及硬度比固定面4之側還高。 201120269 而且’藉由使硏磨面3側之剛性變高,用以對被硏磨 之表面塞入硏磨粒的壓力將變高,硏磨速率將變高,另 耐磨損性也將提高。另外,藉由使存在於固定面4表 近的纖維束lb之密度成爲低密度,由於適度維持對被 基材表面之隨動性或適合性,在表面上變得難以發生舌I 硏磨墊10之厚度方向縱截面中之平均數量密度】 進行如下方式所算出。使用刀刃而平行於厚度方向切 磨墊10,利用掃瞄型電子顯微鏡(SEM )而以100至 倍觀察、拍攝其切斷面。還有,此時也可以利用氧化 之染料以進行切斷面之染色。然後,從所拍攝的影像 算在從硏磨面3之表面起而朝厚度方向20%以內之厚 域Ri所觀察到的纖維束lb每既定面積之橫截面的個 算出纖維束lb每單位面積的橫截面之個數的數量密度 /mm2 )。還有,硏磨面經過立絨處理之情形下,在從 絨的極細纖維或纖維束之根部起而朝厚度方向20 %以 厚度區域,算出數量密度。另外,在硏磨墊表面形成 或孔之情形下,在未形成有溝或孔之部分,算出數量密 在數個位置(例如,5個位置)到處算出如此之數量密 將所獲得之數量密度之數量平均設爲平均數量密度D! 樣地,平均數量密度D2係計算在從固定面4之表面起 厚度方向20%以內之厚度區域R2所觀察到的纖維束每 面積之橫截面的個數,算出每單位面積的橫截面個數 量密度(個/mm2 )。在數個位置(例如,5個位置) 算出如此之數量密度,將所獲得之數量密度的數量平 爲平均數量密度D2。 基材 外, 面附 硏磨 1傷。 係 斷硏 1000 锇等 ,計 度區 數, :(個 所立 內之 有溝 • II··? r度。 ;度, 丨。同 而朝 既定 之數 到處 均設 201120269 硏磨墊10之平均數量密度〇,爲1000至5000個/mm2, 較佳爲1000至4500個/mm2,進一步較佳爲1100至4000 個/mm2,特別理想爲1200至3000個/mm2之範圍。卩,低於 1 000個/mm2之情形下,由於使硏磨面3之表面附近的剛性 變低,且由於對被硏磨基材變得難以塞入硏磨粒而使硏磨 速率降低或耐磨損性降低。另外,D!超過5 000個/mm2之 情形下,由於使硏磨面3之表面附近的剛性變得過高,刮 傷變得容易發生。 另外,硏磨墊10之平均數量密度D2爲200至3500個 /mm2’更佳爲3 00至3 000個/mm2,特別理想爲5 00至2500 個/mm2之範圍。02過低之情形下,由於使對被硏磨基材之 隨動性或適合性變得過高及硏磨墊整體之剛性將降低,具 有平坦化性能降低之傾向。於此,所謂平坦化性能係意指 在被硏磨基材上形成具有高平坦度之硏磨面的能力。平均 數量密度D2過高之情形下,由於使對被硏磨基材之隨動性 或適合性變低,具有硏磨面內之硏磨不均一性變高之傾 向。另外,由於硏磨墊內部之硏磨糊的保持性將降低,具 有硏磨速率將降低之傾向。 硏磨墊1〇係其平均數量密度Di與其平均數量密度D2 之比(Dt/Dz)爲1.3至5,較佳爲1.4至3.7,進一步較佳 爲1.5至2.6之範圍。〇"02低於1.3之情形下,由於提高 剛性’硏磨速率將提高;但是由於使對被硏磨基材之隨動 性變得過低,硏磨不均一性將變高,同時耐磨損性也將降 低。另一·方面,D"D 2超過5之情形下,由於使對被硏磨基 材之隨動性變得過高,硏磨速率將降低,另外,由於硏磨 -10- 201120269 墊之硏磨面3側與固定面4側之密度差過大,硏磨面3側 與固定面4側之隨動性產生差異而使平坦化性能降低。 另外,硏磨墊10係存在平均數量密度D!、平均數量 密度D2、與從硏磨面3之表面起而朝厚度方向40至6 0% 之厚度區域R3中之纖維束橫截面的平均數量密度D3較佳 爲D 1 > D3 > D2之關係。具有如此關係之情形下,由於硏磨 墊1內部之硏磨糊具有優異的保持性,實現更髙的硏磨速 率。另外,硏磨墊之剛性與對被硏磨基材之隨動性也具有 優異的均衡性。其結果,平坦化性能或硏磨速率變得更高 的同時,耐磨損性也具有變..高的傾向。 另外,DWD3爲1至1.4範圍之情形下,不織布內部之 剛性均衡性將變得更適切,對硏磨粒之被硏磨基材的塞入 硬度將變高,具有可以獲得高的硏磨速率之傾向。另外, 從對被硏磨基材之隨動性更適切之.觀點,D3/D2較佳爲1.4 至3範圍之情形。 形成纖維束之極細纖維的平均橫截面積係 〇.1至 3 0//m2,較佳爲1 0至1 5//m2。由平均橫截面積低於1 //m2 之極細纖維所構成的纖維束之情形下,於硏磨之際,纖維 將被斷裂而脫落,硏磨粒將凝聚於所脫落的纖維而使刮傷 變得容易發生。另外,由平均橫截面積超過3 0//m2之極細 纖維所構成的纖維束之情形下,極細纖維之表面積將變 大,充分提高硏磨面附近之纖維束的密度將變得困難。 另外,纖維束之平均橫截面積爲40至4 00//m2,進一 步較佳爲40至3 5 0//m2。纖維束之平均橫截面積爲40//m2 以上之情形下,硏磨墊之強度或耐磨損性將提髙,另外, -11- 201120269 也變得難以引起因不織布製造時之針扎處理所造成的纖維 斷裂。另外,纖維束之平均橫截面積爲400//m2以下之情形 下,由於能夠充分提高硏磨面附近之纖維束的密度,能夠 進一步提高硏磨速率。還有,形成·一纖維束之極細纖維的 條數較佳爲5至4000條,進一步較佳爲5至30條。 形成極細纖維之聚合物並未予以特別限定。具體例, 例如,可列舉:聚對苯二甲酸乙二酯(PET )、間苯二甲酸 改性PET、磺基間苯二甲酸改性PET、聚對苯二甲酸丁二 酯、聚對苯二甲酸己二酯等之芳香族聚酯類及其共聚物; -聚乳酸、聚丁二酸乙二酯、聚丁二酸丁二酯、聚丁二酸己 二酸丁二酯、聚羥基丁酸酯-聚羥基戊酸酯共聚物等之脂肪 族聚酯及其共聚物;耐綸6、耐綸66、耐綸10、耐綸11' 耐綸12、耐綸6-12等之聚醯胺類及其共聚物;聚丙烯、聚 乙烯、聚丁烯、聚甲基戊烯、氯系聚烯烴等之聚烯烴類及 其共聚物;含有25至70莫耳%之乙烯單位的改性聚乙烯 醇;及聚胺甲酸酯系、耐綸系、聚酯系等之彈性體。此等 聚合物能夠單獨地或組合二種以上而使用。 還有,形成極細纖維之聚合物係玻璃轉移溫度(Tg) 較佳爲50至300 °C,進一步較佳爲60至150 °C ’在50 °C使 其飽和吸水時之吸水率爲0.2至2質量%之聚合物特別理 想。 玻璃轉移溫度爲上述範圍之情形下,由於能夠維持更 高的剛性,硏磨墊之平坦化性能將進一步變高’另外’於 硏磨之際,隨時間經過而使剛性變得不易降低。另外’在 50 °C使其飽和吸水時之吸水率爲上述範圍之情形下’由於 -12- 201120269 硏磨墊於適度之範圍吸收硏磨糊,硏磨速率或硏磨均一性 進一步變得良好。另外,由於不會過度吸收硏磨糊,硏磨 墊之剛性隨時間經過之降低及平坦化性能隨時間經過之變 動將被抑制。 如此之聚合物的具體例,例如,可列舉:由PET ( Tg 77t:、吸水率1質量% )、間苯二甲酸改性PET ( Tg 67至 77°C、吸水率1質量% )、磺基間苯二甲酸改性PET ( Tg 67 至77°C、吸水率1至3質量%)、聚萘二甲酸丁二酯(Tg 8 5°C、吸水率1質量% )、聚萘二甲酸乙二酯(Tg 124°C, 吸水率:1.質量% )等所形成的芳香族聚酯系纖維;由間苯 二甲酸與壬二醇與甲基辛二醇共聚合聚醯胺(Tg 125至 140°C、吸水率1至3質量%)等所形成的半芳香族聚醯胺 系纖維等。尤其,將芳香族成分作爲1成分單體單位而含 有的PET等或改性PET等之半芳香族聚酯系聚合物特別理 想。使用半芳香族聚酯系聚合物之情形下,從下列觀點而 特別理想:容易提高硏磨片之剛性,於硏磨之際,也不易 發生因水分所導致的隨時間經過變化,另外,容易形成緻 密且高密度之不織布》 ^外,本實施形態中之不織布係由極細纖維之纖維束 所形成,而該極細纖維係源自由極細纖維發生型纖維之長 纖維所構成的長纖維棉網,具有優異的形態安定性,再者, 從纖維脫落將變少的觀點也較佳。例如,如此之不織布係 藉由與熔融紡紗直接鍵結的所謂紡紗黏合法而製造由如海 島型複合纖維之極細纖維發生型纖維所構成的長纖維棉 網,纏繞處理此長纖維棉網而作成纏繞棉網後,將極細纖 -13- 201120269 維發生型纖維轉換成極細纖維所製造。還有,所謂長纖維 並非使纖維長度如約1 〇至5 0 mm短纖維的方式來刻意切 斷的短纖維(staple),具有長的纖維長度之纖維。具體而 言,例如極細纖維發生型纖維的纖維長度較佳爲100 mm 以上,只要技術上可製造,並且不會物理性斷裂,也可以 爲數m、數百m、數km之纖維長度。 另外,本實施形態中之不織布也可以爲使形態安定性 提高之目的下而使編織物纏繞一體化的不織布。還有,使 用纏繞不織布之情形,纖維束之平均數量密度係以除了編 織物以外之僅不織布·的厚度爲基準所算出。 硏磨墊10係具有在由極細纖維la之纖維束lb所形成 的不織布1之內部賦予有高分子彈性體2而予以複合化的 構造。 不織布1與高分子彈性體2之含有比率(不織布/高分 子彈性體;質量比)較佳爲5 5 /4 5至95/5 ’進一步較佳爲 60/40至90/10,特別理想爲70/30至90/10之範圍。如此 範圍之情形下,可以獲得剛性爲適度之硏磨墊。高分子彈 性體之含有比率過少之情形下,具有硏磨墊之剛性變得過 低之傾向。另外,高分子彈性體之含有比率過多之情形下’ 具有硏磨墊之剛性變得過高之傾向。 另外,如第2圖所示,於硏磨墊10中’形成纖維束 lb之極細纖維la較佳爲利用高分子彈性體2所黏合而予 以集束。於此,所謂將極細纖維la予以集束係意指存在於 纖維束lb內部之極細纖維la的大部分係藉由滲入纖維束 1 b內部之高分子彈性體2所黏合而予以束縛的狀態°如此 -14- 201120269 方式,藉由使極細纖維1 a予以集束,硏磨墊1 0之剛性將 變高,同時也抑制極細纖維la之脫落。極細纖維la未予 以集束之情形下,由於極細纖維擺動,具有使硏磨墊變得 柔軟之傾向。201120269 VI. Description of the Invention: TECHNICAL FIELD The present invention relates to a honing pad for flattening or mirroring a honed substrate, and a chemical mechanical honing method using the honing pad. More specifically, for example, a non-woven type honing pad which is preferably used for surface honing of a surface of a semiconductor wafer or honing of a wiring board. [Prior Art] In recent years, with the high integration of integrated circuits and multilayer wiring, high flatness on a semiconductor wafer on which an integrated circuit is formed is being sought. Chemical mechanical honing (CMP) is widely used in honing methods for honing semiconductor wafers. The CMP is a method of honing by rubbing the honing paste on the surface of the honed substrate which is being rotated while contacting the honing pad in the planetary gear shape. The honing pad used in the conventional CMP is a honing pad composed of a polymer foam molded body having the closed cell structure disclosed in the following Patent Documents 1 to 4; or a non-woven fabric as disclosed in the following Patent Documents 5 to 18. Type honing pad. For example, a honing pad composed of a foamed molded article is produced by casting foam molding of a two-liquid-curing polyurethane. Such a honing pad also has high rigidity by using a non-woven type honing pad. Therefore, at the time of honing, the honing rate (honing speed) is high because the convex portion of the honed substrate becomes easy to selectively apply the load. However, the honing pad composed of the foamed molded body has a drawback in that the agglomerated honing particles are present in the honing surface, since the load is also selectively applied to the condensed honing particles. It is easy to cause scratches on the honing surface. Therefore, as disclosed in Non-Patent Document 1, there is a disadvantage that it is particularly easy in the case of a substrate having a copper-bonded 201120269 wire which is easily scratched or a low dielectric constant material having a weak honing interface. Scratch or interface peeling occurred. Further, in the case of casting foaming, it is difficult to obtain a foamed molded body which is uniformly foamed, and there is a disadvantage that the honing unevenness in the honing surface tends to be high. On the other hand, for example, the non-woven type honing pad contains a non-woven fabric and a polymeric elastomer such as a polyurethane resin provided inside the nonwoven fabric. Therefore, the non-woven type honing pad also has superior softness compared to the honing pad composed of the foamed molded body. Therefore, even if the entangled granules are present on the honing surface, it is difficult to selectively apply the load to the entangled honing granules, and it is difficult to cause scratches on the honing surface. However, the non-woven type honing pad has a problem that the flattening performance is not sufficiently high. The reason for this is as follows: Since the non-woven type honing pad is soft, when honing, it deforms with the surface shape of the honed substrate, or the honing characteristic changes over time, and the stress is locally concentrated on The part of the fiber that exists. In addition, the non-woven type honing pad also has a problem of low honing rate. Further, the following Patent Documents 15 to 18 disclose a non-woven type honing pad which is formed of a non-woven fabric formed of a fiber bundle of ultrafine fibers for the purpose of achieving a more precise and highly precise honing process. Specifically, for example, Patent Document 15 discloses a nonwoven fabric formed by winding a fiber bundle of a polyester microfiber having an average fineness of 0.0001 to 0.01 dtex, and a polyamine which is present in the inner space of the nonwoven fabric. A honing pad made of a sheet of a polymer elastomer having an acid ester as a main component. Patent Document 1: Japanese Patent Laid-Open Publication No. 2000-1 7 83 74 Patent Document 2: Japanese Patent Laid-Open No. 2000-24 803 No. 4 Patent Document 3: Japanese Patent Laid-Open No. 2 0 0 1 - 8 9 5 4 8 Japanese Patent Laid-Open Publication No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. Japanese Laid-Open Patent Publication No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. Japanese Patent Laid-Open Publication No. Hei No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. No. Hei. [Patent Document 14] Japanese Patent Laid-Open Publication No. Hei. No. 2005-334997. Japanese Patent Laid-Open No. 2004-130395, Patent Document 18: Japanese Patent JP-A-2002-172555 Non-Patent Document 1: Kashiyuki Masahiro, et al., "Science of CMP", Science Foram Co., Ltd., August 20, 1997, p. 113 to 119 [Invention] Technical Problem to be Solved by the Invention As described above, the CMP system using the honing pad composed of the foamed molded article has an excellent honing rate, but has a problem that it is easy to cause scratching, and the honing unevenness in the honing surface tends to be high. Further, CMP using a non-woven type honing pad is difficult to give a scratch, but has a low honing rate and a problem of short life due to low abrasion resistance. The present invention has been made to solve such a problem, and an object thereof is to provide a non-woven type honing pad having excellent cut resistance of 201120269, which can attain a high grinding rate and low honing unevenness in a honing surface. In addition, CMP which is less likely to cause scratching can be achieved. MEANS FOR SOLVING THE PROBLEMS One aspect of the present invention is a honing pad comprising a fiber bundle composed of a fiber bundle having an average transverse area of 0.1 to 30//m 2 and a high density imparted inside the nonwoven fabric. Molecular elastomer; in the longitudinal section of the thickness, the average number density 纤维1 of the cross-section of the fiber bundles in the thickness domain from the first surface to within 20% of the thickness direction is 1000 to 5000 / mm 2 ; Di and the opposite direction The ratio (Di/Dz) of the average number density of cross-sections of the fiber bundles in the thickness region from the second surface of the first surface to within 20% of the thickness is from 1.3 to 5. In addition, another aspect of the present invention is a chemical mechanical honing method, which is a chemical mechanical honing method for a substrate; while the honing paste is dropped on the surface of the substrate while the first surface of the honing pad is in contact with the Grinding the surface of the substrate. The objects, features, aspects and advantages of the present invention will become more apparent from the claims EFFECT OF THE INVENTION By honing the surface of the substrate by using the honing pad of the present invention, high-accuracy honing processing can be realized at the honing rate. In addition, scratches are less likely to remain on the surface of the substrate to be coated. Furthermore, the honing surface of the honing pad is highly abrasive. [Embodiment] An embodiment of the honing pad according to the present invention will be described with reference to the 高 高 高 . . . . . . . . . . . . . 2011 2011 2011 2011 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 Fig. 1 is a schematic longitudinal sectional view showing the honing pad 1 of the present embodiment. In Fig. 1, 1 is a non-woven fabric formed by a fiber bundle lb of an ultrafine fiber la having an average cross-sectional view of 30.丨 to 30//m2, and 2 is a polymer elastic body imparted inside the nonwoven fabric 1, 3 The honing surface of the first surface of the honing pad 1 is the fixing surface of the second surface of the lining pad 10. Further, Ri is a thickness region from the surface of the honing surface 3 to 20% in the thickness direction, and R·2 is from 20% in the thickness direction from the surface of the fixing surface 4 facing the honing surface 3. Thickness area. Further, R3 is a thickness region from the surface of the honing surface 3 to 40 to 60% in the thickness direction. Further, the honing surface 3 is in contact with the surface of the honed substrate during honing, and the fixing surface 4 is fixed to the surface of the rotating fixed disk of the CMP apparatus using a double-sided adhesive tape or the like. As shown in Fig. 1, the honing pad 10 is a composite sheet comprising a nonwoven fabric 1 formed of a fiber bundle 1b of the ultrafine fibers 1 and a high molecular elastomer 2 provided inside the nonwoven fabric 1. The thickness of the honing pad is suitably selected according to the use, for example, preferably from about 0.5 to 3 mm, further preferably from about 0.7 to 2 mm. Further, the longitudinal section of the honing pad 1 in the thickness direction is an average number density D of the cross section of the fiber bundle in the thickness region from the surface of the honing surface 3 to 20% in the thickness direction, from 1,000 to 5,000. /mm2. The ratio () of the average number density D! of the fiber bundle cross-section in the thickness region from the surface opposite to the fixing surface 4 of the honing surface 3 to the thickness of 20% in the thickness direction is 1 . 3 to 5. In this manner, the density of the fiber bundles 1b present in the vicinity of the surface of the honing surface 3 of the honing pad 10 is higher than the density of the fiber bundles 1b located near the surface of the fixed faces 4. By making the density of the fiber bundles lb existing in the vicinity of the surface of the honing surface 3 high, the rigidity and hardness of the honing surface 3 side can be made higher than the side of the fixed surface 4. 201120269 Moreover, 'by increasing the rigidity of the honing surface 3 side, the pressure for tamping the honed surface to the honing grain will become higher, the honing rate will become higher, and the wear resistance will also be improved. . Further, by making the density of the fiber bundles 1b which are present on the fixed surface 4 low, the tongue I honing pad becomes difficult to occur on the surface due to moderately maintaining the followability or suitability to the surface of the substrate. The average number density in the longitudinal section of the thickness direction of 10 is calculated as follows. The pad 10 was cut parallel to the thickness direction using a blade, and the cut surface was observed by a scanning electron microscope (SEM) at 100 to magnification. Further, at this time, it is also possible to use the oxidized dye to perform dyeing on the cut surface. Then, from the photographed image, the calculated fiber bundle lb per unit area of the cross section of the predetermined area of the fiber bundle lb observed from the thick surface Ri within 20% in the thickness direction from the surface of the honing surface 3 The number density of the number of cross sections / mm2). Further, in the case where the honing surface is subjected to the velvet treatment, the number density is calculated from the root portion of the fine fiber or the fiber bundle of the pile to the thickness region of 20% in the thickness direction. In addition, in the case where the surface of the honing pad is formed or a hole, in the portion where the groove or the hole is not formed, the number density which is obtained by calculating the number of the dense portions at a plurality of positions (for example, five positions) is calculated. The number is averaged as the average number density D!. The average number density D2 is the number of cross-sections per area of the fiber bundle observed in the thickness region R2 within 20% of the thickness direction from the surface of the fixed surface 4. Calculate the number density (number/mm2) of the cross section per unit area. The number density is calculated at a plurality of positions (e.g., 5 positions), and the amount of the obtained number density is equal to the average number density D2. Outside the substrate, the surface is honed and wounded. The system is divided into 1000 锇, etc., the number of counting areas, : (there is a ditch in the standing area • II··? r degree. ; degree, 丨. The same number is set everywhere 201120269 The average number of honing pads 10 The density 〇 is from 1,000 to 5,000 / mm 2 , preferably from 1,000 to 4,500 / mm 2 , further preferably from 1,100 to 4,000 / mm 2 , particularly preferably from 1200 to 3,000 / mm 2 , 卩, less than 1,000 In the case of /mm2, the rigidity near the surface of the honing surface 3 is lowered, and the honing rate is lowered or the abrasion resistance is lowered because it becomes difficult to insert the honing particles to the honed substrate. Further, in the case where D! exceeds 5,000 pieces/mm2, since the rigidity near the surface of the honing surface 3 is excessively high, scratching easily occurs. In addition, the average number density D2 of the honing pad 10 is 200. Up to 3500 / mm2' is preferably from 300 to 3 000 / mm2, particularly preferably in the range of 500 to 2500 / mm2. In the case of too low 02, due to the follow-up of the substrate being honed Or the suitability becomes too high and the rigidity of the honing pad as a whole is lowered, and the flattening performance tends to be lowered. Here, the flattening performance means The ability to form a honing surface having a high degree of flatness on a honed substrate. In the case where the average number density D2 is too high, since the followability or suitability to the honed substrate is lowered, the honing is performed. The tendency of the honing unevenness in the surface becomes higher. In addition, since the retention of the mash in the honing pad is lowered, the honing rate tends to decrease. The honing pad 1 is the average number density Di The ratio (Dt/Dz) to its average number density D2 is from 1.3 to 5, preferably from 1.4 to 3.7, and further preferably from 1.5 to 2.6. In the case where 〇 "02 is lower than 1.3, the rigidity is increased 硏The grinding rate will increase; however, since the followability to the honed substrate becomes too low, the honing heterogeneity will become higher and the wear resistance will also decrease. On the other hand, D"D 2 In the case of more than 5, since the followability to the honed substrate becomes too high, the honing rate is lowered, and the honing surface 3 side and the fixing surface 4 side of the mat -10- 201120269 The difference in density is too large, and the followability of the side of the honing surface 3 and the side of the fixing surface 4 is different to lower the flattening performance. Further, the honing pad 10 has an average number density D!, an average number density D2, and an average of the fiber bundle cross-sections in the thickness region R3 from the surface of the honing surface 3 to the thickness direction of 40 to 60%. The number density D3 is preferably a relationship of D 1 > D3 > D2. In the case of such a relationship, since the honing paste inside the honing pad 1 has excellent retentivity, a more honing honing rate is achieved. The rigidity of the honing pad and the followability to the honed substrate also have an excellent balance. As a result, the flattening performance or the honing rate becomes higher, and the abrasion resistance tends to be higher. In addition, in the case where the DWD3 is in the range of 1 to 1.4, the rigidity balance inside the nonwoven fabric becomes more appropriate, and the penetration hardness of the honed substrate to the honing grain becomes higher, and the honing rate can be obtained. The tendency. Further, from the viewpoint of being more suitable for the followability of the honed substrate, D3/D2 is preferably in the range of 1.4 to 3. The ultrafine fibers forming the fiber bundle have an average cross-sectional area of from 1 to 30/m2, preferably from 10 to 15/m2. In the case of a fiber bundle composed of ultrafine fibers having an average cross-sectional area of less than 1 // m2, the fiber will be broken and detached during honing, and the honing particles will condense on the detached fibers to cause scratching. It becomes easy to happen. Further, in the case of a fiber bundle composed of ultrafine fibers having an average cross-sectional area of more than 30/m2, the surface area of the ultrafine fibers is increased, and it is difficult to sufficiently increase the density of the fiber bundles in the vicinity of the honing surface. Further, the fiber bundle has an average cross-sectional area of 40 to 400 / m 2 , and further preferably 40 to 3 5 / / m 2 . When the average cross-sectional area of the fiber bundle is 40/m2 or more, the strength or wear resistance of the honing pad will be improved, and -11-201120269 will also become difficult to cause pinning treatment due to non-woven fabric manufacturing. The resulting fiber breaks. Further, when the average cross-sectional area of the fiber bundle is 400 / / m 2 or less, the honing rate can be further increased because the density of the fiber bundle in the vicinity of the honing surface can be sufficiently increased. Further, the number of the ultrafine fibers forming the fiber bundle is preferably from 5 to 4,000, more preferably from 5 to 30. The polymer forming the ultrafine fibers is not particularly limited. Specific examples include, for example, polyethylene terephthalate (PET), isophthalic acid modified PET, sulfoisophthalic acid modified PET, polybutylene terephthalate, and polyparaphenylene. Aromatic polyesters such as hexamethylene dicarboxylate and copolymers thereof; - polylactic acid, polyethylene succinate, polybutylene succinate, polybutylene succinate, polyhydroxyl Aliphatic polyesters such as butyrate-polyhydroxyvalerate copolymers and copolymers thereof; polyester 6, nylon 66, nylon 10, nylon 11' nylon 12, nylon 6-12, etc. Indoleamines and copolymers thereof; polyolefins and copolymers thereof such as polypropylene, polyethylene, polybutene, polymethylpentene, chlorine-based polyolefins; and ethylene units containing 25 to 70 mol% Polyvinyl alcohol; and an elastomer such as a polyurethane, a nylon or a polyester. These polymers can be used singly or in combination of two or more. Further, the polymer-forming glass transition temperature (Tg) for forming the ultrafine fibers is preferably from 50 to 300 ° C, more preferably from 60 to 150 ° C. When the saturated water is absorbed at 50 ° C, the water absorption is 0.2 to 2% by mass of the polymer is particularly desirable. When the glass transition temperature is in the above range, the flattening performance of the honing pad is further increased by maintaining higher rigidity. In addition, the rigidity is less likely to be lowered as time passes. In addition, 'when the water absorption rate at 50 ° C makes it saturated, the water absorption rate is in the above range'. Since the -12- 201120269 honing pad absorbs the mash in a moderate range, the honing rate or the honing uniformity is further improved. . In addition, since the squeegee is not excessively absorbed, the rigidity of the honing pad is lowered with time and the variation of the flattening performance over time is suppressed. Specific examples of such a polymer include, for example, PET (Tg 77t: water absorption: 1% by mass), isophthalic acid modified PET (Tg 67 to 77 ° C, water absorption: 1% by mass), and sulphur Isophthalic acid modified PET (Tg 67 to 77 ° C, water absorption 1 to 3 mass%), polybutylene naphthalate (Tg 8 5 ° C, water absorption 1% by mass), polynaphthalene dicarboxylic acid Aromatic polyester fiber formed by ethylene glycol (Tg 124 ° C, water absorption: 1. mass%); copolymerization of isophthalic acid (Tg) from isophthalic acid and decanediol and methyl octanediol Semi-aromatic polyamide fibers such as 125 to 140 ° C and water absorption of 1 to 3 mass%). In particular, a semi-aromatic polyester-based polymer such as PET or the like which contains an aromatic component as a monomer unit of one component or modified PET is particularly preferable. In the case of using a semi-aromatic polyester-based polymer, it is particularly preferable from the viewpoint that it is easy to increase the rigidity of the honing sheet, and it is less likely to cause a change with time due to moisture during honing, and it is easy. Forming a dense and high-density non-woven fabric, the non-woven fabric in the present embodiment is formed of a fiber bundle of ultrafine fibers, and the ultrafine fiber is a long-fiber cotton web composed of long fibers of the ultrafine fiber-generating fiber. It has excellent form stability, and it is also preferable from the viewpoint that the fiber shedding is reduced. For example, such a non-woven fabric is manufactured by a so-called spinning adhesive which is directly bonded to melt-spun yarn, and a long-fiber cotton web composed of a very fine fiber-generating fiber such as an island-in-sea type composite fiber is produced, and the long-fiber cotton web is wound and processed. After the winding cotton web is formed, the ultrafine fiber-13-201120269 dimensionally-generating fiber is converted into a very fine fiber. Further, the term "long fiber" is not a staple which is deliberately cut in such a manner that the fiber length is as long as about 1 〇 to 50 mm short fibers, and a fiber having a long fiber length. Specifically, for example, the fiber length of the ultrafine fiber-generating fiber is preferably 100 mm or more, and may be a fiber length of several m, several hundred m, or several km as long as it is technically manufacturable and does not physically break. Further, the nonwoven fabric in the present embodiment may be a nonwoven fabric in which the knitted fabric is wound and integrated for the purpose of improving the form stability. Further, in the case of using a entangled nonwoven fabric, the average number density of the fiber bundles is calculated based on the thickness of only the non-woven fabric other than the woven fabric. The honing pad 10 has a structure in which the polymer elastic body 2 is provided inside the nonwoven fabric 1 formed of the fiber bundles 1b of the ultrafine fibers 1a, and is composited. The content ratio of the nonwoven fabric 1 to the polymeric elastomer 2 (non-woven fabric/polymer elastomer; mass ratio) is preferably from 5 5 /45 to 95/5', more preferably from 60/40 to 90/10, particularly preferably Range of 70/30 to 90/10. In such a range, a stiffening pad of moderate rigidity can be obtained. When the content ratio of the polymer elastic body is too small, the rigidity of the honing pad tends to be too low. Further, when the content ratio of the polymeric elastomer is too large, the rigidity of the honing pad tends to be too high. Further, as shown in Fig. 2, the ultrafine fibers la forming the fiber bundles lb in the honing pad 10 are preferably bundled by the polymer elastic body 2 to be bundled. Here, the bundling of the ultrafine fibers la means that most of the ultrafine fibers la existing inside the fiber bundles 1b are bound by the polymer elastic body 2 penetrating into the inside of the fiber bundles 1b. In the manner of the ultrafine fibers 1 a being bundled, the rigidity of the honing pad 10 is increased, and the peeling of the ultrafine fibers la is also suppressed. In the case where the ultrafine fibers la are not bundled, the honing mat tends to be soft due to the oscillation of the ultrafine fibers.
另外,如第2圖所示,複數條纖維束lb彼此較佳爲藉 由存在於纖維束lb之外側的高分子彈性體2所黏合而以塊 狀(bulk)存在。如此方式,藉由使纖維束彼此予以黏合而提 高硏磨墊之形態安定性且提高硏磨安定性。還有,極細纖 維之集束狀態及纖維束彼此之黏合狀態能夠藉由硏磨墊截 面之電子顯微鏡照片而加以確認.J 黏合滲入極細纖維內部之高分子彈性體及極細纖維束 彼此之高分子彈性體較佳爲非多孔質狀。還有,所謂非多 孔質狀係意指實質上不具有如多孔質狀、或海綿狀(以下, 也簡稱爲多孔質狀)之高分子彈性體的許多獨立氣泡的狀 態。具體而言,例如,意指並非如使溶劑系聚胺甲酸酯凝 固而可以獲得之具有許多微細獨立氣泡之高分子彈性體。 進行集束或黏合之高分子彈性體爲非多孔質狀之情形下, 硏磨安定性將變高,另外,由於硏磨時之糊屑或墊屑變得 不易堆積於空隙中,能夠不容易磨損且長時間維持高的硏 磨速率。再者,由於對極細纖維之接著強度變高,能夠更 抑制起因於纖維脫落之刮傷的發生。再者,由於可以獲得 更高的剛性,且可以獲得更具有優異的平坦化性能的硏磨 墊。 在硏磨墊10之硏磨面3之D硬度較佳爲25至50,進 一步較佳爲30至49,特別理想爲爲31至47。D硬度爲如 -15- .201120269 此範圍之情形下,不易受到被硏磨基材之表面形狀的影 .響,從平坦化性能之觀點,可以獲得最適剛性之硏磨墊。 接著’針對在不織布內部所賦予的高分子彈性體而詳 .細加以說明。 不織布之內部所賦予的高分子彈性體的種類並未予以 特別限定。高分子彈性體之具體例,例如,由聚胺甲酸酯 系樹脂、聚醯胺系樹脂、(甲基)丙烯酸酯系樹脂、(甲 基).丙烯酸酯-苯乙烯系樹脂、(甲基)丙烯酸酯·丙烯腈 系樹脂、(甲基)丙烯酸酯-烯烴系樹脂、(甲基)丙烯酸 酯-(加氫)異戊二烯系樹脂、(甲基)丙.雜酸酯-丁二烯 系樹脂、苯乙烯-丁二烯系樹脂、苯乙烯-加氫異戊二烯系 樹脂、丙烯腈-丁二烯系樹脂、丙烯腈-丁二烯-苯乙烯系樹 脂、醋酸乙烯系樹脂、(甲基)丙烯酸酯·醋酸乙烯系樹脂、 乙烯-醋酸乙烯系樹脂、乙烯-烯烴系樹脂'矽氧烷系樹脂、 氟系樹脂、聚酯系樹脂所構成的彈性體。高分子彈性體可 以各自單獨使用或是也可以組合二種以上而使用。此等高 分子彈性體之中,如聚胺甲酸酯系樹脂、聚醯胺系樹脂、 聚乙烯醇系樹脂等之氫鍵結性高分子彈性體特別理想。還 有’氫鍵結性高分子彈性體係藉由氫鍵而進行結晶化或凝 聚的高分子彈性體,對極細纖維之集束性及對極細纖維之 束縛黏合性高。另外,聚胺甲酸酯系樹脂係用以集束極細 纖維或黏合纖維束彼此之具特別優異的接著性,另外,從 提高硏磨墊之硬度,具有優異的硏磨下隨時間經過的安定 性之觀點則特別理想。 高分子彈性體之玻璃轉移溫度較佳爲- lot以下,進一 •16- 201120269 步較佳爲-15 °C以下。玻璃轉移溫度過高之情形下,由於高 分子彈性體脆弱,擔憂硏磨中將脫落。玻璃轉移溫度係由 利用在動態黏彈性測定拉伸模式之損失彈性模數的波峰溫 度所算出。玻璃轉移溫度係視高分子彈性體之分散的波 峰溫度而定。例如,聚胺甲酸酯系樹脂之情形,藉由調整 成爲軟質成分之聚醇的組成或硬質成分與軟質成分之比率 而能夠使玻璃轉移溫度成爲-1 〇 °c以下。 另外,高分子彈性體較佳爲具有如下之彈性。從硏磨 墊之剛性變高,另外也具有優異的彈性之觀點,高分子彈 性體之在23°c及50°c之儲存彈性模數(G’)爲90至900 MPa,進一步較佳爲20至800 MPa。另外,從具有優異的 硏磨安定性之觀點,在23 °C之儲存彈性模數(G23’)與在 5 0°C之儲存彈性模數(G5〇’)之比(G23 7 G50’)爲4以下, 進一步較佳爲3以下且1/3以上。 另外,從具有優異的硏磨糊之保液性及硏磨安定性之 觀點,高分子彈性體係於50°C予以飽和吸水時之吸水率較 佳爲0.2至5質量%,進一步較佳爲0.5至3質量%。 於此,高分子彈性體之代表例係針對聚胺甲酸酯系樹 脂而詳細加以說明。聚胺甲酸酯系樹脂可列舉:藉由以既 定之莫耳比而使高分子聚醇、有機聚異氰酸酯、與鏈延長 劑等反應所獲得之各種聚胺甲酸酯系樹脂。 高分子聚醇之具體例,例如,可列舉:聚乙二醇、聚 丙二醇、聚四亞甲基二醇 '聚(.甲基四亞甲基二醇)等之 聚酸系聚醇及其共聚物;聚伸丁基己二酸酯二醇、聚伸丁 基癸二酸酯二醇、聚六亞甲基二酸酯二醇、聚(3-甲基- l,5- -17- 201120269 伸戊基己二酸酯)二醇、聚(3-甲基-1,5-伸戊基癸二酸酯) 二醇、間苯二甲酸共聚合聚醇、對苯二甲酸共聚合聚醇、 環己醇共聚合聚醇、聚己內酯二醇等之聚酯系聚醇及其共 聚物;聚六亞甲基碳酸酯二醇、聚(3 -甲基·1,5·伸戊基碳 酸酯)二醇、聚五亞甲基碳酸酯二醇、聚四亞甲基碳酸酯 二醇、聚(甲基-1,8-八亞甲基碳酸酯)二醇、聚九亞甲基 碳酸酯二醇、聚環己烷碳酸酯等之聚碳酸酯系聚醇及其共 聚物;聚酯碳酸酯聚醇等。另外必要時,也可以倂用三羥 甲基丙烷等之3官能醇或季戊四醇等之4官能醇等之多官 能醇,或是;乙二醇、丙二醇、1,4-丁二醇、1,6-己二醇等之 短鏈醇。 另外,藉由將羧基、磺酸基、烴基、碳數5以下-尤 其碳數3以下之聚伸烷基二醇基等之具有親水性基之聚醇 成分作爲樹脂構造單位而含有,能夠使對水性介質之分散 性、或對硏磨糊之潤濕性提高。 具有羧基之聚醇成分的具體例,可列舉:2,2-雙(羥 甲基)丙酸、2,2-雙(羥甲基)丁酸、2,2-雙(羥甲基)戊 酸等之含有羧基之二醇。另外,具有碳數5以下之聚伸烷 基二醇基之聚醇成分的具體例,可列舉:聚乙二醇、聚丙 二醇及其共聚物。 還有,聚醇成分係使用具有-10 °C以下,進一步具有 -20 °C以下之玻璃轉移溫度的聚碳酸酯系聚醇,使聚胺甲酸 易脂酸 容有碳 於含聚 由爲之 , 佳等 外較醇 另分聚 , 成系 下醇酯 以聚酸 0°c之碳 -1此聚 爲如狀 成。鏈 度想直 溫理、 移別醇 轉特聚 璃而系 玻數酯 之模酸 脂性碳 樹彈聚 系高式 酯提環 -18 - 201120269 酯系聚醇,其中特別理想爲含有聚醇成分全部量之60至 1 00質量%的熔點爲〇°C以下之非晶性聚碳酸酯系聚醇。從 耐割傷性高且吸水性或儲存彈性模數也爲適度之觀點’較 佳爲將如此之聚碳酸酯系聚醇作爲原料之聚胺甲酸酯系樹 脂。 熔點爲〇°c以下之非晶性聚碳酸酯系聚醇的具體例’例 如,可列舉:聚(3·甲基-1,5-伸戊基碳酸酯)二醇、聚(甲 基-1,8 -八亞甲基碳酸酯)二醇等之具有分枝之聚碳酸酯聚 醇;聚六亞甲基碳酸酯二醇、聚五亞甲基碳酸酯二醇、聚 四亞甲基碳酸酯二醇办聚九亞甲基碳酸酯二醇、聚環己烷 碳酸酯等之聚碳酸酯系聚醇。 聚醇成分不論單獨使用或組合二種以上而使用皆可。 從藉由賦予適度彈性而能夠抑制刮傷發生之觀點’源 自聚胺甲酸酯系樹脂中之聚醇成分的構造單位之含有比例 較佳爲30至65質量%,進一步較佳爲40至60質量% ’特 別理想爲45至55質量%。 還有,含有源自具有親水性基之聚醇成分的構造單位 之聚胺甲酸酯系樹脂係對硏磨糊之潤濕性將提高,但是具 有吸水率變得過高之傾向。爲了獲得使在上述的50 °C飽和 吸水時之吸水率成爲如0.2至5質量%之聚胺甲酸酯系樹 脂,較佳爲使具有親水性基之聚醇成分的共聚合比例成爲 〇 · 1至1 0質量%,進一步較佳成爲〇. 5至5質量%。藉由以 如此之含有比例而使具有親水性基之聚醇成分作爲構造單 位而含有,能夠一邊將因吸水所導致的膨潤軟化抑制至最 小限度且一邊提高吸水率或潤濕性。另外,爲了抑制使吸 -19- 201120269 水率變得過高,較佳爲與吸水性低的聚醇成分相組合而使 用。如此之聚醇的具體例,例如,可列舉進行下列之聚碳 酸酯系聚醇共聚合之聚碳酸酯聚醇等:聚伸丁基癸酸酯二 醇、聚(3-甲基-1,5-伸戊基己二酸酯)二醇、聚(3_甲基 -1,5-伸戊基癸二酸酯)二醇等之聚酯系聚醇及其共聚物; 聚(3_甲基-1,5-伸戊基碳酸酯)二醇、聚(甲基— is —八亞 甲基碳酸酯)二醇、聚六亞甲基碳酸酯二醇、聚五亞甲基 碳酸酯二醇、聚四亞甲基碳酸酯二醇、聚九亞甲基碳酸酯 二醇、聚環己烷碳酸酯二醇等。 有機聚異氰酸酯之具體例,例如,可列舉:六亞甲基 二異氰酸酯、異佛酮二異氰酸酯、降莰烷二異氰酸酯、4,4,-二環己基甲烷二異氰酸酯等之脂肪族或脂環族二異氰酸酯 等之無黃變型二異氰酸酯;2,4 -甲苯基二異氰酸醋、2,6-甲苯基二異氰酸酯、4,4’-二苯基甲烷二異氰酸酯、二甲苯 二異氤酸酯聚胺甲酸酯等之芳香族二異氰酸酯等。另外必 要時也可以倂用3官能異氰酸酯或4官能異氰酸酯等之多 官能異氰酸酯。此等異氰酸酯可以單獨使用,也可以組合 二種以上而使用。從對極細纖維之接著性高且提高極細纖 維之集束力’另外,可以獲得硬度高的硏磨墊之觀點,此 等異氰酸酯之中’較佳爲4,4’-二環己基甲院二異氰酸酯、 2,4-甲苯基二異氰酸酯、2,6-甲苯基二異氰酸酯、4,4,-二苯 基甲院一異氰酸酯、—甲苯二異氰酸酯等之脂環式二異截 酸酯或芳香族二異氰酸酯。 鏈延長劑之具體例,例如,可列舉:肼、乙二胺、丙 二胺、六亞甲基二胺、九亞甲基二胺、二甲苯二胺、異佛 -20- 201120269 酮二胺、哌啶及其衍生物、己二酸二醯肼、間苯二甲酸二 酿肼等之二胺類;二乙三胺等之三胺類;三乙四胺等之四 胺類;乙二醇、丙二醇、1,4-丁二醇、1,6-己二醇、1,4-雙 (P-羥乙氧基)苯、1,4-環己烷二醇等之二醇類;三羥甲基 丙烷等之三醇類;季戊四醇等之五醇類;胺乙基醇、胺丙 基醇等之胺基醇類等》此等鏈延長劑可以單獨使用或是也 可以組合二種以上而使用》從對纖維之接著性高,另外’ 可以獲得硬度爲適當的硏磨墊之觀點,此等鏈延長劑之 中,較佳爲從肼、哌啶、六亞甲基二胺、異佛酮二胺及其 衍生物、二乙三胺等之三胺之中而組合二種以:上而使用。 另外,與鏈延長劑一起,也可以倂用乙胺、丙胺、丁胺等 之單胺類;4-胺基丁酸、6-胺基己酸等之含有羧基之單胺 化合物;甲醇、乙醇、丙醇、丁醇等之單醇類。而且,藉 由倂用.2,2-雙(羥甲基)丙酸、2,2-雙(羥甲基)丁酸、2,2-雙(羥甲基)戊酸等之含有羧基之二醇等,將羧基等之離 子性基導入聚胺甲酸酯系彈性體之骨架中而能夠進一步使 對水之潤濕性提高。 聚胺甲酸酯系樹脂係用以控制吸水率或儲存彈性模 數,較佳爲藉由添加分子內含有2個以上可與形成聚胺甲 酸酯之單體單位所具有的官能基進行反應之官能基的交聯 劑、或聚異氰酸酯系化合物、多官能嵌段異氰酸酯系化合 物等之自我交聯性化合物而形成交聯教構造。單體單位所 具有的官能基與交聯劑的官能基之組合,可列舉:羧基與 曙唑啉基、羧基與碳二醯亞胺基、羧基與環氧基、羧基與 環碳酸酯基、羧基與氮雜環丙烷基、羧基與肼衍生物或醯 -21 - 201120269 肼衍生物等。從交聯形成爲容易且所獲得之硏磨墊之剛性 或耐磨損性爲優異之觀點,於此等組合之中,特別理想爲 具有羧基之單體單位與具有曙唑啉基 '碳二醯亞胺基或環 氧基之交聯劑的組合;具有羥基或胺基之單體單位與具有 嵌段異氰酸酯基之交聯劑的組合;及具有羧基之單體單位 與肼衍生物或醯肼衍生物的組合。具有碳二醯亞胺基之交 聯劑,例如,可列舉:日清紡績股份有限公司製「Carbodilite E-01」、「Carbodilite E-02」、「Carbodilite V-02」等之 水分散碳二醯亞胺系化合物。另外,具有噚唑啉基之交聯 劑,例如,可列舉:日本觸媒股份有限公司製「Ε ρ 〇 c r 〇 s s K-2010E」、「Epocross K-2020E j 、 「Epocross WS- 500」 等之水分散輕啉系化合物。相對於聚胺甲酸酯系樹脂而 言,交聯劑之有效成分較佳爲1至20質量%。更佳爲1.5 至1 0質量%。 於不損害本發明之效果的範圍內,聚胺甲酸酯系樹脂 也可以更含有滲透劑、消泡劑、潤滑劑、撥水劑、撥油劑、 增黏劑、增量劑、硬化促進劑、抗氧化劑、紫外線吸收劑、 防黴劑、發泡劑、聚乙烯醇、羧甲基纖維素等之水溶性高 分子化合物、染料、顏料、無機微粒等。 接著,針對本實施形態之硏磨墊之製造方法之一例詳 細加以說明。 (1 )棉網製造步驟 於本製造方法中,首先製造由進行水溶性熱可塑性樹 脂與非水溶性熱可塑性樹脂之熔融紡紗所獲得之海島型複 合纖維所構成的長纖維棉網。還有,於本實施形態中,將 -22- 201120269 海島型複合纖維作爲用以形成極細纖維之複合纖維使用, 也可以使用多層積層型截面纖維等之習知的極細纖維發生 型纖維以取代海島型複合纖維。 '海島型複合纖維係分別進行水溶性熱可塑性樹脂、及 與水溶性熱可塑性樹脂相溶性低的非水溶性熱可塑性樹脂 之溶融紡紗後,藉由使其複合化所獲得。然後,藉由從如 此之海島型複合纖維進行水溶性熱可塑性樹脂之溶解去除 或分解去除而形成極細纖維。從工業性之觀點,海島型複 合纖維之寬度較佳爲0.5至3分特克斯,進一步較佳爲0.8 至2.5分特..克斯。 水溶性熱可塑性樹脂係藉由水或鹼水溶液、酸水溶液 等之水溶液,於加熱條件下或加壓條件下,予以溶解去除 或分解去除之聚合物。水溶性熱可塑性樹脂之具體例,例 如,可列舉:聚乙烯醇(PVA) 、PVA系共聚物、共聚合 聚氧乙烯聚乙二醇及/或含有磺酸鹼金屬鹽之化合物等之 改性聚酯等。此等水溶性熱可塑性樹脂之中,從具有優異 的對水的溶解性之觀點,較佳爲PVA或PVA系共聚物。 另外,非水溶性熱可塑性樹脂係用以形成上述之極細 纖維的各種聚合物,並無特別限定而能夠使用。還有,非 水溶性熱可塑性樹脂也可以含有各種添加劑。添加劑之具 體例可列舉:觸媒、著色防止劑、耐熱劑、難燃劑、潤滑 劑、防污劑、螢光增白劑、消豔劑、著色劑、光澤改良劑、 除電劑、抗菌劑、防蟎劑、無機微粒等。 藉由熔融紡紗水溶性熱可塑性樹脂與非水溶性熱可塑 性樹脂而予以複合化之後,針對藉由紡紗黏合法而形成長 -23- 201120269 纖維棉網之方法,以下,詳細加以說明。 首先,藉由分別各自的擠出劑而熔融混煉水 塑性樹脂及非水溶性熱可塑性樹脂,同時使從各 紡紗噴嘴而使熔融樹脂之紗束同時噴出。然後, 複合噴嘴而使所噴出的紗束使其複合後,從紡紗 孔使其噴出而形成海島型複合纖維。從容易縮小 截面積且可以獲得纖維密度高的纖維束之觀點, 合纖維中之島數較佳爲5至400 0島/纖維,進一 10至1〇〇〇島/纖維。 利用冷卻裝置以冷卻海島型複合纖維後,利 射/噴嘴等之抽氣裝置,藉由速度相當於1 00 0至 鐘之拉取速度的高速氣流而成爲目的之纖度的方 拉伸。之後,藉由將所拉伸的複合纖維堆積於移 集面上而形成有長纖維棉網。還有此時,必要時 分壓黏所堆積的長纖維棉網。從工業性之觀點, 網之基重量(單位面積質量)較佳爲20至500 g/m: (2)棉網纏繞步驟 接著,針對藉由重疊數片纏繞所獲得之長纖 形成纏繞棉網之棉網纏繞步驟加以說明。纏繞棉 針扎或高壓水流處理等之習知不織布製造方法, 纖維棉網進行纏繞處理而可以獲得。 首先,將防止針折斷油劑、抗靜電油劑、纏 劑等之矽氧烷系油劑或礦物油系油劑賦予至長纖 還有,爲了使基重不均減低,也可以藉由交叉包 疊二片以上之纖維棉網且賦予油劑。其後,藉由 溶性熱可 不相同的 藉由利用 頭之噴嘴 單纖維的 海島型複 步較佳爲 用空氣噴 6000m/分 式來予以 動式之收 也可以部 長纖維棉 ^之範圍。 維棉網而 網係利用 藉由對長 繞改善油 維棉網。 覆材而重 針扎而進 -24- 201120269 行使纖維三次元纏繞的纏繞處理。藉由進行針扎而可以獲 得高的纖維密度且難以引起纖維脫落之纏繞棉網。於針扎 中,藉由改變表面側與背面側之針扎條件,能夠對表面側 與背面側之纖維束密度賦予差異。 在針扎之油劑的種類或量、針形狀、針深度、扎針次 等之針條件係使成爲硏磨面之表面側的纖維束密度、與成 爲固定面之背面側的纖維束密度成爲適切之密度差的方式 來予以適當選擇。 針之鉤數係從例如1至9鉤之中所選出,於未發生針 折斷之範圍越多越好..。另外,針扎..深度較佳設爲在棉網表 面針扎後之模樣並不明顯的範圍。具體而言,例如,可列 舉如下之條件:初期係利用6至9鉤之針而以5至2 5 mm 之深度進行針扎處理,後半則利用3至6鉤之針而作成深 度0.1至15 mm來集中纏繞表.面側之纖維。另外,.針扎數 係根據針形狀、油劑之種類及用量等而適當選擇,具體而 言,較佳約爲5 00至5000扎/cm2,另外,相對於從背面側 之扎數,較佳爲以1 . 5至2倍以上而處理從表面側之扎數。 另外,與背面側作一比較,表面側較佳使用針之扎數較多 的針,針之扎深度越淺越好。另外,較佳爲提高扎數而藉 由針之鉤而選擇性地纏繞表面側之纖維。 另外,從可以獲得纖維密度高的纏繞棉網之觀點,針 扎後之纏繞棉網的基重較佳成爲針前之長纖維棉網基重的 1.2倍以上,進一步較佳爲1.5倍以上的方式來進行。纏繞 棉網的基重係按照成爲目的之硏磨墊的厚度等而予以適當 選擇,從具有優異的操作性之觀點,較佳爲100至1 500 g/m2 -25- .201120269 之範圍。 另外,從可以獲得形態保持性良好、纖維之脫落少且 纖維密度高的纏繞棉網之觀點,纏繞棉網的層間剝離強度 較佳爲2kg/2.5cm以上,進一步較佳爲4kg/2.5cm以上。 還有,層間剝離強度係成爲三次元纏繞程度的目標。層間 剝離強度過小之情形下,纖維纏繞體之纖維密度並不充分 高。另外,雖然纏繞不織布之層間剝離強度的上限並未予 以特別限定,從纏繞處理效率之觀點,較佳約爲3 0 kg/2.5 cm以下。 (3)濕熱收縮處理步驟 接著,藉由使纏繞棉網濕熱收縮而提高纏繞棉網之纖 維密度及纏繞程度。還有,於本步驟中,與含有短纖維之 纏繞棉網濕熱收縮之情形作一比較,藉由使含有長纖維之 纏繞棉網濕熱收縮更能夠使纏繞棉網大幅收縮,因此,極 細纖維之纖維密度變得緻密。濕熱收縮處理較佳爲藉由水 蒸氣加熱而進行。 水蒸氣加熱條件係環境氣溫較佳爲60至130 °C之範 圍,相對濕度較佳爲75 %以上,相對濕度進一步較佳爲80% 以上’進行60至600秒鐘之加熱處理。從能夠以高收縮率 而使纏繞棉網收縮之觀點,較佳爲如此加熱條件之情形。 還有,相對濕度過低之情形下,藉由接觸於纖維之水分將 快速乾燥,具有收縮將變得不充分之傾向。 濕熱收縮處理係使纏繞棉網之面積收縮率較佳成爲 3 5 %以上,進一步較佳成爲4 0 %以上的方式來使其收縮。如 此方式’藉由以高的收縮率而使其收縮,纖維密度將變得 -26- 201120269 緻密。面積收縮率之上限並未予以特別限定,從收縮之限 度或處理效率之觀點,較佳約爲80%。還有,面積收縮率 (% )係藉由下式(1 )所算出: 面積收縮率(%)=(收縮處理前之片材面的面積_ 收縮處理後之片材面的面積)/收縮處理前之片材面的面積 X 1 00 ... ( 1 ) ° 如此方式,予以濕熱收縮處理之纏繞棉網係藉由於海 島型複合纖維之熱變形溫度以上之溫度予以加熱輥或加熱 壓縮,進一步也可以提高纖維密度。此時,藉由對表面側 與、背面側,利用不同的條件進行加熱壓縮,也能夠使纖維& 束之密度梯度形成。藉由加熱輥所進行的壓縮條件,例如, 可列舉:輥溫度爲110至150 °c、輥壓力爲0.05至0.4MPa 之條件。收縮處理後之纏繞棉網的基重對收縮處理前之纏 繞棉網的基重較佳爲1.2至4倍,進一步較佳爲1.5至4 倍。Further, as shown in Fig. 2, the plurality of fiber bundles 1b are preferably bonded to each other by the polymer elastic body 2 existing on the outer side of the fiber bundle 1b, and are present in a bulk. In this manner, the shape stability of the honing pad is improved and the honing stability is improved by bonding the fiber bundles to each other. Further, the bundle state of the ultrafine fibers and the state in which the fiber bundles are bonded to each other can be confirmed by an electron micrograph of the cross section of the honing pad. J is a polymer elastic which is infiltrated into the inside of the ultrafine fibers and the polymer fibers of the ultrafine fiber bundles. The body is preferably non-porous. Further, the term "non-porous" means a state in which a plurality of independent bubbles of a polymer elastomer having a porous shape or a sponge shape (hereinafter, also referred to simply as a porous shape) are not substantially present. Specifically, for example, it means a polymer elastomer having many fine closed cells which are not obtained by solidifying a solvent-based polyurethane. In the case where the polymer elastomer to be bundled or bonded is non-porous, the honing stability is increased, and since the swarf or the swarf during honing becomes less likely to accumulate in the void, it is less likely to be worn. And maintain a high honing rate for a long time. Further, since the bonding strength to the ultrafine fibers is increased, the occurrence of scratches due to the falling off of the fibers can be further suppressed. Furthermore, since a higher rigidity can be obtained, a honing pad having more excellent flattening performance can be obtained. The D hardness of the honing surface 3 of the honing pad 10 is preferably from 25 to 50, further preferably from 30 to 49, particularly preferably from 31 to 47. When the D hardness is in the range of -15-.201120269, it is less susceptible to the surface shape of the honed substrate, and an optimum rigidity honing pad can be obtained from the viewpoint of planarization performance. Next, the polymer elastomer to be applied inside the nonwoven fabric will be described in detail. The type of the polymeric elastomer to be imparted inside the nonwoven fabric is not particularly limited. Specific examples of the polymer elastomer include, for example, a polyurethane resin, a polyamide resin, a (meth)acrylate resin, a (meth)acrylate-styrene resin, and a (methyl group). ) acrylate/acrylonitrile resin, (meth) acrylate-olefin resin, (meth) acrylate-(hydrogenated) isoprene resin, (meth) propyl ester-butyl Ethylene resin, styrene-butadiene resin, styrene-hydrogenated isoprene resin, acrylonitrile-butadiene resin, acrylonitrile-butadiene-styrene resin, vinyl acetate resin An elastomer composed of a (meth) acrylate, a vinyl acetate resin, an ethylene-vinyl acetate resin, an ethylene-olefin resin, a fluorinated resin, a fluorine resin, or a polyester resin. The polymeric elastomers may be used singly or in combination of two or more. Among these high molecular elastomers, hydrogen bonding polymer elastomers such as a polyurethane resin, a polyamide resin, and a polyvinyl alcohol resin are particularly preferable. Further, a polymer elastomer in which a hydrogen-bonded polymer elastic system is crystallized or aggregated by hydrogen bonding has a high binding property to an ultrafine fiber and a binding bond to an ultrafine fiber. Further, the polyurethane resin is used to bundle extremely fine fibers or bonded fiber bundles with particularly excellent adhesion, and to improve the hardness of the honing pad, and to have excellent stability over time. The point of view is particularly desirable. The glass transition temperature of the polymeric elastomer is preferably -lot or less, preferably from -16 to 201120269, preferably below -15 °C. In the case where the glass transition temperature is too high, the high molecular elastomer is fragile and it is feared that it will fall off during honing. The glass transition temperature was calculated from the peak temperature of the loss elastic modulus measured by the dynamic viscoelasticity tensile mode. The glass transition temperature depends on the peak temperature of dispersion of the polymeric elastomer. For example, in the case of a polyurethane resin, the glass transition temperature can be made -1 〇 °c or less by adjusting the composition of the polyol which is a soft component or the ratio of the hard component to the soft component. Further, the polymeric elastomer preferably has the following elasticity. The storage elastic modulus (G') of the polymeric elastomer at 23 ° C and 50 ° C is 90 to 900 MPa, more preferably from the viewpoint that the rigidity of the honing pad becomes high and the elasticity is excellent. 20 to 800 MPa. In addition, from the viewpoint of excellent honing stability, the ratio of the storage elastic modulus (G23') at 23 °C to the storage elastic modulus (G5〇') at 50 °C (G23 7 G50') It is 4 or less, More preferably, it is 3 or less and 1/3 or more. Further, from the viewpoint of excellent liquid retention and honing stability of the mash, the water absorption of the polymer elastic system at 50 ° C for saturated water absorption is preferably from 0.2 to 5% by mass, further preferably 0.5. Up to 3 mass%. Here, a representative example of the polymeric elastomer will be described in detail with respect to the polyurethane resin. Examples of the polyurethane resin include various polyurethane resins obtained by reacting a polymer polyol, an organic polyisocyanate, a chain extender, and the like with a predetermined molar ratio. Specific examples of the high molecular polyol include, for example, polyalcohol polyalcohols such as polyethylene glycol, polypropylene glycol, and polytetramethylene glycol 'poly(.methyltetramethylene glycol). Copolymer; polybutylene adipate diol, polybutylene terephthalate diol, polyhexamethylene dicarboxylate diol, poly(3-methyl-l,5--17- 201120269 pentyl adipate diol, poly(3-methyl-1,5-exopentyl sebacate) diol, isophthalic acid copolymerized polyol, terephthalic acid copolymerization Polyols and copolymers thereof, such as alcohol, cyclohexanol copolymerized polyalcohol, polycaprolactone diol, etc.; polyhexamethylene carbonate diol, poly(3-methyl·1,5· Pentyl carbonate) diol, polypentamethylene carbonate diol, polytetramethylene carbonate diol, poly(methyl-1,8-octamethylene carbonate) diol, poly-Jiu A polycarbonate-based polyalcohol such as methyl carbonate diol or polycyclohexane carbonate or a copolymer thereof; a polyester carbonate polyalcohol or the like. Further, if necessary, a polyfunctional alcohol such as a trifunctional alcohol such as trimethylolpropane or a tetrafunctional alcohol such as pentaerythritol may be used, or ethylene glycol, propylene glycol or 1,4-butanediol may be used. Short-chain alcohol such as 6-hexanediol. In addition, a polyol component having a hydrophilic group such as a carboxyl group, a sulfonic acid group, a hydrocarbon group, or a carbon number of 5 or less, particularly a carbon number of 3 or less, is contained as a resin structural unit, and can be contained. The dispersibility of the aqueous medium or the wettability to the mash is improved. Specific examples of the polyol component having a carboxyl group include 2,2-bis(hydroxymethyl)propionic acid, 2,2-bis(hydroxymethyl)butyric acid, and 2,2-bis(hydroxymethyl)pentane. a diol containing a carboxyl group such as an acid. Further, specific examples of the polyalcohol component having a polyalkylene glycol group having 5 or less carbon atoms include polyethylene glycol, polypropylene glycol, and copolymers thereof. Further, the polyalcohol component is a polycarbonate-based polyalcohol having a glass transition temperature of -10 ° C or lower and further having a glass transition temperature of -20 ° C or lower, and the polyurethane fatty acid is allowed to contain carbon in the polycondensation. , and the other is more concentrated than the alcohol, and the lower alcohol ester is formed by the poly-acid 0 °c carbon-1. Chain degree wants to straighten the temperature, shifts the alcohol to the special glass, and the glass ester ester is a fatty acid carbon tree elastic polymer high ester ring -18 - 201120269 Ester polyalcohol, especially ideally containing polyol The melting point of 60 to 100% by mass of the total amount is an amorphous polycarbonate-based polyol having a melting point of 〇 ° C or less. From the viewpoint of high cut resistance and water absorption or storage elastic modulus, it is preferred that the polycarbonate-based polyalcohol is used as a raw material of a polyurethane resin. Specific examples of the amorphous polycarbonate-based polyalcohol having a melting point of 〇°c or less 'for example, poly(3·methyl-1,5-exopentyl carbonate) diol, poly(methyl-) Branched polycarbonate polyol such as 1,8-octamethylene carbonate) diol; polyhexamethylene carbonate diol, polypentamethylene carbonate diol, polytetramethylene The carbonate diol is a polycarbonate-based polyalcohol such as polyhexamethylene carbonate diol or polycyclohexane carbonate. The polyhydric alcohol component may be used singly or in combination of two or more. From the viewpoint of suppressing the occurrence of scratches by imparting moderate elasticity, the content ratio of the structural unit derived from the polyalkate resin in the polyurethane resin is preferably from 30 to 65 mass%, more preferably from 40 to 60% by mass 'particularly ideally 45 to 55 mass%. In addition, the polyurethane resin containing a structural unit derived from a polyol component having a hydrophilic group improves the wettability of the mash, but tends to have an excessively high water absorption. In order to obtain a polyurethane resin having a water absorption ratio of from 0.2 to 5% by mass in the above-mentioned saturated water absorption at 50 ° C, it is preferred that the copolymerization ratio of the polyol component having a hydrophilic group is 〇· 1 to 10% by mass, further preferably 〇. 5 to 5% by mass. When the polyol component having a hydrophilic group is contained as a structural unit in such a content ratio, it is possible to improve the water absorption rate or the wettability while suppressing the swelling softening due to water absorption to a minimum. Further, in order to suppress the water content of the absorption -19-201120269 from becoming too high, it is preferably used in combination with a polyol component having a low water absorbability. Specific examples of such a polyhydric alcohol include polycarbonate polyalcohols obtained by copolymerizing the following polycarbonate-based polyols: poly(butyl phthalate diol), poly(3-methyl-1, Polyester-based polyalcohols such as 5-extended pentyl adipate diol, poly(3-methyl-1,5-exopentyl sebacate) diol, and the like; poly(3_ Methyl-1,5-extended pentyl carbonate diol, poly(methyl-is-octamethyl carbonate) diol, polyhexamethylene carbonate diol, polypentamethylene carbonate A diol, a polytetramethylene carbonate diol, a polyhexamethylene carbonate diol, a polycyclohexane carbonate diol, or the like. Specific examples of the organic polyisocyanate include aliphatic or alicyclic groups such as hexamethylene diisocyanate, isophorone diisocyanate, norbornane diisocyanate, and 4,4,-dicyclohexylmethane diisocyanate. Non-yellowing diisocyanate such as diisocyanate; 2,4-tolyl diisocyanate, 2,6-tolyl diisocyanate, 4,4'-diphenylmethane diisocyanate, xylene diisocyanate An aromatic diisocyanate such as a polyurethane or the like. Further, a polyfunctional isocyanate such as a trifunctional isocyanate or a tetrafunctional isocyanate may be used as necessary. These isocyanates may be used singly or in combination of two or more. From the viewpoint of high adhesion to the ultrafine fibers and an increase in the bundle force of the ultrafine fibers, in addition, a viewpoint of a high hardness honing pad can be obtained, and among these isocyanates, '4,4'-dicyclohexylylene diisocyanate is preferred. , 2,4-tolyl diisocyanate, 2,6-tolyl diisocyanate, 4,4,-diphenylmethyl isocyanate, toluene diisocyanate, etc., alicyclic diisalate or aromatic Isocyanate. Specific examples of the chain extender include, for example, anthracene, ethylenediamine, propylenediamine, hexamethylenediamine, nonamethylenediamine, xylenediamine, and isophora-20-201120269 ketodiamine , piperidine and its derivatives, diammonium adipate, diamines such as dibasic phthalic acid; triamines such as diethylenetriamine; tetraamines such as triethylenetetramine; a glycol such as an alcohol, propylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,4-bis(P-hydroxyethoxy)benzene or 1,4-cyclohexanediol; a triol such as trimethylolpropane; a pentaol such as pentaerythritol; an amine alcohol such as an amine ethyl alcohol or an aminopropyl alcohol; etc. These chain extenders may be used singly or in combination of two The above-mentioned "use" has high adhesion to fibers, and the viewpoint of obtaining a honing pad having a suitable hardness is preferable. Among these chain extenders, hydrazine, piperidine, hexamethylenediamine, and the like are preferable. Among the isophorone diamines and derivatives thereof, triamines such as diethylenetriamine, and the like, two of them are used in combination: Further, together with the chain extender, a monoamine such as ethylamine, propylamine or butylamine; a monoamine compound having a carboxyl group such as 4-aminobutyric acid or 6-aminohexanoic acid; methanol or ethanol; Monools such as propanol and butanol. Further, by using ruthenium containing 2,2-bis(hydroxymethyl)propionic acid, 2,2-bis(hydroxymethyl)butyric acid, 2,2-bis(hydroxymethyl)pentanoic acid or the like In the diol or the like, an ionic group such as a carboxyl group is introduced into the skeleton of the polyurethane elastomer, and the wettability to water can be further improved. The polyurethane resin is used to control the water absorption rate or the storage elastic modulus, and it is preferred to carry out a reaction by adding two or more functional groups which can be combined with the monomer unit forming the polyurethane. A functional crosslinker or a self-crosslinkable compound such as a polyisocyanate compound or a polyfunctional block isocyanate compound forms a crosslinked structure. Examples of the combination of the functional group of the monomer unit and the functional group of the crosslinking agent include a carboxyl group and an oxazoline group, a carboxyl group and a carbodiimide group, a carboxyl group and an epoxy group, a carboxyl group and a cyclic carbonate group, a carboxyl group and an aziridine group, a carboxyl group and a hydrazine derivative or a hydrazine-21 - 201120269 hydrazine derivative. From the viewpoint that the crosslinking is formed easily and the rigidity or abrasion resistance of the obtained honing mat is excellent, among these combinations, it is particularly preferable that the monomer unit having a carboxyl group and the oxazoline group 'carbon two a combination of a hydrazine or an epoxy group crosslinking agent; a combination of a monomer unit having a hydroxyl group or an amine group and a crosslinking agent having a blocked isocyanate group; and a monomer unit having a carboxyl group and an anthracene derivative or an anthracene A combination of anthraquinone derivatives. For example, a water-dispersible carbon dioxide such as "Carbodilite E-01", "Carbodilite E-02", or "Carbodilite V-02" manufactured by Nisshinbo Co., Ltd. can be used as the crosslinking agent having a carbodiimide group. Imine compound. In addition, examples of the crosslinking agent having an oxazoline group include "Ερ 〇cr 〇ss K-2010E" manufactured by Nippon Shokubai Co., Ltd., "Epocross K-2020E j", "Epocross WS-500", and the like. The water is dispersed in a light morpholino compound. The active ingredient of the crosslinking agent is preferably from 1 to 20% by mass based on the polyurethane resin. More preferably, it is 1.5 to 10% by mass. The polyurethane resin may further contain a penetrating agent, an antifoaming agent, a lubricant, a water repellent agent, an oil repellent agent, a tackifier, a bulking agent, and a hardening promotion, within a range not impairing the effects of the present invention. A water-soluble polymer compound such as a solvent, an antioxidant, an ultraviolet absorber, an antifungal agent, a foaming agent, polyvinyl alcohol or carboxymethyl cellulose, a dye, a pigment, an inorganic fine particle or the like. Next, an example of a method of manufacturing the honing pad of the present embodiment will be described in detail. (1) Cotton web manufacturing step In the present production method, a long fiber web composed of sea-island composite fibers obtained by melt spinning of a water-soluble thermoplastic resin and a water-insoluble thermoplastic resin is first produced. In addition, in the present embodiment, the -22-201120269 sea-island composite fiber is used as a composite fiber for forming ultrafine fibers, and a conventional ultrafine fiber-generating fiber such as a multilayer laminated fiber may be used instead of the island. Type composite fiber. The 'island-type composite fiber system is obtained by melt-spinning a water-soluble thermoplastic resin and a water-insoluble thermoplastic resin having low compatibility with a water-soluble thermoplastic resin, and then combining them. Then, the ultrafine fibers are formed by dissolving or decomposing and removing the water-soluble thermoplastic resin from the island-in-the-sea type composite fiber. From the industrial point of view, the width of the island-in-the-sea composite fiber is preferably from 0.5 to 3 dtex, more preferably from 0.8 to 2.5 dtex. The water-soluble thermoplastic resin is a polymer which is dissolved or removed by decomposition in an aqueous solution such as water or an aqueous alkali solution or an aqueous acid solution under heating or under a pressurized condition. Specific examples of the water-soluble thermoplastic resin include, for example, polyvinyl alcohol (PVA), a PVA-based copolymer, a copolymerized polyoxyethylene polyethylene glycol, and/or a compound containing an alkali metal sulfonate. Polyester, etc. Among these water-soluble thermoplastic resins, PVA or PVA-based copolymers are preferred from the viewpoint of having excellent solubility in water. Further, the water-insoluble thermoplastic resin is a polymer which is used to form the above-mentioned ultrafine fibers, and can be used without particular limitation. Further, the water-insoluble thermoplastic resin may contain various additives. Specific examples of the additive include a catalyst, a coloring preventive agent, a heat resistant agent, a flame retardant, a lubricant, an antifouling agent, a fluorescent whitening agent, a deodorant, a coloring agent, a gloss improving agent, a static eliminating agent, and an antibacterial agent. , anti-caries agents, inorganic particles, etc. The method of forming a long -23-201120269 fiber cotton web by a spunbonding method by a melt-spinning water-soluble thermoplastic resin and a water-insoluble thermoplastic resin is hereinafter described in detail. First, the water-plastic resin and the water-insoluble thermoplastic resin are melt-kneaded by the respective extrudates, and the yarn bundle of the molten resin is simultaneously ejected from each of the spinning nozzles. Then, the nozzles are combined and the bundle of the discharged yarns are combined, and then ejected from the spinning holes to form an island-in-the-sea type composite fiber. From the viewpoint of easily reducing the cross-sectional area and obtaining a fiber bundle having a high fiber density, the number of islands in the fiber is preferably from 5 to 400 islands/fiber, and from 10 to 1 island/fiber. After the sea-island type composite fiber is cooled by the cooling device, the air suction device such as the radiation/nozzle is stretched by the high-speed air flow having a speed equivalent to a drawing speed of 100 to 10 seconds. Thereafter, a long fiber web was formed by depositing the drawn composite fiber on the transfer surface. At this time, if necessary, the long-fiber cotton web deposited by the pressure is divided. From the industrial point of view, the basis weight (mass per unit area) of the net is preferably from 20 to 500 g/m: (2) Cotton web winding step Next, a twisted cotton web is formed for the long fibers obtained by overlapping several sheets of winding The cotton web winding step is explained. A conventional non-woven fabric manufacturing method such as winding cotton needle or high-pressure water flow treatment can be obtained by winding a fiber cotton web. First, a non-anethanane-based oil or a mineral oil-based oil agent such as a needle-breaking oil-reducing agent, an antistatic oil agent, and a sizing agent is applied to the long fiber, and in order to reduce the basis weight unevenness, it is also possible to cross Two or more fiber webs are wrapped and an oil agent is added. Thereafter, the sea-island type of the single fiber by the nozzle of the head may be different by the heat of the heat, and it is preferable to use the air jet of 6000 m/min to obtain the range of the fiber cotton. The cotton mesh is used by the net system to improve the oil net by long winding. Covering the material and heavy needles into the -24- 201120269 Exercise the winding of the fiber three-dimensional winding. By winding the needle, it is possible to obtain a wound web which has a high fiber density and is difficult to cause the fibers to fall off. In the needle sticking, by changing the needle-forming conditions on the front side and the back side, it is possible to impart a difference in the fiber bundle density between the front side and the back side. In the needle condition such as the type or amount of the oil agent to be needled, the shape of the needle, the depth of the needle, and the needle diameter, the density of the fiber bundle on the surface side of the honing surface and the density of the fiber bundle on the back side of the fixed surface are appropriate. The difference in density is appropriately selected. The number of hooks of the needle is selected from, for example, 1 to 9 hooks, and the more the number of needle breaks does not occur, the better... In addition, the needle depth is preferably set to a range in which the appearance of the surface of the cotton web is not obvious. Specifically, for example, the following conditions may be mentioned: the initial stage uses a 6 to 9 hook needle to perform a needle sticking process at a depth of 5 to 25 mm, and the latter half uses a 3 to 6 hook needle to make a depth of 0.1 to 15 Mm to concentrate the winding table. The fibers on the side. Further, the number of needles is appropriately selected depending on the shape of the needle, the type and amount of the oil, and the like, and specifically, it is preferably about 500 to 5,000 Å/cm 2 , and the number of the ties from the back side is Preferably, the number of strands from the surface side is treated by 1.5 to 2 times or more. Further, in comparison with the back side, it is preferable to use a needle having a large number of needles on the surface side, and the shallower the depth of the needle, the better. Further, it is preferable to increase the number of the strands and selectively wind the fibers on the surface side by the hooks of the needles. In addition, from the viewpoint of obtaining a wound cotton web having a high fiber density, the basis weight of the wound cotton web after needle sticking is preferably 1.2 times or more, more preferably 1.5 times or more, based on the basis weight of the long fiber web before the needle. Way to proceed. The basis weight of the entangled cotton web is appropriately selected in accordance with the thickness of the honing mat to be used, etc., and is preferably in the range of 100 to 1,500 g/m2 to 25-.201120269 from the viewpoint of excellent workability. Further, from the viewpoint of obtaining a wound web having good form retention, less fiber shedding, and high fiber density, the interlaminar peel strength of the wound web is preferably 2 kg/2.5 cm or more, and more preferably 4 kg/2.5 cm or more. . Also, the interlaminar peel strength is the target of the degree of three-dimensional winding. In the case where the interlaminar peel strength is too small, the fiber density of the filament wound body is not sufficiently high. Further, the upper limit of the interlaminar peeling strength of the entangled nonwoven fabric is not particularly limited, and is preferably about 30 kg/2.5 cm or less from the viewpoint of the winding treatment efficiency. (3) Wet heat shrinkage treatment step Next, the fiber density and the degree of entanglement of the wound cotton web are increased by moist heat shrinkage of the wound cotton web. In addition, in this step, compared with the case of wet heat shrinkage of the wound cotton web containing short fibers, the wet cotton shrinkage of the wrapped cotton web containing long fibers can further shrink the wound cotton web, so that the ultrafine fibers are The fiber density becomes dense. The moist heat shrinkage treatment is preferably carried out by steam heating. The steam heating condition is preferably in the range of 60 to 130 ° C, the relative humidity is preferably 75% or more, and the relative humidity is more preferably 80% or more. The heat treatment is carried out for 60 to 600 seconds. From the viewpoint of being able to shrink the wound web at a high shrinkage ratio, it is preferable to carry out such heating conditions. Further, in the case where the relative humidity is too low, the moisture which is in contact with the fibers is rapidly dried, and the shrinkage tends to be insufficient. The wet heat shrinkage treatment is such that the area shrinkage ratio of the wound web is preferably 35% or more, and more preferably 40% or more. In this way, the fiber density will become dense by -26-201120269 by shrinking it with a high shrinkage rate. The upper limit of the area shrinkage ratio is not particularly limited, and is preferably about 80% from the viewpoint of the shrinkage limit or the treatment efficiency. Further, the area shrinkage ratio (%) is calculated by the following formula (1): Area shrinkage ratio (%) = (area of sheet surface before shrinkage treatment _ area of sheet surface after shrinkage treatment) / shrinkage The area of the sheet surface before the treatment X 1 00 ... ( 1 ) ° In this manner, the wrapped cotton web subjected to the moist heat shrinkage treatment is heated by a heating roller or heated by the temperature above the heat distortion temperature of the sea-island type composite fiber. Further, the fiber density can also be increased. In this case, the density gradient of the fiber &le beam can be formed by heating and compressing the surface side and the back side by different conditions. The compression conditions by the heating roller include, for example, a roller temperature of 110 to 150 ° C and a roller pressure of 0.05 to 0.4 MPa. The basis weight of the wound web after the shrinkage treatment is preferably 1.2 to 4 times, more preferably 1.5 to 4 times, to the basis weight of the wound web before the shrinking treatment.
(4)高分子彈性體塡充步驟I 也可以藉由於予以收縮處理之纏繞棉網的海島型複合 纖維之進行極細纖維化處理之前,將高分子彈性體賦予纏 繞棉網之內部而使海島型複合纖維黏著。如此方式,藉由 於進行極細纖維化處理之前,將高分子彈性體賦予纏繞棉 網,能夠提高纏繞棉網的形態安定性,或是調整所獲得之 硏磨墊纖維束之密度梯度。 本步驟係藉由使高分子彈性體之水性液含浸於予以收 縮處理後之纏繞棉網後,使高分子彈性體凝固而使高分子 彈性體含浸賦予纏繞棉網之內部。 -27- 201120269 所謂高分子彈性體之水性液係使形成高分子彈性體之 成分分散於水系介質的水性分散液中’另外’使形成高分 子彈性體之成分溶解於水性介質的水性溶液中。高分子彈 性體之水性液的固形物濃度較佳爲1 〇質量%以上’進—步 更佳爲1 5質量%以上。 即使高分子彈性體之水性分散液爲高濃度’黏度也 低,由於也具有優異的含浸滲透性,容易對纏繞棉網進行 高塡充,對纖維也具有優異的接著性。因而,藉由本步驟 所含浸賦予的高分子彈性體能夠強力束縛海島型複合纖 維,另外,也容易提高硏磨墊之表觀密度。另外,由於凝 固高分子彈性體之水性分散液所獲得之高分子彈性體係對 水之潤濕性高,可以獲得能夠均勻且大量保持硏磨粒的硏 jg 0 於水性分散液中,包含懸浮及乳化。分散於水性分散 液的高分子彈性體的平均粒徑較佳約爲0.01至〇.2μηι。 調製水性分散液之方法並未予以特別限定。例如,聚 胺甲酸酯系樹脂之情形,藉由將具有羧基、磺酸基、羥基、 碳數爲5以下-尤其碳數爲3以下之聚伸烷基二醇基等之 具有親水性基的單體單位作爲樹脂構造單位而含有,能夠 賦予對水性介質之分散性。從一邊將因吸水所造成的膨潤 軟化抑制至最小限度且一邊提高吸水率或潤濕性之觀點, 具有如此之親水性基之單體單位的共聚合比例較佳爲〇. 1 至10質量%,進一步較佳爲0.5至5質量%。 另外,藉由使用界面活性劑,也能夠使聚胺甲酸酯系 樹脂之粒子乳化或懸浮於水系介質中。可用於乳化或懸浮 -28- 201120269 之界面活性劑的具體例,例如,可列舉:月桂基硫酸鈉、 月桂基硫酸銨、聚伸氧烷基十二烷基醚醋酸鈉、十二烷基 苯磺酸鈉、烷基二苯基醚二磺酸鈉、二辛基磺基琥珀酸鈉 等之陰離子性界面活性劑;聚伸氧乙基壬基苯基醚、聚伸 氧乙基辛基苯基醚、聚伸氧乙基月桂基醚、聚伸氧乙基硬 脂醯基醚、聚伸氧乙基-聚伸氧丙基嵌段共聚物等之非離子 性界面活性劑等。另外,也可以使用具有反應性之所謂的 反應性界面活性劑。另外,藉由適當選擇界面活性劑之濁 點,也能夠將感熱凝膠化性賦予聚胺甲酸酯樹脂》 使高分子彈性體之水性液含浸於纏繞棉網中之方法, ...例如,可列舉:使用刮刀塗布機、桿塗布機、或輥塗布機 之方法,或是進行浸漬之方法等。然後,藉由進行含浸有 .高分子彈性體水性液的纏繞棉網之乾燥,能夠使高分子彈 性體凝固。乾燥方法可列舉:於50至200 °C之乾燥裝置中 進行熱處理之方法;或是於紅外線加熱之後,於乾燥機中 進行熱處理之方法等。還有,藉由使高分子彈性體之水性 液含浸於纏繞棉網中之後進行乾燥之情形,水分將從纏繞 搞網之表層蒸發而水性液將遷移至表層。較佳爲藉由以促 進該遷移之條件使其乾燥,使高分子彈性體於表層中不均 而使纖維束之密度梯度形成。熱風乾燥機之熱處理溫度的 具體例,例如,較佳爲1 3 0至1 7 0 °C,進一步較佳爲1 4 0 至170 °C。利用如此之方法,藉由不僅依照纖維束之密度 差,也依照高分子彈性體所造成的密度差而提高硏磨面側 之密度,並藉由使硏磨面側進一步變得緻密而可以獲得耐 磨損性更高的硏磨墊。 -29- 201120269 (5 )極細纖維形成步驟 針對藉由去除海島型複合纖維中之水溶性熱可塑性樹 脂而形成極細纖維之步驟,詳細加以說明。 海島型複合纖維中之水溶性熱可塑性樹脂係使用水、 鹼性水溶液、酸性水溶液等予以溶解去除或予以分解去除。 於本步驟中,首先纏繞棉網或賦予高分子彈性體之纏 繞棉網係被浸漬於水、鹼性水溶液、酸性水溶液等之熱水 中而予以熱水處理。另外,爲了提高溶解效率,必要時也 可以進行利用輥之壓輥處理、高壓水流處理、超音波處理、 噴淋處理、攪拌處理、搓揉處理等。還有,爲了使固定面 之纖維束成爲低密度,也可以藉由高速水流或機械而進行 搓揉處理來處理。 還有,不進行濕熱收縮處理步驟(3),於本步驟中, 也可以同時進行纏繞棉網之收縮處理與海島型複合纖維之 極細纖維化。如此之同時進行收縮處理、與極細纖維化之 方法的具體例,例如,可列舉:第1階段係將纏繞棉網於 65至90°C的熱水中浸漬5至3 00秒鐘之後,再者,第2階 段係於8 5至1 0 0 °C的熱水中處理1 0 0至6 0 0秒鐘之條件。(4) Polymer elastomer filling step I It is also possible to impart a polymer elastic body to the inside of the wound cotton web by the ultrafine fiberizing treatment of the sea-island type composite fiber of the wound cotton web which has been subjected to shrinkage treatment, so that the sea-island type The composite fiber is adhered. In this manner, by applying the polymeric elastomer to the wound web before the ultrafine fiberizing treatment, the form stability of the wound web can be improved, or the density gradient of the obtained lining fiber bundle can be adjusted. In this step, the polymer elastomer is impregnated with the wound cotton web after the shrinkage treatment, and the polymer elastomer is solidified to impregnate the polymer elastomer to the inside of the wound cotton web. -27- 201120269 The aqueous liquid of the polymeric elastomer disperses the component forming the polymeric elastomer in the aqueous dispersion of the aqueous medium. In addition, the component forming the polymeric elastomer is dissolved in the aqueous solution of the aqueous medium. The solid content of the aqueous liquid of the polymer elastomer is preferably 1% by mass or more, and more preferably 15% by mass or more. Even if the aqueous dispersion of the polymeric elastomer has a high concentration and a low viscosity, it has excellent impregnation permeability, and it is easy to perform high entanglement on the wound cotton web, and has excellent adhesion to the fiber. Therefore, the polymer elastic body imparted by the impregnation in this step can strongly bind the sea-island type composite fiber, and it is also easy to increase the apparent density of the honing pad. Further, since the polymer elastic system obtained by the aqueous dispersion of the solidified polymeric elastomer has high wettability to water, it is possible to obtain a 且jg 0 capable of uniformly and largely maintaining the honing particles in the aqueous dispersion, including suspension and emulsification. The average particle diameter of the polymeric elastomer dispersed in the aqueous dispersion is preferably from about 0.01 to about 0.2 μm. The method of preparing the aqueous dispersion is not particularly limited. For example, in the case of a polyurethane resin, a hydrophilic group having a carboxyl group, a sulfonic acid group, a hydroxyl group, a carbon number of 5 or less, particularly a polyalkylene group having a carbon number of 3 or less, etc. The monomer unit is contained as a resin structural unit, and can impart dispersibility to an aqueous medium. The copolymerization ratio of the monomer unit having such a hydrophilic group is preferably from 0.1 to 10% by mass, from the viewpoint of suppressing the swelling and softening by the water absorption to the minimum and improving the water absorption or the wettability. Further, it is preferably from 0.5 to 5% by mass. Further, by using a surfactant, particles of the polyurethane resin can be emulsified or suspended in an aqueous medium. Specific examples of the surfactant which can be used for emulsifying or suspending -28-201120269, for example, sodium lauryl sulfate, ammonium lauryl sulfate, sodium polyoxyalkylene lauryl ether acetate, dodecylbenzene Anionic surfactants such as sodium sulfonate, sodium alkyl diphenyl ether disulfonate, sodium dioctyl sulfosuccinate; poly(extended ethoxyethyl phenyl ether), poly(extended oxyethyl octyl benzene) A nonionic surfactant such as a group ether, a polyoxyethylether lauryl ether, a polyoxyethylidene stearyl ether, a polyoxyethylene-polyoxypropylene block copolymer, or the like. Further, a reactive so-called reactive surfactant can also be used. Further, by appropriately selecting the cloud point of the surfactant, it is also possible to impart a sensible gelation property to the polyurethane resin. The method of impregnating the aqueous solution of the polymer elastomer into the wound cotton web, for example, For example, a method using a knife coater, a bar coater, or a roll coater, or a method of performing dipping, or the like can be mentioned. Then, the polymer elastic body can be solidified by drying the wound cotton web impregnated with the aqueous polymer elastomer aqueous solution. The drying method may be a method of heat-treating in a drying apparatus at 50 to 200 ° C or a method of heat-treating in a dryer after infrared heating. Further, by immersing the aqueous liquid of the polymeric elastomer in the wound cotton web and then drying it, the water will evaporate from the surface layer of the wound web and the aqueous liquid will migrate to the surface layer. It is preferred to form a density gradient of the fiber bundle by drying the polymer elastomer under the conditions for promoting the migration. Specific examples of the heat treatment temperature of the hot air dryer are, for example, preferably from 130 to 170 ° C, more preferably from 140 to 170 ° C. By such a method, the density of the honing surface side can be increased not only according to the difference in density of the fiber bundle but also the density difference caused by the polymeric elastomer, and can be obtained by further densifying the honing surface side. A wear pad with higher wear resistance. -29- 201120269 (5) Ultrafine fiber forming step The step of forming ultrafine fibers by removing the water-soluble thermoplastic resin in the sea-island type composite fiber will be described in detail. The water-soluble thermoplastic resin in the island-in-the-sea composite fiber is dissolved or removed by using water, an alkaline aqueous solution, an acidic aqueous solution, or the like, and is removed by decomposition. In this step, the wound cotton web which is first wound around the cotton web or imparted to the polymeric elastomer is immersed in hot water such as water, an alkaline aqueous solution, or an acidic aqueous solution to be subjected to hot water treatment. Further, in order to improve the dissolution efficiency, a roll press treatment, a high-pressure water flow treatment, an ultrasonic treatment, a shower treatment, a stirring treatment, a hydrazine treatment, or the like may be performed as necessary. Further, in order to make the fiber bundle of the fixing surface low in density, it may be treated by a high-speed water flow or a mechanical treatment. Further, the wet heat shrinkage treatment step (3) is not carried out, and in this step, the shrinkage treatment of the wound cotton web and the extremely fine fiberization of the sea-island type composite fiber may be simultaneously performed. Specific examples of the method of performing the shrinkage treatment and the ultrafine fiber at the same time include, for example, immersing the wound cotton web in hot water at 65 to 90 ° C for 5 to 300 seconds in the first stage, and then The second stage is to treat the conditions of 100 to 600 seconds in hot water at 85 to 100 °C.
(6 )高分子彈性體塡充步驟II 接著,集束極細纖維,另外,爲了進一步束縛極細纖 維束彼此,針對賦予高分子彈性體之步驟加以說明。於極 細纖維形成步驟(5)中,藉由對海島型複合纖維實施極細 纖維化處理,水溶性熱可塑性樹脂將被去除而在極細纖維 束之內部形成有空隙。於本步驟中,藉由將高分子彈性體 賦予如此之空隙中而集束極細纖維。另外,同時進一步藉 -30- 201120269 由高分子彈性體而束縛極細纖維束彼此。還有,極細纖維 已形成纖維束之情形下,藉由毛細現象’高分子彈性體之 水性液容易被纖維束之內部所吸收。還有,本發明所用之 高分子彈性體的水性液可以使用相同於高分子彈性體塡充 步驟1所說明的水性液。另外,使高分子彈性體塡充及凝 固之方法,方法上也可以使用相同於高分子彈性體塡充步 驟I所說明的方法。進行如此方式,硏磨墊前驅物將被形 成。 (7 )精加工步驟 藉由對於所獲得之硏磨墊前驅物實施平坦化.處理,本 實施形態之硏磨墊將可以獲得。平坦化處理係藉由將硏磨 墊前驅物熱壓縮成形成既定之厚度,藉由利用砂紙、扎針 布、鑽石等以硏磨表面而平滑地精加工表面,用以調整厚 度之處理。進行如此方式,所精加工的硏磨墊之厚度較佳 約爲0.5至3 mm。 另外,硏磨墊之表面也可以予以起毛處理。藉由進行 起毛處理,硏磨墊之硏磨面與被硏磨基材之接觸面積將變 大,另外,與硏磨糊之潤濕性將提高。起毛處理係利用砂 紙而拋光處理硏磨墊表面之方法。砂紙較佳使用硏磨粒棉 紗支數# 40號至# 80號之砂紙。起毛處理之具體例,例 如,可列舉:利用接觸型拋光機所進行的連續起毛處理、 或金剛砂型拋光處理、或組合接觸型與金剛砂型之拋光處 理等。另外’爲了形成均一之起毛狀態,也可以壓縮硏磨 墊所起毛處理的表面。 另外’爲了使平坦化性能更提高,也可以在硏磨墊之 -31 - 201120269 表面實施用以形成同心圓狀、螺旋狀、格子狀等之溝或孔 的表面加工。藉由實施如此之表面加工’能夠在硏磨面更 均一地使硏磨糊佈滿。 接著,針對使用本實施形態之硏磨墊的化學機械硏磨 方法,一邊參照第3圖且一邊詳細說明。第3圖係顯示使 用本實施形態之硏磨墊10的化學機械硏磨方法之實施模 樣的側面圖。 於使用本實施形態之硏磨墊10的化學機械硏磨方法 中,例如可使用具備如第3圖所示之圓形旋轉固定盤11、 糊供..應噴嘴12'載體13、與墊調節器14的CMP裝置20。 在旋轉固定盤I1之表面’藉由雙面膠帶而利用其固定面4 以貼附硏磨墊1〇。另外,載體13係被硏磨基材15所支撐。 於CMP裝置20中,固定盤11係藉由省略圖面的馬達 而於箭頭記號所示之方向上旋轉。另外’載體13係在固定. 盤11之面內,行星齒輪狀地藉由省略圖面的馬達而於例如 箭頭記號所示之方向上旋轉。墊調節器14也在固定盤11 之面內,行星齒輪狀地藉由省略圖面的馬達而於例如箭頭 記號所示之方向上旋轉。 - 首先,一邊將蒸餾水流至被旋轉固定盤11所固定而旋 轉的硏磨墊10之表面上,一邊按壓旋轉於硏磨墊10表面 之墊調節器14而進行硏磨墊10表面之調節。接著,從糊 供應噴嘴12而將含有各種化學成分及硬質之微細硏磨粒 的硏磨糊16供應至進行旋轉之硏磨墊10之表面。然後, 在硏磨糊16各處所佈滿的硏磨墊10上,按壓被載體13所 固定而進行旋轉之被硏磨基材15。然後,直到可以獲得既 -32- .201120269 定之平坦度爲止而持續硏磨處理。藉由調整作用於硏磨時 之按壓力或是旋轉固定盤11與載體13之相對運動速度, 精加工品質將受到影響。 於本實施形態之化學機械硏磨方法中,硏磨墊10係在 旋轉固定盤11之表面,被固定面4所固定。藉由利用固定 面4以固定硏磨墊10,由於纖維束之數量密度高且剛性高 的硏磨面3成爲外表面,硏磨速率及耐磨損性將變高,另 外,硏磨面內之硏磨不均一性將變低。另外,由於被旋轉 固定盤11所固定的固定面4側之表層係纖維束之數量密度 低且剛性低,能夠維持對被硏磨基材1 5之表面的適度隨動 性或適合性。 ~ 硏磨糊16之成分係根據被硏磨基材15之種類而予以 適當選擇。硏磨粒之具體例,例如,可列舉:具有數十nm 至數百nm粒徑之Si02、Al2〇3、Ce02、Μη203、鑽石粒子 等。另外,化學成分之具體例,例如,可列舉:改質酸/鹼 等被硏磨面之成分或界面活性劑等。 如此之本實施形態之化學機械硏磨方法係可用於各種 基材之硏磨。基材之具體例,例如,可列舉:矽、氧化矽、 氧氟化矽、有機聚合物等之絕緣材料;銅、鋁、鎢等之導 電材料;鉬、鈦、氮化鉬、氮化鈦等之位障材料等。另外, 其用途之具體例’例如,可列舉:矽晶圓、化合物半導體 晶圓、半導體晶圓、半導體元件、液晶構件、光學元件、 水晶、光學基板、電子電路基板、電子電路遮罩基板、多 層配線基板、硬碟、MEM S (微機電系統)基材等之硏磨。 還有,硏磨可以爲一次硏磨、二次硏磨(調整硏磨)、精 -33- 201120269 加工硏磨、鏡面硏磨等中任一種。 實施例 以下’藉由實施例以具體說明實施例。還有 之範圍係依照實施例之記載,並未予以任何限定 首先’彙整本實施例所用之評估方法而加以 〔評估方法〕 (1)極細纖維束之平均數量密度(D丨、D2、 纖維之平均截面積及纖維束之平均截面積的測定 藉由使用切刀之刃而平行於厚度方向進行 墊,形成厚度方向之截面,。然後,利用氧化餓以 得之截面。再利用掃瞄型電子顯微鏡(S EM ), 1 000倍觀察截面,拍攝其影像。然後,從所獲得 任意求得所選出的1〇〇個極細纖維束之截面積, 値設爲極細纖維束之平均截面積。.另外,求得形 維束之1〇〇條極細纖維的截面積,將其平均値作 維的單纖維之平均截面積。 另外,從所獲得之影像,從硏磨墊之表面起 方向20%以內之厚度區域中,各處選擇5個位置 正方形區域,計算各位置中之極細纖維束的個數 果,算出存在於每1 mm2之極細纖維束的個數。 置之平均設爲D丨。 另外,從所獲得之影像’從硏磨墊之背面起 方向20 %以內之厚度區域中,各處選擇5個位置 正方形區域’計算各位置中之極細纖維束的個襲 果,算出存在於每1 mm2之極細纖維束的個數。 ,本發明 〇 說明。 〇3 )、單 切斷硏磨 染色所獲 以1 〇 0至 之影像而 將其平均 成極細纖 「爲極細纖 i而朝厚度 之 0 · 1 m m :。從其結 將5個位 〖而朝厚度 之 0 · 1 mm 〔。從其結 將5個位 -34- 201120269 置之平均設爲D2。 另外,從所獲得之影像’從硏磨墊之表面起而朝厚度 方向50%附近之部分中,各處選擇5個位置之0.1 mm正方 形區域,計算各位置中之極細纖維束的個數。從其結果, 算出存在於每1 mm2之極細纖維束的個數。將5個位置之 平均設爲D3。 (2 )纏繞棉網之層間剝離強度 從所獲得之纏繞棉網’製作長23 cm、寬2.5 cm之長 方形上之試驗片。然後,在試驗片之一端,利用刮鬍刀而 將刻痕劃入厚度方向之約略中央。然後,用手拉伸距離邊 緣約10 cm而剝離。然後,將所剝離的兩片邊緣固定於各 自拉伸試驗機之夾頭。然後,利用拉伸試驗機拉伸’獲得 應力-歪斜曲線(SS曲線),從其平坦部分之應力而求出 剝離強力。還有,拉伸速度係以1〇〇 mm/分鐘進行。還有’ 所獲得之結果係3個試驗片之平均値。 (3)硏磨墊之D硬度的測定方法 使用硬度計D型(高分子計器股份有限公司製)’根 據】IS K 62 5 3而測定硏磨墊的硏磨面之D硬度。還有,載 重係設定爲5kg。 (4 )磨耗重量減輕 根據《!13〖5600-5-9之方法而測定切斷成直徑13(:111圓 形之硏磨墊硏磨面的Taber(塔柏)磨損。還有,以磨損輪: H-22、載重:500g、旋轉數:1000次之條件而測定。求出 測定前重量與測定後重量之差的重量減輕(mg )。 (5)高分子彈性體之玻璃轉移溫度(Tg)的測定 -35- 201120269 作成由構成硏磨墊之高分子彈性體而成之長4 cmx寬 0_5 cmx厚400#m±100//m之薄膜。然後,利用測微計以測 定薄膜之厚度後,使用動態黏彈性測定裝置(DVE Rheospectoler、Rheology股份有限公司製),以頻率11 Hz、 升溫速度3 °C /分鐘之條件而進行動態黏彈性之測定,將損 失彈性模數之主要分散波峰溫度設爲玻璃轉移溫度。 (6) 在2 3 °C及5 0°C之高分子彈性體的儲存彈性模數測 定方法 將構成硏磨墊之高分子彈性體作成長4cmx寬0.5 cm X 厚400//m±100//m之薄膜*然後,利用測微計以測定薄膜之 厚度後,使用動態黏彈性測定裝置(DVE Rheospectoler、 Rheology股份有限公司製),以頻率1 1 Hz、升溫速度3°C/ 分鐘之條件而測定在23 °C及5 0°C之儲存彈性模數,算出儲 存彈性模數。 (7) 高分子彈性體之飽和吸水率測定方法 將構成硏磨墊之高分子彈性體在50°C乾燥後所獲得之 厚度200 μηι之薄膜,於130 °C進行30分鐘之熱處理。然後, 在20°C、65%RH之條件下放置3日。然後,測定此時之乾 燥時的質量。在將乾燥的薄膜,於50°C之水中浸漬2日。 然後,從50 °C之水取出後,隨即拭去薄膜最外表面之多餘 的水滴等,測定吸水後之質量。然後,藉由下式而算出飽 和吸水率。 飽和吸水率(% ) =〔(吸水後之質量-乾燥時之質 量)/乾燥時之質量〕χίΟΟ (8 )硏磨墊之硏磨性能 -36- 201120269 將雙面黏著膠帶貼附於硏磨墊之固定面而固定於CMP 硏磨裝置(野村製作所股份有限公司製「PPO-60S」)之旋 轉固定盤。然後,藉由使用棉紗支數# 20 0之鑽石修整器 (diamond dresser)(三菱 Material(股)製之 MEC200L), 以壓力177 kP a、修整器旋轉數110旋轉/分鐘之條件,一邊 流入速度120mL/分鐘之^蒸餾水,一邊硏削硏磨墊表面18 分鐘而進行調節(風乾)。 接著,將硏磨糊供應至固定於旋轉固定盤之硏磨墊表 面。硏磨糊係使用以蒸餾水而將Cabot公司製硏磨糊SS25 稀釋成2倍之硏磨糊。另外,硏磨糊之供應量係設爲12 0ml/ 分鐘。然後,以壓板旋轉數50旋轉/分鐘、頭旋轉數49旋 轉/分鐘、硏磨壓力35kPa之條件,進行具有氧化膜表面之 直徑8吋矽晶圓之100秒鐘硏磨。 然後,在矽晶圓面內,測定4 9點之硏磨前及硏磨後的 氧化膜膜厚,求出硏磨速率(nm/分鐘)。另外,將49點 之硏磨速率的平均値設爲平均硏磨速率(R),進一步求出 硏磨速率之標準偏差(σ)。然後,藉由式(1): 不均一性(% ) = ( σ/R ) X 1 00 …(1 ) 而算出不均一性。不均一性之値越小,顯示硏磨面內 越被均一地硏磨。而且,能夠實現高精確度之硏磨加工。 另外,藉由式(2 ): 硏磨速率安定性(%) =(硏磨速率最大値-硏磨速 率最小値)χ 1〇〇…(2 ) 而算出硏磨速率安定性。 再者,藉由使用晶圓表面檢查裝置 Surfscan SP1 -37- 201120269 (KLA-Tencor公司製)而測定存在於硏磨後之: 之矽晶圓表面的〇_· 1 6 μιη以上大小之刮傷來評估 〔實施例1〕 使用作爲島成分之PVA樹脂、作爲海成分 莫耳%之間苯二甲酸改性PET。還有,間苯二甲 係使在5 0°C飽和吸水時之吸水率爲1質量%, 溫度爲77 °C。藉由從25島/纖維之熔融複合紡紗 嘴溫度260°C ),以25 : 75 (質量比)之比例 脂與間苯二甲酸改性PET噴出,形成海島型複 束。然後,藉由設置於噴嘴正下方之空氣噴射 拉伸详噴嘴所噴出之紗束,一邊進行拉伸而細 行冷卻而紡紗出平均纖度2.0 dtex之海島型複会 有,空氣噴射抽氣裝置之抽氣力係從每單位E 量、與所獲得之長纖維纖度之比例而使間接所 速度成爲4000m/min的方式來予以調整。然後 • 置於空氣噴射抽氣裝置正下方的移動式網上進 合纖維之連續收集,獲得基重量40 g/m2之紡紗 纖維棉網)。 接著,藉由交叉拋光而重疊12片之所獲得 片,製作總基重爲4 80 g/m2之棉網積層體。然 之棉網積層體噴灑防止針折斷油劑。接著,棉 依序使用針棉紗支數42號、鉤數3個之針、及 42號、鉤數6個之針,利用從其第一表面側起 5至25 mm之深度且扎數1500扎/cm2之條件而 理,進一步利用從其第二表面側起而以針深度 具有氧化膜 刮傷性。 之改性度6 酸改性PET 其玻璃轉移 用噴嘴(噴 ϋ使PVA樹 合纖維之紗 抽氣裝置而 化且一邊進 Γ長纖維。還 時間之噴出 求出的紡紗 ,藉由在設 行海島型複 黏合片(長 之紡紗黏合 後,所獲得 網積層體係 針棉紗支數 而以針深度 予以針扎處 0 至 1 5 mm -38- 201120269 之深度且扎數500扎/cm2之條件而予以針扎處理。因針扎 所造成的棉網積層體之面積收縮率爲3〇%。藉由如此之針 扎處理而可以獲得基重600 g/m2、層間剝離強度11.0 kg/2.5cm之纏繞棉網。 接著,藉由將所獲得之纏繞棉網於7 〇 °C之熱水中浸漬 90秒鐘而使島成分應力緩和,使得面積收縮43 進一步 10分鐘浸漬於95 °C之熱水中而使PVA樹脂溶解去除。還 有,於乾燥狀態中,因熱水處理所造成的纏繞棉網之面積 收縮率爲45%。藉由熱水處理而可以獲得由極細纖維之纖 維束所構成的不織布。不織布之基重爲780 g/m2、表觀密 度爲 0.55 g/m3。 然後,使得已調整至固形物濃度25質量%之聚胺甲酸 酯彈性體A之水性乳液含浸於所獲得之不織布中。還有, 水性乳液中之聚胺甲酸酯彈性體A之平均粒徑爲0 · 0 5 。 還有,聚胺甲酸酯彈性體A係如下之高分子。相對於 高分子二醇50質量%而言’聚胺甲酸酯彈性體A係使共聚 合1·5質量%之4,4’-二環己基甲烷二異氰酸酯與短鏈胺與 短鏈二醇與2,2’-雙(羥甲基)丙酸的合計量50質量%反應的 聚碳酸酯系無黃變型聚胺甲酸酯100質量份’再利用碳二 醯亞胺系5質量份使其交聯的交聯聚胺甲酸酯樹脂。還 有,高分子二醇係以99.9: 〇·1(莫耳比)來混合非晶性聚 碳酸酯系聚醇之六亞甲基碳酸酯與五亞甲基碳酸酯之共聚 合聚醇、與碳數2至3之聚烷二醇的混合物。 聚胺甲酸酯彈性體Α係吸水率2質量%、在2 3 °C之儲 存彈性模數450 MPa、在50 °C之儲存彈性模數300 MPa、 -39- 201120269 及玻璃轉移溫度-2 5 °C。另外,以聚胺甲酸酯彈性體A之固 形物換算’相對於不織布之質量而言,水性乳液係含浸1 5 質量%。接著,藉由於90 °C、50 % RH氣體環境中,進行含 浸有水性乳液的不織布之凝固處理,進一步於150 X:進行乾 燥處理,在進一步於150 °C進行熱壓縮而可以獲得硏磨墊前 驅物A0。硏磨墊前驅物A0係基重量910g/m2、表觀密度 0.62 g/m3、厚度1.45 mm。另外,不織布與聚胺甲酸酯彈 性體A之質量比率爲87/13。 然後,藉由拋光硏削加工硏磨墊前驅物A0,可以獲得 所平坦化的硏磨墊A 1。利用電子顯微鏡以觀察硏磨墊A 1 之截面,極細纖維束之平均存在密度Di約爲2500個/mm2, 極細纖維束之平均存在密度D2約爲1 200個/mm2,Di/Dz 約爲2.1。另外’於其截面中,觀察到由平均截面積約爲 1 Mm2之極細纖維所構成的平均截面積約爲3 2 0//m2之極細 纖維束。而且,極細纖維係藉由滲入極細纖維束內部之聚 胺甲酸酯彈性體所集束,另外,極細纖維束彼此也藉由聚 胺甲酸酯彈性體所黏著。硏磨墊A1係基重量75 0 g/m2、表 觀密度0.61 g/m3、厚度1.23 mm、D密度37。 所獲得之硏磨墊A1係被切斷成直徑51 cm之圓形,進 一步實施在主要面形成寬2.0 mm、深1.0 mm、間隔15.0 mm 之格子狀溝的加工。藉由上述之評估方法而評估如此之硏 磨墊A1的硏磨性能。將結果顯示於表1。 -40- 2 1X 11 20 02【I撇】 V , α 比較例< 300 300 〇 ΓΛ 〇 I 長纖維 〇 CN Η ω CL< CN 450 300 〇 比較例4 1010 〇 in 〇 〇\ 二 350 mmm 〇 CN 450 〇 m ο (Ν 比_3 350 340 350 〇 Ό 350 短纖維 CN 450 300 Ο <Ν 比較例2 2400 1600 400 〇 τ—Η 325 長纖維 寸 〇\ un (N 450 Ο m Ο (Ν 比較例1 2550 2430 2340 寸 .350 長纖維 11.0 間苯二甲酸改's m (N 450 300 Ο (Ν 實施例4 2300 1640 540 (N m 長纖維 〇 (N 450 Ο m Ο (Ν 實施例3 2840 2600 1 1890 ! m <N 長纖維 〇 <N 450 300 Ο (Ν 實施例2 1 2450 1840 1260 _1 On CN 325 長纖維 to (N Ο 300 Ο CN 實施例1 2500 1800 1200 Η 320 長纖維 11.0 m (N 寸 Ο Ο (Ν 實施例編號 1 平均數量密度(個/mm2) — — -1 平均數量密度D3(個/mm2) 平均數量密度D2(個/mm2) Di/〇2 I 晅 讎 遯 山11 幾 籍 U 纖維束之平均横截面積㈣2) 不織布構成纖維之種類 纏繞棉網之層間剝離強度(kg/2.5 cm) 極細纖維之熱可塑性樹脂之種類 高分子彈性體之Tg(°C) 高分子彈性體之23°c儲存彈性模數(MPa) 高分子彈性體之50°C儲存彈性模數(MPa) 高分子彈性體之飽和吸水率(%) 201120269 Γ~I 2 - 1 1 '1 § 0S8 82 srn on 0.91(6) Polymer elastomer filling step II Next, a step of providing a polymer elastic body in order to further bind the ultrafine fiber bundles is carried out by bundling the ultrafine fibers. In the ultrafine fiber forming step (5), the sea-island type composite fiber is subjected to an extremely fine fiberizing treatment, whereby the water-soluble thermoplastic resin is removed and a void is formed inside the ultrafine fiber bundle. In this step, the ultrafine fibers are bundled by imparting a polymeric elastomer to such a void. In addition, at the same time, further, -30-201120269 binds the ultrafine fiber bundles to each other by the polymeric elastomer. Further, in the case where the ultrafine fibers have been formed into a fiber bundle, the aqueous liquid of the polymer elastomer is easily absorbed by the inside of the fiber bundle by the capillary phenomenon. Further, the aqueous liquid of the polymeric elastomer used in the present invention may be the same as the aqueous liquid described in Step 1 of the polymeric elastomer. Further, in the method of filling and solidifying the polymer elastomer, the method described in the same manner as in the polymer elastomer charging step I may be used. In this manner, the honing pad precursor will be formed. (7) Finishing step The honing pad of the present embodiment can be obtained by performing planarization treatment on the obtained honing pad precursor. The flattening treatment is performed by heat-compressing the honing pad precursor to a predetermined thickness, and smoothing the surface by sanding the surface with a sandpaper, a tie cloth, a diamond, or the like to adjust the thickness. In this manner, the thickness of the finished honing pad is preferably about 0.5 to 3 mm. In addition, the surface of the honing pad can also be raised. By performing the raising treatment, the contact area between the honing surface of the honing pad and the honed substrate becomes large, and the wettability with the mash is improved. The raising treatment is a method of polishing the surface of the honing pad with sandpaper. Sandpaper is preferably made of honing grain cotton yarn count #40###80 sandpaper. Specific examples of the raising treatment include, for example, a continuous raising treatment by a contact type polishing machine, or a diamond-type polishing treatment, or a combination contact type and a diamond-type polishing treatment. Further, in order to form a uniform raised state, it is also possible to compress the surface of the honing pad which is raised. Further, in order to improve the flattening performance, surface processing for forming grooves or holes of concentric, spiral, lattice, or the like may be performed on the surface of the honing pad -31 - 201120269. By performing such surface processing, it is possible to make the honing paste more uniform on the honing surface. Next, the chemical mechanical honing method using the honing pad of the present embodiment will be described in detail with reference to Fig. 3 . Fig. 3 is a side view showing an embodiment of a chemical mechanical honing method using the honing pad 10 of the present embodiment. In the chemical mechanical honing method using the honing pad 10 of the present embodiment, for example, a circular rotating fixed disk 11 as shown in Fig. 3, a paste supply, a nozzle 12' carrier 13, and a pad adjustment can be used. The CMP device 20 of the device 14. The fixing surface 4 is attached to the surface of the rotating fixed disk I1 by a double-sided tape to attach the honing pad 1 〇. Further, the carrier 13 is supported by the honing substrate 15. In the CMP apparatus 20, the fixed disk 11 is rotated in the direction indicated by the arrow mark by omitting the motor of the drawing. Further, the carrier 13 is fixed in the plane of the disk 11, and is rotated in a direction indicated by, for example, an arrow mark by a motor in which the figure is omitted. The pad conditioner 14 is also rotated in the direction indicated by the arrow mark by the motor omitting the motor in the plane of the fixed disk 11. - First, the surface of the honing pad 10 is adjusted while flowing the distilled water to the surface of the honing pad 10 which is rotated by the fixed fixed disk 11, while pressing the pad adjuster 14 which is rotated on the surface of the honing pad 10. Next, the mash paste 16 containing various chemical components and hard fine honing abrasive grains is supplied from the paste supply nozzle 12 to the surface of the honing pad 10 which is rotated. Then, on the honing pad 10 which is filled around the honing paste 16, the honed base material 15 which is fixed by the carrier 13 and rotated is pressed. Then, until the flatness of -32-.201120269 is obtained, the honing process is continued. The finishing quality is affected by adjusting the pressing force applied to the honing or by rotating the relative movement speed of the fixed disk 11 and the carrier 13. In the chemical mechanical honing method of the present embodiment, the honing pad 10 is fixed to the surface of the rotating fixed disk 11 by the fixing surface 4. By fixing the honing pad 10 by the fixing surface 4, since the number of the fiber bundles is high and the rigidity of the honing surface 3 becomes the outer surface, the honing rate and the abrasion resistance become high, and the honing surface is also increased. The unevenness of the honing will become lower. Further, since the surface layer fiber bundle on the side of the fixing surface 4 fixed to the rotating fixed disk 11 has a low number density and low rigidity, moderate followability or suitability for the surface of the honed base material 15 can be maintained. The composition of the honing paste 16 is appropriately selected depending on the type of the honed substrate 15. Specific examples of the honing particles include, for example, SiO 2 , Al 2 〇 3 , Ce 02 , Μ 203 , diamond particles having a particle diameter of several tens nm to several hundreds nm. Further, specific examples of the chemical component include, for example, a component of a honed surface such as a modified acid/base or a surfactant. The chemical mechanical honing method of this embodiment can be used for honing various substrates. Specific examples of the substrate include, for example, insulating materials such as ruthenium, osmium oxide, yttrium oxyfluoride, and organic polymers; conductive materials such as copper, aluminum, and tungsten; molybdenum, titanium, molybdenum nitride, and titanium nitride; Waiting for barrier materials, etc. Further, specific examples of the application thereof include, for example, a germanium wafer, a compound semiconductor wafer, a semiconductor wafer, a semiconductor element, a liquid crystal member, an optical element, a crystal, an optical substrate, an electronic circuit substrate, an electronic circuit mask substrate, Honing of multilayer wiring boards, hard disks, MEM S (Micro Electro Mechanical Systems) substrates, etc. In addition, the honing can be one of honing, secondary honing (adjusting honing), fine -33-201120269 processing honing, mirror honing, and the like. EXAMPLES Hereinafter, the examples will be specifically described by way of examples. Further, the scope is based on the description of the examples, and is not limited thereto. First, the evaluation method used in the present embodiment is applied. [Evaluation method] (1) Average number density of the ultrafine fiber bundles (D丨, D2, fiber The average cross-sectional area and the average cross-sectional area of the fiber bundle are measured by using a blade edge parallel to the thickness direction to form a cross section in the thickness direction. Then, the cross section obtained by oxidizing is used. Microscope (S EM ), 1 000 times observation section, photographing the image. Then, from any obtained, the cross-sectional area of one selected ultrafine fiber bundle was determined, and 値 was set as the average cross-sectional area of the ultrafine fiber bundle. In addition, the cross-sectional area of the single-fiber ultrafine fiber of the shape-dimensional bundle is obtained, and the average cross-sectional area of the single fiber which is averaged as the dimension is obtained. Further, from the obtained image, the direction from the surface of the honing pad is 20%. In the thickness region within the area, five square areas of the position are selected, and the number of the ultrafine fiber bundles in each position is calculated, and the number of the ultrafine fiber bundles present per 1 mm2 is calculated. In addition, from the obtained image 'in the thickness region within 20% from the back surface of the honing pad, five square square regions are selected everywhere' to calculate the results of the ultrafine fiber bundles in each position, Calculate the number of ultrafine fiber bundles present per 1 mm2. This is a description of the present invention. 〇3), single cut honing dyeing obtained from 1 〇0 to the image and averaged into very fine fibers "for very fine fibers i is toward 0 · 1 mm of thickness: from the junction 5 bits to the thickness of 0 · 1 mm [. From its knot, the 5 bits - 34 - 201120269 are set to an average of D2. The image obtained was selected from the surface of the honing pad to a portion near 50% in the thickness direction, and a 0.1 mm square region of five positions was selected, and the number of ultrafine fiber bundles in each position was calculated. Calculate the number of fine fiber bundles present per 1 mm2. Set the average of the five positions to D3. (2) The peeling strength between the layers of the wound cotton web is 23 cm long and 2.5 mm wide from the obtained wound cotton web. a test piece on a rectangle of cm. Then, at one end of the test piece, The nick was drawn into the approximate center of the thickness direction with a razor, and then peeled off by stretching the edge by about 10 cm by hand. Then, the peeled two edges were fixed to the chucks of the respective tensile testers. Then, the stress-skew curve (SS curve) was obtained by stretching in a tensile tester, and the peeling strength was obtained from the stress in the flat portion. Further, the stretching speed was performed at 1 〇〇mm/min. 'The results obtained are the average enthalpy of the three test pieces. (3) The D hardness of the honing pad is measured using a hardness meter type D (manufactured by Kobunco Co., Ltd.) according to IS K 62 5 3 D hardness of the honing surface of the honing pad. Also, the load system is set to 5 kg. (4) Abrasion weight reduction According to the method of !13 〖5600-5-9, the Taber wear is cut into a diameter of 13 (: 111 round honing pad honing surface. Also, to wear Wheel: H-22, load: 500 g, rotation number: 1000 times. The weight loss (mg) of the difference between the weight before measurement and the weight after measurement was determined. (5) Glass transition temperature of the polymer elastomer ( Determination of Tg) -35- 201120269 A film having a length of 4 cm x width 0_5 cm x thickness of 400 #m ± 100 //m formed of a polymeric elastomer constituting a honing pad is formed. Then, a micrometer is used to measure the film. After the thickness, the dynamic viscoelasticity was measured at a frequency of 11 Hz and a temperature increase rate of 3 ° C /min using a dynamic viscoelasticity measuring apparatus (DVE Rheospectoler, manufactured by Rheology Co., Ltd.), and the main dispersion of the loss elastic modulus was mainly dispersed. The peak temperature is set to the glass transition temperature. (6) The storage elastic modulus of the polymer elastomer at 23 ° C and 50 ° C is determined by growing the polymer elastomer of the honing pad to a thickness of 4 cm x 0.5 cm X Film with a thickness of 400//m±100//m*, then using a micrometer to determine the film After the thickness, a storage elastic modulus at 23 ° C and 50 ° C was measured using a dynamic viscoelasticity measuring device (DVE Rheospectoler, manufactured by Rheology Co., Ltd.) at a frequency of 1 1 Hz and a temperature increase rate of 3 ° C / minute. The number of storage elastic modulus is calculated. (7) Method for measuring the saturated water absorption of the polymer elastomer The film of the thickness of 200 μm obtained after drying the polymer elastomer constituting the honing pad at 50 ° C at 130 ° C The heat treatment was carried out for 30 minutes, and then left for 3 days under conditions of 20 ° C and 65% RH. Then, the mass at the time of drying was measured, and the dried film was immersed in water at 50 ° C for 2 days. Then, after taking out water of 50 ° C, the excess water droplets on the outermost surface of the film were wiped off, and the mass after water absorption was measured. Then, the saturated water absorption rate was calculated by the following formula: Saturated water absorption rate (%) = [ (Quality after water absorption - Quality when dry) / Quality during drying] χίΟΟ (8) Honing performance of honing pad -36- 201120269 Attach double-sided adhesive tape to the fixing surface of the honing pad and fix it to CMP Honing device (Nomura Manufacturing Co., Ltd. has Rotary fixed disc of the company "PPO-60S". Then, by using the diamond dresser of the cotton yarn count #20 0 (MEC200L made by Mitsubishi Material), the pressure is 177 kP a, trimming The condition of the number of rotations of 110 rotations/min was adjusted while the surface of the honing pad was immersed for 18 minutes while flowing into the distilled water having a speed of 120 mL/min (air drying). Next, the mash paste is supplied to the surface of the honing pad fixed to the rotary fixed disk. For the mash paste, the Cabot company mash paste SS25 was diluted to 2 times with distilled water. In addition, the supply of mash is set to 120 ml/min. Then, 100 seconds of honing of the 8 直径 diameter wafer having the surface of the oxide film was carried out under the conditions of a number of revolutions of the platen of 50 rotations/min, a number of head rotations of 49 rotations/min, and a honing pressure of 35 kPa. Then, the film thickness of the oxide film before and after honing at 49 points was measured in the surface of the germanium wafer, and the honing rate (nm/min) was determined. Further, the average enthalpy of the honing rate of 49 points was taken as the average honing rate (R), and the standard deviation (σ) of the honing rate was further determined. Then, the inhomogeneity is calculated by the equation (1): the heterogeneity (%) = (σ/R) X 1 00 (1). The smaller the heterogeneity, the more uniform the honing surface is. Moreover, high-accuracy honing processing can be realized. Further, the honing rate stability is calculated by the formula (2): honing rate stability (%) = (maximum honing rate 値 - honing rate minimum 値) χ 1 〇〇 (2). Further, by using the wafer surface inspection apparatus Surfscan SP1 -37-201120269 (manufactured by KLA-Tencor Co., Ltd.), the smear of 矽_·1 6 μm or more which is present after honing is measured. Evaluation [Example 1] A PVA resin as an island component and a phthalic acid-modified PET as a sea component mol% were used. Further, the meta-xylene system has a water absorption ratio of 1% by mass and a temperature of 77 °C when saturated with water at 50 °C. The island-type complex is formed by ejecting a ratio of 25:75 (mass ratio) of fat to the PET modified by a melt-composite spinning temperature of 25 islands/fibers at a temperature of 260 ° C. Then, by the air jet which is disposed immediately below the nozzle, the yarn bundle discharged from the nozzle is stretched and finely cooled to spun the island-type rendezvous having an average fineness of 2.0 dtex, and the air jet pumping device The pumping force was adjusted in such a manner that the indirect speed was 4000 m/min from the ratio of the unit E per unit to the obtained long fiber fineness. Then • Continuous collection of mobile web feed fibers placed directly below the air jet aspirator to obtain a spun fiber web with a basis weight of 40 g/m2). Next, 12 sheets were obtained by cross-polishing, and a cotton web layer having a total basis weight of 4 80 g/m 2 was produced. However, the cotton mesh laminate spray prevents the needle from breaking off the oil. Next, the cotton is sequentially used with a needle cotton count of 42, a hook number of 3 needles, and a 42 gauge needle with a hook number of 6 needles, using a depth of 5 to 25 mm from the first surface side and a number of 1500 ties. The condition of /cm2 is further utilized to have an oxide film scratch resistance at the needle depth from the second surface side thereof. Modification degree 6 Acid-modified PET The nozzle for glass transfer (sneezing to make the PVA dendritic fiber yarn extraction device and to feed the long fibers at the same time. Island-type composite bonding sheet (after the long spinning, the obtained number of needle-wound yarns of the mesh layer system is obtained, and the depth of the needle is 0 to 15 mm -38-201120269 at the needle depth and the number of the bundles is 500 扎/cm2 The condition is handled by needle sticking. The area shrinkage of the cotton web laminate due to needle sticking is 3〇%. By this needle sticking treatment, the basis weight of 600 g/m2 and the interlaminar peel strength of 11.0 kg/2.5 can be obtained. The winding cotton web of cm. Next, the island component stress is moderated by immersing the obtained wound cotton web in hot water of 7 ° C for 90 seconds, so that the area shrinkage 43 is further immersed at 95 ° C for 10 minutes. In the hot water, the PVA resin is dissolved and removed. Also, in the dry state, the area shrinkage of the wound cotton web due to hot water treatment is 45%. The fiber bundle of the ultrafine fibers can be obtained by hot water treatment. Non-woven fabric composed of non-woven fabrics with a basis weight of 780 g/m2 The apparent density was 0.55 g/m 3 . Then, the aqueous emulsion of the polyurethane elastomer A adjusted to a solid concentration of 25% by mass was impregnated into the obtained non-woven fabric. Also, the polyamine in the aqueous emulsion The average particle diameter of the formate elastomer A is 0 · 0 5 . Further, the polyurethane elastomer A is a polymer as follows: 'Polyurethane' relative to 50% by mass of the polymer diol Elastomer A is a total amount of 4,5'-dicyclohexylmethane diisocyanate and short-chain amine and short-chain diol and 2,2'-bis(hydroxymethyl)propionic acid copolymerized by 1.5% by mass. 50 parts by mass of a polycarbonate-based non-yellowing type polyurethane having 100 parts by mass of a crosslinked polyurethane resin which is crosslinked by using 5 parts by mass of a carbodiimide. The molecular diol is a mixture of a non-polymerized polyalcohol of hexamethylene carbonate and penta methylene carbonate of an amorphous polycarbonate-based polyalcohol with a carbon number of 29.9: 莫·1 (mole ratio). a mixture of polyalkylene glycols up to 3. Polyurethane elastomers have a water absorption of 2% by mass, a storage modulus of 450 MPa at 23 ° C, and a temperature of 50 ° C. Storage elastic modulus 300 MPa, -39- 201120269 and glass transition temperature -25 ° C. In addition, in terms of the solid content of polyurethane elastomer A, the aqueous emulsion is impregnated with respect to the quality of the non-woven fabric. 5% by mass. Next, by coagulation treatment of a non-woven fabric impregnated with an aqueous emulsion in a 90 ° C, 50% RH gas atmosphere, further drying treatment at 150 X: and further heat compression at 150 ° C The honing pad precursor A0 was obtained. The honing pad precursor A0 had a basis weight of 910 g/m2, an apparent density of 0.62 g/m3, and a thickness of 1.45 mm. Further, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 87/13. Then, by polishing the honing pad precursor A0, the flattened honing pad A 1 can be obtained. Using an electron microscope to observe the cross section of the honing pad A 1 , the average density D of the ultrafine fiber bundle is about 2500 / mm 2 , and the average density D 2 of the ultrafine fiber bundle is about 1 200 / mm 2 , and the Di / Dz is about 2.1. . Further, in the cross section thereof, an ultrafine fiber bundle composed of ultrafine fibers having an average cross-sectional area of about 1 Mm2 and having an average cross-sectional area of about 3 2 0//m 2 was observed. Further, the ultrafine fibers are bundled by the polyurethane elastomer penetrating into the inside of the ultrafine fiber bundle, and the ultrafine fiber bundles are also adhered to each other by the polyurethane elastomer. The honing pad A1 has a basis weight of 75 0 g/m2, an apparent density of 0.61 g/m3, a thickness of 1.23 mm, and a D density of 37. The obtained honing pad A1 was cut into a circular shape having a diameter of 51 cm, and further processing for forming a lattice-like groove having a width of 2.0 mm, a depth of 1.0 mm, and a spacing of 15.0 mm was formed on the main surface. The honing performance of such a pad A1 was evaluated by the above evaluation method. The results are shown in Table 1. -40- 2 1X 11 20 02 [I撇] V , α Comparative Example < 300 300 〇ΓΛ 〇I Long fiber 〇CN Η ω CL<CN 450 300 〇Comparative Example 4 1010 〇in 〇〇\ Two 350 mmm 〇 CN 450 〇m ο (Ν ratio _3 350 340 350 〇Ό 350 short fiber CN 450 300 Ο <Ν Comparative example 2 2400 1600 400 〇τ—Η 325 Long fiber inch 〇\ un (N 450 Ο m Ο (Ν Comparative Example 1 2550 2430 2340 inch. 350 long fiber 11.0 isophthalic acid changed 's m (N 450 300 Ο (Ν Example 4 2300 1640 540 (N m long fiber 〇 (N 450 Ο m Ο (Ν Example 3 2840 2600 1 1890 ! m <N long fiber 〇<N 450 300 Ο (Ν Example 2 1 2450 1840 1260 _1 On CN 325 Long fiber to (N Ο 300 Ο CN Example 1 2500 1800 1200 Η 320 long fiber 11.0 m (N inch Ο Ο (Ν Example No. 1 Average number density (pieces/mm2) — — -1 Average number density D3 (pieces/mm2) Average number density D2 (pieces/mm2) Di/〇2 I 晅雠遁Mountain 11 The average cross-sectional area of several U-fiber bundles (4) 2) Non-woven fabrics The type of fibers wrapped between the layers of the cotton web (kg/2.5 cm) The heat of the microfiber Type of plastic resin Tg (°C) of polymer elastomer 23°c storage elastic modulus of polymer elastomer (MPa) 50°C storage elastic modulus of polymer elastomer (MPa) Saturated polymer elastomer Water absorption rate (%) 201120269 Γ~I 2 - 1 1 '1 § 0S8 82 srn on 0.91
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c I 201120269 〔實施例2〕 以環境氣溫60°C、相對溼度80%、500秒鐘之條件, 進行實施例1所獲得之纏繞棉網之蒸氣加熱。然後’對於 所蒸氣加熱處理的纏繞棉網,利用i2〇°C之熱輥僅壓縮處理 其表面。於乾燥狀態下,藉由此蒸氣加熱處理及壓縮處理 所造成的纏繞棉網之面積收縮率係40%。然後’使固形物 濃度1 5質量%之聚胺甲酸酯彈性體A的水性乳液含浸於該 處理後之纏繞棉網中。接著,藉由於90°C、50%RH氣體環 境中,進行含浸有水性乳液的不織布之凝固處理’進一步 於15 0°C進行乾燥處理,形成纏繞棉網與聚胺甲酸酯彈性體 A之複合體(纏繞棉網複合體)。還有,以聚胺甲酸酯彈 性體A之固形物換算,相對於纏繞棉網複合體之全部質 量,水性乳液含浸有7質量%。然後,藉由將所獲得之纏 繞棉網複合體於95 t之熱水中浸漬10分鐘而使PVA樹脂 溶解去除,進一步藉由進行乾燥而形成由極細纖維之纖維 束所構成的不織布與聚胺甲酸酯彈性體A之複合體(不織 布複合體)。 然後,進一步使已調整至固形物濃度25質量%之聚胺 甲酸酯彈性體A的水性乳液含浸於不織布複合體中。以聚 .胺甲酸酯彈性體A之固形物換算,相對於不織布之全部質 量而言,水性乳液係含浸1 5質量%。接著,藉由於9 0 °C、 5 0%RH氣體環境中,進行含浸有水性乳液的不織布之凝固 處理,進一步於15〇°C進行乾燥處理,再進一步於15〇°C進 -43- 201120269 行熱壓縮而可以獲得硏磨墊前驅物BO。硏磨墊前驅物BO 係基重量73 0 g/m2、表觀密度0.58 g/m3、厚度1 .26 mm。 另外,不織布與聚胺甲酸酯彈性體A之質量比率爲8 0/2 0。 然後,藉由拋光硏削加工硏磨墊前驅物B0,可以獲得 所平坦化的硏磨墊B 1。利用電子顯微鏡以觀察硏磨墊B 1 之截面,極細纖維束之平均存在密度D!約爲2450個/mm2, 極細纖維束之平均存在密度D2約爲1 260個/mm2,DWD2 約爲1.9。另外,於其截面中,觀察到由平均截面積約爲 12//m2之極細纖維.所構成的平均截面積約爲325//m2之極細 纖維束。而且,極細纖維係藉由滲入極細纖維束內部之聚 胺甲酸酯彈性體所集束,另外,硏磨墊B1係基重量614 g/m2、表觀密度0.58 g/m3'厚度1.06 mm、D硬度36。而 且,所獲得之硏磨墊B 1係相同於實施例1被加工、評估。 將結果顯示於表1。 〔實施例3〕 以環境氣溫80°C、相對濕度80%、500秒鐘之條件, 進行實施例1所獲得之纏繞棉網之蒸氣加熱。然後,對於 所蒸氣加熱處理的纏繞棉網,利用120°C之熱輥僅壓縮處理 其表面。於乾燥狀態下,藉由此蒸氣加熱處理及壓縮處理 所造成的纏繞棉網之面積收縮率係50%。然後,使固形物 濃度1 5質量%之聚胺甲酸酯彈性體A的水性乳液含浸於該 處理後之纏繞棉網中。接著,藉由於9 0°C、5 0%RH氣體環 境中,進行含浸有水性乳液的不織布之凝固處理,進一步 於150°C進行乾燥處理’形成纏繞棉網與聚胺甲酸酯彈性體 -44 - 201120269 A之複合體。還有,以聚胺甲酸酯彈性體A之固形物換算’ 相對於纏繞棉網複合體之全部質量,水性乳液含浸有7質 量_%。然後,藉由將纏繞棉網複合體於95°C之熱水中浸漬 10分鐘而使PVA樹脂溶解去除,進一步藉由進行乾燥而形 成由極細纖維之纖維束所構成的不織布與聚胺甲酸酯彈性 體A之複合體。 然後,進一步使已調整至固形物濃度25質量%之聚胺 甲酸酯彈性體A的水性乳液含浸於不織布複合體中。以聚 胺甲酸酯彈性體A之固形物換算,相對於不織布之全部質 量而言,水性乳液係含浸1 5質量%。接著,藉由於90°C、 5 0%RH氣體環境中,進行含浸有水性乳液的不織布之凝固 處理,進一步於150°C進行乾燥處理,再進一步於15〇°C進 行熱壓縮而可以獲得硏磨墊前驅物C0。硏磨墊前驅物C0 係基重量790 g/m2、表觀密度0.63 g/m3、厚度1_25 mm。 另外,不織布與聚胺甲酸酯彈性體A之質量比率爲8 0/2 0。 然後,藉由拋光硏削加工硏磨墊前驅物C0,可以獲得 所平坦化的硏磨墊C1。利用電子顯微鏡以觀察硏磨墊C1 之截面,極細纖維束之平均存在密度D!約爲2840個/mm2’ 極細纖維束之平均存在密度D2約爲1 890個/mm2,Di/Dz 約爲1.5。另外,於其截面中,觀察到由平均截面積約爲 13//m2之極細纖維所構成的平均截面積約爲325//m2之極細 纖維束。而且,極細纖維係藉由滲入極細纖維束內部之聚 胺甲酸酯彈性體所集束,另外,硏磨墊C1係基重量650 g/m2、表觀密度0.63 g/m3、厚度1.03 mm、D硬度37。而 -45- 201120269 且,所獲得之硏磨墊c 1係相同於實施例1被加工、評估。 將結果顯不於表1。 〔實施例4〕 藉由交叉拋光而重疊12片之與實施例1所獲得之同樣 的紡紗黏合片,製作總基重爲480 g/m2之棉網積層體。然 後,將防止針折斷油劑噴灑於所獲得之棉網積層體。接著’ 棉網積層體係依序使用針棉紗支數42號、鉤數1個之針、 及針棉紗支數42號、鉤數6個之針,以從其第一表面側而 以針深度5至25 mm之深度且扎數1 200扎/cm2之條件而 予以針扎處理,進一步從第二表面側而以針深度〇至1 〇 mm 之深度且扎數300扎/cm2之條件而予以針扎處理。因針扎 所造成的棉網積層體之面積收縮率爲2 0%。藉由如此之針 扎處理而可以獲得基重5 60 g/m2、層間剝離強度9.0 kg/2.5 cm之纏繞棉網。 以環境氣溫6 0 °C、相對濕度7 0 %、5 0 0秒鐘之條件, 進行所獲得之纏繞棉網之蒸氣加熱。然後,對於所蒸氣加 熱處理的纏繞棉網,利用110 t:之熱輥僅壓縮處理其表面。 於乾燥狀態下’藉由此蒸氣加熱處理及壓縮處理所造成的 纏繞棉網之面積收縮率係3 5 %。然後,使固形物濃度1 5質 量%之聚胺甲酸酯彈性體A的水性乳液含浸於該處理後之 纏繞棉網中。接著,藉由於90 °C、50 %RH氣體環境中,進 行含浸有水性乳液的不織布之凝固處理,進一步於150 °C進 行乾燥處理’形成纏繞棉網與聚胺甲酸酯彈性體A之複合 體。還有’以聚胺甲酸酯彈性體A之固形物換算,相對於 -46 - 201120269 纏繞棉網複合體之全部質量,水性乳液含浸有7質量% ° 然後,藉由將纏繞棉網複合體於9 5 °C之熱水中浸漬1〇分鐘 而使PVA樹脂溶解去除,進一步藉由進行乾燥而形成由極 細纖維之纖維束所構成的不織布與聚胺甲酸酯琴性體A之 不織布複合體。 然後,進一步使已調整至固形物濃度25質量%之聚胺 甲酸酯彈性體A的水性乳液含浸於不織布複合體中。以聚 胺甲酸酯彈性體A之固形物換算,相對於不織布之全部質 量而言,水性乳液係含浸1 5質量%。接著,藉由於90°C、 50 % RH氣體環境中,進行含浸有水性乳液的不織布之凝固 處理,進一步於150°C進行乾燥處理,再進一步於150°C進 行熱壓縮而可以獲得硏磨墊前驅物E0。硏磨墊前驅物E0 係基重量66 5 g/m2、表觀密度0.53g/m3、厚度1.25 mm。 另外,不織布與聚胺甲酸酯彈性體A之質量比率爲80/20。 然後,藉由拋光硏削加工硏磨墊前驅物E0,可以獲得 所平坦化的硏磨墊E 1。利用電子顯微鏡以觀察硏磨墊E 1 之截面,極細纖維束之平均存在密度Di約爲2300個/mm2, 極細纖維束之平均存在密度D2約爲540個/mm2,約 爲4.3。另外,於其截面中,觀察到由平均截面積約爲11 ym2 之極細纖維所構成的平均截面積約爲325//m2之極細纖維 束。而且,極細纖維係藉由滲入極細纖維束內部之聚胺甲 酸酯彈性體所集束,另外,硏磨墊E1係基重量559 g/m2、 表觀密度〇.53g/m3、厚度1.05mm、D硬度34。而且,所 獲得之硏磨墊E 1係相同於實施例1被加工、評估。將結果 -47- 201120269 顯不於表1。 〔比較例1〕 藉由交叉拋光而重疊12片之與實施例1所獲得之同樣 的紡紗黏合片,製作總基重爲.480 g/m2之棉網積層體。然 後/將防止針折斷油劑噴灑於所獲得之棉網積層體。接著’ 棉網積層體係使用針棉紗支數42號、鉤數6個之針’以分 別從其第一表面側及其第二表面側而以針深度1 〇至1 5 mm 之深度且扎數900扎/cm2之條件而合計1 800扎/cm2進行針 扎處理。因針扎所造成的棉網積層體之面積收縮率爲 3 0%。藉由如此之針扎處理而可以獲得基重600 g/m2、層 間剝離強度1 1 .0 kg/2.5 cm之纏繞棉網。以下,以相同於 實施例1之條件,藉由進行纏繞棉網之熱水處理而使PVA 樹脂溶解去除,進一步含浸賦予聚胺甲酸酯彈性體A,進 一步藉由於150°C進行熱壓縮而可以獲得硏磨墊前驅物 F0。硏磨墊前驅物F0係基重量740 g/m2、表觀密度0.63 g/m3、厚度1.17 mm»另外,不織布與聚胺甲酸酯彈性體A 之質量比率爲87/13。 然後,藉由拋光硏削加工硏磨墊前驅物F0,可以獲得 所平坦化的硏磨墊F 1。利用電子顯微鏡以觀察硏磨墊F 1 之截面,極細纖維束之平均存在密度D!約爲2550個/mm2, 極細纖維束之平均存在密度D2約爲2 3 40個/mm2,Di/D2 約爲1.1。另外,於其截面中,觀察到由平均截面積約爲 14〆之極細纖維所構成的平均截面積約爲3 5 0〆之極細 纖維束。而且,極細纖維係藉由滲入極細纖維束內部之聚 -48- 201120269 胺甲酸酯彈性體所集束,另外,硏磨墊F1係基重量613 g/m2、表觀密度0.63 g/m3、厚度0.98mm、D硬度38。而 且,所獲得之硏磨墊F 1係相同於實施例1被加工、評估。 將結果顯示於表1。 〔比較例2〕 藉由交叉拋光而重疊12片之與實施例1所獲得之同樣 的紡紗黏合片,製作總基重爲480 g/m2之棉網積層體。然 後,將防止針折斷油劑噴灑於所獲得之棉網積層體。接著, 棉網積層體係依序使用針棉紗支數42號、鉤數1個之針、 及針棉紗支數42號、鉤數6個之針,以從其第一表面側而 以針深度5至25 mm之深度且扎數1 200扎/cm2之條件而 予以針扎處理,進一步從第二表面側而以針深度〇至5 mm 之深度且扎數3 00扎/cm2之條件而予以針扎處理。因針扎 所造成的棉網積層體之面積收縮率爲2 0%。藉由如此之針 扎處理而可以獲得基重560 g/m2、層間剝離強度9.4 kg/2.5 cm之纏繞棉網。 以環境氣溫60 °C、相對濕度70%、500秒鐘之條件, 進行所獲得之纏繞棉網之蒸氣加熱。然後,對於所蒸氣加 熱處理的纏繞棉網,利用ll〇°C之熱輥僅壓縮處理其表面。 於乾燥狀態下,藉由此蒸氣加熱處理及壓縮處理所造成的 纏繞棉網之面積收縮率係35%»然後,使固形物濃度15質 量%之聚胺甲酸酯彈性體A的水性乳液含浸於該處理後之 纏繞棉網中。接著,藉由於90°C、5 0%RH氣體環境中,進 行含浸有水性乳液的不織布之凝固處理,進一步於1 5 〇 °C進 -49- 201120269 行乾燥處理,形成纏繞棉網與聚胺甲酸醋彈性體A之複合 體。還有’以聚胺甲酸酯彈性體A之固形物換算’相對於 纏繞棉網複合體之全部質量’水性乳液含浸有7質量%° 然後,藉由將纏繞棉網複合體於95 之熱水中浸漬10分鐘 而使PVA樹脂溶解去除,進一步藉由進行乾燥而形成由極 細纖維之纖維束所構成的不織布與聚胺甲酸醋彈性體A之 不織布複合體。 然後,進一步使已調整至固形物濃度25質量%之聚胺 甲酸酯彈性體A的水性乳液含浸於不織布複合體中。以聚 胺甲酸酯彈性體A之固形物換算’相對於不織布之全部質 量而言,水性乳液係含浸1 5質量%。接著’藉由於90°C、 5 0%RH氣體環境中,進行含浸有水性乳液的不織布之凝固 處理,進一步於150°C進行乾燥處理,再進一步於15〇°C進 行熱壓縮而可以獲得硏磨墊前驅物G0。硏磨墊前驅物G0 係基重量665 g/m2 '表觀密度0.53 g/m3、厚莩1.25 mm。 另外,不織布與聚胺甲酸酯彈性體A之質量比率爲8 0/2 0。 然後,藉由拋光硏削加工硏磨墊前驅物G0,可以獲得 所平坦化的硏磨墊G 1。利用電子顯微鏡以觀察硏磨墊G 1 之截面,極細纖維束之平均存在密度D!約爲2400個/mm2, 極細纖維束之平均存在密度D2約爲400個/mm2,Di/D2約 爲6.0。另外,於其截面中,觀察到由平均截面積約爲n 之極細纖維所構成的平均截面積約爲3 25 pm2之極細纖維 束。而且,極細纖維係藉由滲入極細纖維束內部之聚胺甲 酸酯彈性體所集束,另外,硏磨墊G1係基重量559g/m2、 -50- 201120269 表觀密度0.53 g/m3、厚度l.〇5mm、D硬度34。而且,所 獲得之硏磨墊E 1係相同於實施例1被加工、評估。將結果 顯示於表1。 〔比較例3〕 進行相同於實施例1之方式,藉由以3 000m/miri捲取 從噴嘴所噴出的海島型複合纖維紗束而獲得長纖維。然 後,藉由捲取及切斷所獲得之長纖維,獲得切斷長度30mm 之短纖維。然後,以相同於實施例1之條件而針扎所獲得 之短纖維。藉由如此之針扎處理,可以獲得基重600 g/m2、 層間剝離強度7.5 kg/2.5 cm之短纖維纏繞不織布。還有, 由依照針扎所獲得之片材之面積收縮率爲2 5 %。使用所獲 得之短纖維纏繞不織布以取代纏繞棉網,藉由以相同於實 施例1之條件,使PVA樹脂溶解去除,獲得表觀密度0.35 g/m3之不織布。還有,於溶解去除PVA樹脂之際,藉由大 幅拉伸短纖維纏繞不織布而頻繁引起極細纖維之脫落。然 後,藉由將聚胺甲酸酯彈性體A含浸賦予於所獲得之不織 布中,進一步於150°C進行熱壓縮而可以獲得硏磨墊前驅物 H0。硏磨墊前驅物H0係基重量480 g/m2、表觀密度0.43 g/m3、厚度1.15 mm。另外,不織布與聚胺甲酸酯彈性體A 之質量比率爲87/1 3。 然後,藉由拋光硏削加工硏磨墊前驅物H0,可以獲得 所平坦化的硏磨墊Η 1。利用電子顯微鏡以觀察硏磨墊Η 1 之截面,極細纖維束之平均存在密度D1約爲350個/mm2, 極細纖維束之平均存在密度D2約爲350個/mm2,D!/D2約 -51- 201120269 爲1.0»另外,於其截面中,觀察到由平均截面積約爲16//m2 之極細纖維所構成的平均截面積約爲3 5 0/im2之極細纖維 束。而且,極細纖維係藉由滲入極細纖維束內部之聚胺甲 酸酯彈性體所集束,另外,硏磨墊H1係基重量3 97 g/m2、 表觀密度0.42 g/m3、厚度0.95 mm、D硬度27。而且,所 獲得之硏磨墊H1係相同於實施例1被加工、評估。將結 果_示於表1。還有,藉由大幅拉伸短纖維纏繞不織布, 由於頻繁引起極細纖維之脫落的狀態之故,硏磨評估係被 省略。 〔比較例4〕 進行相同於實施例1之方式,藉由以3000m/min捲取 從噴嘴所墳出的海島型複合纖維紗束而獲得長纖維。然 後,藉由捲取及切斷所獲得之長纖維,獲得切斷長度30 mm 之短纖維。然後,以相同於實施例1之條件而針扎所獲得 之短纖維。藉由如此之針扎處理,可以獲得基重600 g/m2、 層間剝離強度7 kg/2.5 cm之短纖維纏繞不織布。.還有,由 依照針扎所獲得之層之面積收縮率爲25%。 以相同於實施例2之條件,進行所獲得之短纖維纏繞 不織布之蒸氣加熱處理及噴灑處理。然後,以相同於實施 例2之條件,藉由將聚胺甲酸酯彈性體A含浸賦予於該處 理後之短纖維纏繞不織布中,使PVA樹脂溶解去除,進一 步藉由進行聚胺甲酸酯彈性體A之含浸賦予、乾燥及於 150 °C之熱壓縮,可以獲得硏磨墊前驅物10。硏磨墊前驅物 10係基重量730 g/m2、表觀密度0.58 g/m3、厚度1.25 mm。 -52- 201120269 另外,不織布與聚胺甲酸酯彈性體A之質量比率爲8 0/2 0。 然後,藉由拋光硏削加工硏磨墊前驅物1〇,可以獲得 所平坦化的硏磨墊Π。利用電子顯微鏡以觀察硏磨墊11 之截面,極細纖維束之平均存在密度Di約爲1010個/mm2, 極細纖維束之平均存在密度D2約爲930個/mm2,Di/D2約 爲1.1。另外,於其截面中,觀察到由平均截面積約爲16//m2 之極細纖維所構成的平均截面積約爲35 0//m2之極細纖維 束。而且,極細纖維係藉由滲入極細纖維束內部之聚胺甲 酸酯彈性體所集束,另外,硏磨墊Π係基重量613 g/m2、 表觀密度0.58 g/m3、厚度1.06mm、D硬度35。而且’所 獲得之硏磨墊Π係相同於實施例1而實施加工、評估。將 結果顯不於表1。 〔比較例5〕 藉由從熔融複合紡紗用噴嘴(噴嘴溫度260°C )而使間 苯二甲酸改性PET噴出,形成間苯二甲酸改性PET之紗 束。然後,藉由設置於噴嘴正下方之.空氣噴射抽氣裝置而 拉伸從噴嘴所噴出之紗束,一邊拉伸而細化且一邊冷卻而 紡紗平均纖度〇.2dtex之間苯二甲酸改性PET長纖維。然 後,藉由在設置於空氣噴射抽氣裝置之正下方的移動式網 上進行連續收集PET長纖維,獲得基重30 g/m2之PET的 紡紗黏合片(長纖維棉網)。 接著,藉由交叉拋光而重疊1 2片之所獲得之紡紗黏合 片,製作總基重爲3 60 g/m2之棉網積層體。然後’進行相 同於實施例1,藉由針扎處理所獲得之棉網積層體’獲得 -53- .201120269 不織布。然後,藉由將所獲得之不織布9 0秒鐘浸漬於7 0 °C 之熱水中而使其應力緩和,使得面積收縮7 %。如此所熱水 處理的不織布之表觀密度爲0.25 g/cm3。 然後’以相同於實施例1之條件,藉由將聚胺甲酸酯 彈性體A含浸賦予所熱水處理的不織布中,進一步於150 °C 進行熱壓縮而可以獲得硏磨墊前驅物JO。硏磨墊前驅物JO 係基重量390 g/m2、表觀密度0.25 g/cm3、厚度1.55 mm。 另外’不織布與聚胺甲酸酯彈性體A之質量比率爲88/12。 然後,藉由拋光硏削加工硏磨墊前驅物〗0,可以獲得 所平坦化的硏磨墊Π。利用電子顯微鏡以觀察硏磨墊J1 之截面,觀察到未形成纖維束之平均截面積約爲20//m2之 極細纖維。另外,極細纖維橫截面之平均存在密度D ,約爲 300個/mm2,極細纖維橫截面之平均存在密度D2約爲300 個/mm2,D"D2約爲1.0。另外,硏磨墊J1係基重量315 g/m2、表觀密度 0.25 g/cm3、厚度 1 .25 mm、D 硬度 28。 而且,所獲得之硏磨墊J 1係相同於實施例1而予以加工。 還有,磨損重量減輕測定之結果,由於重量大幅減輕,硏 磨評估係被省略。 由表1之結果,關於本發明之實施例1至4中任一種 硏磨墊皆具有優異的硏磨速率、硏磨均一性、耐磨損性、 平坦化性能、耐刮傷性。另一方面,D"D2爲1 . 1之比較例 1的硏磨墊之情形,由於剛性高,硏磨速率係優異,但是 由於隨動性低,硏磨均一性差,另外,耐磨損性低。另一 方面,D"D2爲6之比較例2的硏磨墊之情形,由於剛性低, 硏磨速率低,另外,隨動性過高而平坦化性能變差。另外, -54- 201120269 使用海島型複合纖維之短纖維所獲得之比較例3及比較例 4的硏磨墊之情形,無法形成纖維之高密度化。因此,僅 獲得剛性低的硏磨墊,耐磨損性低。另外,使用以紡紗黏 合法所直接形成的極細纖維之不織布所獲得之比較例5的 硏磨糊之情形也無法形成纖維之高密度化。因此,僅獲得 剛性低的硏磨墊,耐磨損性低。 產業上利用之可能性 關於本發明之硏磨墊能夠作爲用以硏磨進行平坦化或 鏡面化之各種元件、各種基板等之各種製品使用,例如, 半導體基板、半導體元件、化合物半導體元件.、化合物半 導體基板、化合物半導體製品、LED基板、LED製品、矽 晶圓、硬碟基板、玻璃基板、玻璃製品、金屬基板、金屬 製品、塑膠基板、塑膠製品、陶瓷基板、陶瓷製品等》 【圖式簡單說明】 第1圖係本實施形態的硏磨墊10之示意縱截面圖。 第2圖係本實施形態的硏磨墊10之部分放大示意圖。 第3圖係本實施形態的用於化學機械硏磨之CMP裝置 20之槪略圖。 【主要元件符號說明】 1 不 織 布 la 極 細 纖 維 lb 極 細 纖 維 之 纖 維 束 2 闻 分 子 彈 性 體 3 硏 磨 面 ( 第 — 表 面) -55- 201120269 4 固定面(第二表面) 10 硏磨塾 Ri 從硏磨面3之表面起而朝厚度方向 厚度區域 20%以內之 r2 從固定面4之表面起而朝厚度方向 厚度區域 20%以內之 r3 從硏磨面3之表面起而朝厚度方向 之厚度區域 40 至 60% 11 旋轉固定盤 12 糊供應噴嘴 13 載體 14 墊調節器 15 被硏磨基材 16 硏磨糊 20 CMP裝置 -56-c I 201120269 [Example 2] The steam heating of the wound cotton web obtained in Example 1 was carried out under the conditions of an ambient temperature of 60 ° C and a relative humidity of 80% for 500 seconds. Then, for the steam-treated wound web, the surface of the wound web was compressed only by a heat roller of i2 °C. In the dry state, the area shrinkage of the wound web by the steam heat treatment and the compression treatment was 40%. Then, an aqueous emulsion of a polyurethane elastomer A having a solid concentration of 15% by mass was impregnated into the wound cotton web after the treatment. Next, by coagulation treatment of a non-woven fabric impregnated with an aqueous emulsion in a 90 ° C, 50% RH gas atmosphere, the drying treatment was further carried out at 150 ° C to form a wound cotton web and a polyurethane elastomer A. Composite (wound cotton composite). Further, in the solid matter of the polyurethane elastomer A, the aqueous emulsion was impregnated with 7 mass% based on the total mass of the wound cotton web composite. Then, the PVA resin is dissolved and removed by immersing the obtained wound cotton web composite in 95 t of hot water for 10 minutes, and further, by drying, a nonwoven fabric and a polyamine composed of fiber bundles of ultrafine fibers are formed. A complex of formate elastomer A (nonwoven composite). Then, the aqueous emulsion of the polyurethane elastomer A adjusted to a solid concentration of 25% by mass was further impregnated into the nonwoven fabric composite. In terms of the solid content of the polyurethane elastomer A, the aqueous emulsion was impregnated with 15% by mass based on the total mass of the nonwoven fabric. Next, the coagulation treatment of the non-woven fabric impregnated with the aqueous emulsion is carried out in a gas atmosphere of 90 ° C and 50% RH, and further dried at 15 ° C, and further at 15 ° C for -43 - 201120269 The honing pad precursor BO can be obtained by hot compression. The base of the honing pad precursor is 73 0 g/m2, the apparent density is 0.58 g/m3, and the thickness is 1.26 mm. Further, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 80 /2. Then, by polishing the honing pad precursor B0, the flattened honing pad B 1 can be obtained. Using an electron microscope to observe the cross section of the honing pad B1, the average density D of the ultrafine fiber bundles was about 2,450/mm2, and the average density D2 of the ultrafine fiber bundles was about 1,260/mm2, and DWD2 was about 1.9. Further, in the cross section thereof, an ultrafine fiber bundle having an average cross-sectional area of about 325 / / m 2 composed of ultrafine fibers having an average cross-sectional area of about 12 / / m 2 was observed. Further, the ultrafine fibers are bundled by the polyurethane elastomer penetrating into the inside of the ultrafine fiber bundle, and the lining pad B1 has a basis weight of 614 g/m2, an apparent density of 0.58 g/m3', a thickness of 1.06 mm, and D. Hardness 36. Moreover, the obtained honing pad B 1 was processed and evaluated in the same manner as in Example 1. The results are shown in Table 1. [Example 3] The steam heating of the wound cotton web obtained in Example 1 was carried out under the conditions of an ambient temperature of 80 ° C, a relative humidity of 80%, and 500 seconds. Then, for the steam-treated wound web, the surface of the wound web was compressed only by a heat roller of 120 °C. In the dry state, the area shrinkage of the wound web by the steam heat treatment and the compression treatment is 50%. Then, an aqueous emulsion of a polyurethane elastomer A having a solid concentration of 15% by mass was impregnated into the wound cotton web after the treatment. Next, the coagulation treatment of the non-woven fabric impregnated with the aqueous emulsion was carried out in a 90 ° C, 50% RH gas atmosphere, and further dried at 150 ° C to form a wound cotton web and a polyurethane elastomer - 44 - 201120269 A complex. Further, the aqueous emulsion was impregnated with 7 mass% in terms of the solid content of the polyurethane elastomer A with respect to the entire mass of the wound web composite. Then, the PVA resin is dissolved and removed by immersing the wound cotton web composite in hot water at 95 ° C for 10 minutes, and further, by drying, a nonwoven fabric composed of a fiber bundle of ultrafine fibers and a polyurethane are formed. A composite of ester elastomer A. Then, the aqueous emulsion of the polyurethane elastomer A adjusted to a solid concentration of 25% by mass was further impregnated into the nonwoven fabric composite. In terms of the solid content of the polyurethane elastomer A, the aqueous emulsion was impregnated with 15% by mass based on the total mass of the nonwoven fabric. Next, the coagulation treatment of the non-woven fabric impregnated with the aqueous emulsion was carried out in a 90 ° C, 50% RH gas atmosphere, and further dried at 150 ° C, and further hot-pressed at 15 ° C to obtain 硏. Grinding pad precursor C0. The honing pad precursor C0 has a weight of 790 g/m2, an apparent density of 0.63 g/m3, and a thickness of 1_25 mm. Further, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 80 /2. Then, by polishing the honing pad precursor C0 by polishing, the flattened honing pad C1 can be obtained. Using an electron microscope to observe the cross section of the honing pad C1, the average density D of the ultrafine fiber bundles is about 2840/mm2'. The average density D2 of the ultrafine fiber bundles is about 1 890/mm2, and the Di/Dz is about 1.5. . Further, in the cross section thereof, an ultrafine fiber bundle having an average cross-sectional area of about 325 / / m 2 composed of ultrafine fibers having an average cross-sectional area of about 13 / / m 2 was observed. Further, the ultrafine fibers are bundled by the polyurethane elastomer which penetrates into the inside of the ultrafine fiber bundle, and the honing pad C1 has a basis weight of 650 g/m2, an apparent density of 0.63 g/m3, a thickness of 1.03 mm, and D. Hardness 37. And -45-201120269, the obtained honing mat c 1 was processed and evaluated in the same manner as in Example 1. The results are not shown in Table 1. [Example 4] A 12-piece spunbonded sheet obtained in the same manner as in Example 1 was superposed by cross-polishing to prepare a cotton web laminate having a total basis weight of 480 g/m2. Then, the needle breaking oil is prevented from being sprayed on the obtained web laminate. Then, the cotton web layering system uses the needle cotton yarn count No. 42 and the hook number one needle, and the needle cotton yarn count No. 42 and the hook number six needles to take the needle depth from the first surface side thereof. The needle is treated to a depth of 25 mm and a condition of 1 200 ties/cm 2 , and the needle is further needled from the second surface side with a needle depth of 〇 to a depth of 1 〇 mm and a number of sheets of 300 扎/cm 2 . Tie processing. The area shrinkage of the cotton web laminate due to needle sticking is 20%. By such a needle treatment, a wound web having a basis weight of 5 60 g/m 2 and an interlaminar peel strength of 9.0 kg/2.5 cm can be obtained. The steam heating of the obtained wound cotton web was carried out under the conditions of an ambient temperature of 60 ° C, a relative humidity of 70%, and a temperature of 500 seconds. Then, for the steam-treated heat-treated wound web, the surface was compressed only by a heat roller of 110 t:. The area shrinkage of the wound web caused by the steam heat treatment and the compression treatment in the dry state was 35 %. Then, an aqueous emulsion of the polyurethane elastomer A having a solid content concentration of 15% by mass was impregnated into the wound cotton web after the treatment. Next, the coagulation treatment of the non-woven fabric impregnated with the aqueous emulsion was carried out in a 90 ° C, 50% RH gas atmosphere, and further dried at 150 ° C to form a composite of the wound cotton web and the polyurethane elastomer A. body. Further, in terms of the solid content of the polyurethane elastomer A, the aqueous emulsion is impregnated with 7% by mass relative to the entire mass of the -46 - 201120269 wound cotton web composite, and then the wound cotton web composite is The PVA resin is immersed in hot water at 95 ° C for 1 minute to dissolve and remove the PVA resin, and further formed by drying to form a non-woven fabric composed of the fiber bundle of the ultrafine fibers and the non-woven fabric of the polyurethane body A body. Then, the aqueous emulsion of the polyurethane elastomer A adjusted to a solid concentration of 25% by mass was further impregnated into the nonwoven fabric composite. In terms of the solid content of the polyurethane elastomer A, the aqueous emulsion was impregnated with 15% by mass based on the total mass of the nonwoven fabric. Next, the coagulation treatment of the non-woven fabric impregnated with the aqueous emulsion was carried out in a 90 ° C, 50% RH gas atmosphere, and further dried at 150 ° C, and further heat-compressed at 150 ° C to obtain a honing pad. Precursor E0. The honing pad precursor E0 has a weight of 66 5 g/m2, an apparent density of 0.53 g/m3, and a thickness of 1.25 mm. Further, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 80/20. Then, the flattened honing pad E 1 can be obtained by polishing the honing pad precursor E0. Using an electron microscope to observe the cross section of the honing pad E 1 , the average density D of the ultrafine fiber bundles was about 2,300 / mm 2 , and the average density D 2 of the ultrafine fiber bundles was about 540 / mm 2 , which was about 4.3. Further, in the cross section thereof, an ultrafine fiber bundle having an average cross-sectional area of about 325 / / m 2 composed of ultrafine fibers having an average cross-sectional area of about 11 μm 2 was observed. Further, the ultrafine fibers are bundled by a polyurethane elastomer which penetrates into the inside of the ultrafine fiber bundle, and the honing pad E1 has a basis weight of 559 g/m2, an apparent density of 5353 g/m3, and a thickness of 1.05 mm. D hardness 34. Further, the obtained honing pad E 1 was processed and evaluated in the same manner as in Example 1. The results -47- 201120269 are not shown in Table 1. [Comparative Example 1] A 12-piece spunbonded sheet obtained in the same manner as in Example 1 was superposed by cross-polishing to prepare a cotton web laminate having a total basis weight of .480 g/m2. Then/will prevent the needle breakage agent from being sprayed onto the obtained web laminate. Then, 'the cotton mesh layering system uses the needle cotton yarn count No. 42 and the hook number six needles' to have a depth of 1 〇 to 15 5 from the first surface side and the second surface side thereof, respectively, and the number of the stitches. Needle treatment was performed at a total of 1 800 oz/cm 2 under the conditions of 900 扎/cm 2 . The area shrinkage of the cotton web laminate due to needle sticking is 30%. By this needle-punching treatment, a wound web having a basis weight of 600 g/m 2 and an interlaminar peeling strength of 11.0 kg/2.5 cm can be obtained. Hereinafter, the PVA resin was dissolved and removed by hot water treatment of the wound cotton web under the same conditions as in Example 1, and further impregnated to impart polyurethane elastomer A, further by thermal compression at 150 ° C. The honing pad precursor F0 can be obtained. The honing pad precursor F0 has a basis weight of 740 g/m2, an apparent density of 0.63 g/m3, and a thickness of 1.17 mm. In addition, the mass ratio of the nonwoven fabric to the polyurethane elastomer A is 87/13. Then, by polishing the honing pad precursor F0, the flattened honing pad F 1 can be obtained. Using an electron microscope to observe the cross section of the honing pad F1, the average density D of the ultrafine fiber bundles is about 2550/mm2, and the average density D2 of the ultrafine fiber bundles is about 2 3 40/mm2, and Di/D2 is about Is 1.1. Further, in the cross section thereof, an ultrafine fiber bundle having an average cross-sectional area of about 305 Å consisting of ultrafine fibers having an average cross-sectional area of about 14 Å was observed. Further, the ultrafine fibers are bundled by the poly-48-201120269 urethane elastomer which penetrates into the inside of the ultrafine fiber bundle, and the lining pad F1 has a basis weight of 613 g/m2, an apparent density of 0.63 g/m3, and a thickness. 0.98 mm, D hardness 38. Moreover, the obtained honing mat F 1 was processed and evaluated in the same manner as in Example 1. The results are shown in Table 1. [Comparative Example 2] A 12-piece spunbonded sheet obtained in the same manner as in Example 1 was superposed by cross-polishing to prepare a cotton web laminate having a total basis weight of 480 g/m2. Then, the needle breaking oil is prevented from being sprayed on the obtained web laminate. Next, the cotton web layering system sequentially uses needle cotton yarn count No. 42, needle number one needle, and needle cotton yarn count No. 42 and hook number six needles to have a needle depth of 5 from the first surface side thereof. The needle was treated to a depth of 25 mm and a number of sheets of 1,200 扎/cm 2 , and further needled from the second surface side with a needle depth of 〇 to a depth of 5 mm and a number of sheets of 300 ž/cm 2 Tie processing. The area shrinkage of the cotton web laminate due to needle sticking is 20%. By such a needle treatment, a wound web having a basis weight of 560 g/m 2 and an interlayer peel strength of 9.4 kg/2.5 cm can be obtained. The steam heating of the obtained wound cotton web was carried out under the conditions of an ambient temperature of 60 ° C, a relative humidity of 70%, and a temperature of 500 seconds. Then, for the steam-treated heat-treated wound web, the surface of the wound web was compressed only by a hot roll of ll ° ° C. In the dry state, the area shrinkage of the wound web caused by the steam heat treatment and the compression treatment is 35% » Then, the aqueous emulsion of the polyurethane elastomer A having a solid concentration of 15% by mass is impregnated In the wound cotton web after the treatment. Next, the solidification treatment of the non-woven fabric impregnated with the aqueous emulsion is carried out in a 90 ° C, 50% RH gas atmosphere, and further dried at -5 〇 ° C -49-201120269 to form a wound cotton web and a polyamine. A complex of formic acid acetate elastomer A. Also, 'in terms of the solid content of the polyurethane elastomer A, relative to the entire mass of the wound cotton web composite, the aqueous emulsion is impregnated with 7 mass%. Then, by winding the cotton web composite at 95 heat The PVA resin was dissolved and removed in water for 10 minutes, and further, by drying, a nonwoven fabric composed of a nonwoven fabric composed of ultrafine fibers and a polyurethane nonwoven fabric A was formed. Then, the aqueous emulsion of the polyurethane elastomer A adjusted to a solid concentration of 25% by mass was further impregnated into the nonwoven fabric composite. The aqueous emulsion was impregnated with 15% by mass in terms of the solid content of the polyurethane elastomer A in terms of the total mass of the nonwoven fabric. Then, the solidification treatment of the non-woven fabric impregnated with the aqueous emulsion was carried out in a 90 ° C, 50% RH gas atmosphere, and further dried at 150 ° C, and further hot-pressed at 15 ° C to obtain 硏. Grinding pad precursor G0. The honing pad precursor G0 base weight 665 g/m2 'apparent density 0.53 g/m3, thick 莩 1.25 mm. Further, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 80 /2. Then, by polishing the honing pad precursor G0 by polishing, the flattened honing pad G 1 can be obtained. Using an electron microscope to observe the cross section of the honing pad G 1 , the average density D of the ultrafine fiber bundle is about 2400 / mm 2 , and the average density D 2 of the ultrafine fiber bundle is about 400 / mm 2 , and the Di / D 2 is about 6.0. . Further, in the cross section thereof, an ultrafine fiber bundle having an average cross-sectional area of about 3 25 pm2 composed of ultrafine fibers having an average cross-sectional area of about n was observed. Further, the ultrafine fibers are bundled by the polyurethane elastomer which penetrates into the inside of the ultrafine fiber bundle, and the guillotine G1 has a basis weight of 559 g/m2, -50 to 201120269, an apparent density of 0.53 g/m3, and a thickness l. .〇5mm, D hardness 34. Further, the obtained honing pad E 1 was processed and evaluated in the same manner as in Example 1. The results are shown in Table 1. [Comparative Example 3] In the same manner as in Example 1, long fibers were obtained by winding a sea-island type composite fiber yarn bundle discharged from a nozzle at 3 000 m/miri. Then, by winding and cutting the obtained long fibers, short fibers having a cut length of 30 mm were obtained. Then, the obtained short fibers were needled under the same conditions as in Example 1. By such a needle-punching treatment, a short-fiber wound non-woven fabric having a basis weight of 600 g/m 2 and an interlayer peeling strength of 7.5 kg/2.5 cm can be obtained. Further, the area shrinkage ratio of the sheet obtained by the needle sticking was 25 %. Using the obtained short fiber wound non-woven fabric instead of the wound cotton web, the PVA resin was dissolved and removed under the same conditions as in Example 1, to obtain a non-woven fabric having an apparent density of 0.35 g/m3. Further, when the PVA resin is dissolved and removed, the ultrafine fibers are frequently detached by winding the non-woven fabric with the large-stretched short fibers. Then, the impregnated pad precursor H0 was obtained by further impregnating the polyurethane nonwoven A with the obtained nonwoven fabric and further heat-compressing at 150 °C. The honing pad precursor H0 has a basis weight of 480 g/m2, an apparent density of 0.43 g/m3, and a thickness of 1.15 mm. Further, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 87/13. Then, by polishing the honing pad precursor H0, the flattened honing pad 1 can be obtained. Using an electron microscope to observe the cross section of the honing pad 1, the average density D1 of the ultrafine fiber bundle is about 350/mm2, and the average density D2 of the ultrafine fiber bundle is about 350/mm2, D!/D2 about -51. - 201120269 is 1.0» In addition, in its cross section, an ultrafine fiber bundle composed of ultrafine fibers having an average cross-sectional area of about 16//m2 and having an average cross-sectional area of about 3,500/min2 was observed. Further, the ultrafine fibers are bundled by the polyurethane elastomer penetrating into the inside of the ultrafine fiber bundle, and the honing pad H1 has a basis weight of 3 97 g/m2, an apparent density of 0.42 g/m3, and a thickness of 0.95 mm. D hardness 27. Further, the obtained honing pad H1 was processed and evaluated in the same manner as in Example 1. The results are shown in Table 1. Further, the honing evaluation is omitted because the short fibers are entangled with the nonwoven fabric, and the extremely fine fibers are frequently peeled off. [Comparative Example 4] In the same manner as in Example 1, long fibers were obtained by winding a sea-island type composite fiber yarn bundle which was sown from a nozzle at 3000 m/min. Then, by winding and cutting the obtained long fibers, short fibers having a cut length of 30 mm were obtained. Then, the obtained short fibers were needled under the same conditions as in Example 1. By such a needle-punching treatment, a short-fiber wound non-woven fabric having a basis weight of 600 g/m 2 and an interlayer peeling strength of 7 kg/2.5 cm can be obtained. Also, the area shrinkage rate of the layer obtained by the needle stick is 25%. The steam heat treatment and the spray treatment of the obtained short fiber wound nonwoven fabric were carried out under the same conditions as in Example 2. Then, the PVA resin was dissolved and removed by subjecting the polyurethane elastomer A to the treated short fiber-wound nonwoven fabric under the same conditions as in Example 2, further by performing the polyurethane. The honing pad precursor 10 can be obtained by impregnation, drying and thermal compression of the elastomer A at 150 °C. The honing pad precursor 10 base weight 730 g / m2, apparent density 0.58 g / m3, thickness 1.25 mm. -52- 201120269 In addition, the mass ratio of the nonwoven fabric to the polyurethane elastomer A was 8 0/2 0. Then, by polishing the honing pad precursor 1 〇, the flattened honing pad can be obtained. Using an electron microscope to observe the cross section of the honing pad 11, the average density D of the ultrafine fiber bundles was about 1010/mm2, and the average density D2 of the ultrafine fiber bundles was about 930/mm2, and the Di/D2 was about 1.1. Further, in the cross section thereof, an ultrafine fiber bundle having an average cross-sectional area of about 35 0 / / m 2 composed of ultrafine fibers having an average cross-sectional area of about 16 / / m 2 was observed. Further, the ultrafine fibers are bundled by the polyurethane elastomer which penetrates into the inside of the ultrafine fiber bundle, and the lining base weight is 613 g/m2, the apparent density is 0.58 g/m3, and the thickness is 1.06 mm, D. Hardness 35. Further, the obtained honing pad was processed and evaluated in the same manner as in Example 1. The results are not shown in Table 1. [Comparative Example 5] The isophthalate-modified PET was discharged from a nozzle for melt-composite spinning (nozzle temperature: 260 ° C) to form a yarn of isophthalic acid-modified PET. Then, the yarn bundle ejected from the nozzle is stretched by an air jet pumping device disposed directly below the nozzle, and is stretched and refined while cooling, and the average fineness of the spinning is 〇. 2dtex. PET long fiber. Then, by continuously collecting PET long fibers on a mobile net disposed directly below the air jet suction device, a spunbonded sheet (long fiber web) of PET having a basis weight of 30 g/m2 was obtained. Next, a spun yarn obtained by laminating 12 sheets by cross-polishing was used to prepare a web laminate having a total basis weight of 3 60 g/m2. Then, the same procedure as in Example 1 was carried out, and the web laminate obtained by the needle-punching treatment was obtained as -53-.201120269 non-woven fabric. Then, the obtained non-woven fabric was immersed in hot water of 70 ° C for 90 seconds to relax the stress, so that the area was shrunk by 7%. The non-woven fabric treated with such hot water has an apparent density of 0.25 g/cm3. Then, under the same conditions as in Example 1, the polyurethane precursor A was impregnated into the non-woven fabric subjected to the hot water treatment, and further heat-compressed at 150 °C to obtain the honing pad precursor JO. The honing pad precursor has a weight of 390 g/m2, an apparent density of 0.25 g/cm3, and a thickness of 1.55 mm. Further, the mass ratio of the non-woven fabric to the polyurethane elastomer A was 88/12. Then, by polishing the honing pad precursor "0", the flattened honing pad can be obtained. An electron microscope was used to observe the cross section of the honing pad J1, and an ultrafine fiber having an average cross-sectional area of about 20//m2 which was not formed into a fiber bundle was observed. Further, the average density of the cross section of the ultrafine fibers is about 300/mm2, and the average density D2 of the cross section of the ultrafine fibers is about 300/mm2, and D"D2 is about 1.0. In addition, the honing pad J1 has a basis weight of 315 g/m2, an apparent density of 0.25 g/cm3, a thickness of 1.25 mm, and a D hardness of 28. Further, the obtained honing pad J 1 was processed in the same manner as in Example 1. Also, as a result of the wear weight reduction measurement, the honing evaluation was omitted because the weight was greatly reduced. From the results of Table 1, the honing pads of any of Examples 1 to 4 of the present invention have excellent honing rate, honing uniformity, abrasion resistance, flattening property, and scratch resistance. On the other hand, in the case of the honing pad of Comparative Example 1 in which D"D2 is 1.1, since the rigidity is high, the honing rate is excellent, but since the followability is low, the honing uniformity is poor, and the wear resistance is further improved. low. On the other hand, in the case of the honing pad of Comparative Example 2 in which D"D2 is 6, the rigidity is low, the honing rate is low, and the followability is too high, and the flattening performance is deteriorated. Further, in the case of the honing pads of Comparative Example 3 and Comparative Example 4 obtained by using the short fibers of the sea-island type composite fiber, the density of the fibers could not be formed. Therefore, only the honing pad having low rigidity is obtained, and the wear resistance is low. Further, in the case of the honing paste of Comparative Example 5 obtained by using the nonwoven fabric of the ultrafine fibers directly formed by the spunbonding, the density of the fibers could not be formed. Therefore, only the honing pad having low rigidity is obtained, and the wear resistance is low. INDUSTRIAL APPLICABILITY The honing pad of the present invention can be used as various products for honing and planarizing various elements, various substrates, and the like, for example, a semiconductor substrate, a semiconductor element, and a compound semiconductor element. Compound semiconductor substrate, compound semiconductor product, LED substrate, LED product, germanium wafer, hard disk substrate, glass substrate, glass product, metal substrate, metal product, plastic substrate, plastic product, ceramic substrate, ceramic product, etc. Brief Description of the Drawings Fig. 1 is a schematic longitudinal cross-sectional view of a honing pad 10 of the present embodiment. Fig. 2 is a partially enlarged schematic view showing the honing pad 10 of the present embodiment. Fig. 3 is a schematic view showing a CMP apparatus 20 for chemical mechanical honing of the present embodiment. [Explanation of main component symbols] 1 Non-woven fabric la Microfiber lb Microfiber fiber bundle 2 Smoked molecular elastomer 3 Honest surface (surface - surface) -55- 201120269 4 Fixed surface (second surface) 10 硏Ri Ri from 硏R3 from the surface of the grinding surface 3 to the thickness region of 20% in the thickness direction from the surface of the fixing surface 4 and r3 within 20% of the thickness region in the thickness direction from the surface of the honing surface 3 to the thickness region in the thickness direction 40 to 60% 11 rotary fixed disk 12 paste supply nozzle 13 carrier 14 pad conditioner 15 honed substrate 16 硏 20 20 CMP device - 56-
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| JP2009249974 | 2009-10-30 |
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| JP (1) | JP5629266B2 (en) |
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| WO (1) | WO2011052173A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI610389B (en) * | 2016-09-05 | 2018-01-01 | 詠巨科技有限公司 | Polishing pad conditioning method, polishing pad conditioning device and chemical mechanical planarization system |
| TWI808227B (en) * | 2018-08-09 | 2023-07-11 | 日商荏原製作所股份有限公司 | Substrate cleaning device and substrate cleaning method |
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| US7892993B2 (en) | 2003-06-19 | 2011-02-22 | Eastman Chemical Company | Water-dispersible and multicomponent fibers from sulfopolyesters |
| US8513147B2 (en) | 2003-06-19 | 2013-08-20 | Eastman Chemical Company | Nonwovens produced from multicomponent fibers |
| US20040260034A1 (en) | 2003-06-19 | 2004-12-23 | Haile William Alston | Water-dispersible fibers and fibrous articles |
| US8512519B2 (en) | 2009-04-24 | 2013-08-20 | Eastman Chemical Company | Sulfopolyesters for paper strength and process |
| US9273417B2 (en) | 2010-10-21 | 2016-03-01 | Eastman Chemical Company | Wet-Laid process to produce a bound nonwoven article |
| US8840757B2 (en) | 2012-01-31 | 2014-09-23 | Eastman Chemical Company | Processes to produce short cut microfibers |
| US9303357B2 (en) | 2013-04-19 | 2016-04-05 | Eastman Chemical Company | Paper and nonwoven articles comprising synthetic microfiber binders |
| JP6180873B2 (en) * | 2013-08-30 | 2017-08-16 | 株式会社クラレ | Fiber composite sheet, polishing pad and manufacturing method thereof |
| US9605126B2 (en) | 2013-12-17 | 2017-03-28 | Eastman Chemical Company | Ultrafiltration process for the recovery of concentrated sulfopolyester dispersion |
| US9598802B2 (en) | 2013-12-17 | 2017-03-21 | Eastman Chemical Company | Ultrafiltration process for producing a sulfopolyester concentrate |
| JP6355429B2 (en) * | 2014-05-22 | 2018-07-11 | 株式会社ディスコ | Polishing pad manufacturing method |
| KR101848165B1 (en) * | 2016-10-28 | 2018-04-11 | 현대제철 주식회사 | Analyzing method for carbon fiber tow of carbon fiber reinforced plastics |
| JP7156341B2 (en) * | 2020-07-13 | 2022-10-19 | 信越半導体株式会社 | Single-sided polishing apparatus, single-sided polishing method, and polishing pad |
| JP7721681B2 (en) * | 2021-05-11 | 2025-08-12 | スリーエム イノベイティブ プロパティズ カンパニー | Tooled device for robotic paint repair |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP3901939B2 (en) * | 2000-12-05 | 2007-04-04 | 帝人コードレ株式会社 | Polishing base fabric and polishing method |
| JP3815226B2 (en) * | 2001-01-31 | 2006-08-30 | 東レ株式会社 | Polishing cloth |
| WO2008093850A1 (en) * | 2007-02-01 | 2008-08-07 | Kuraray Co., Ltd. | Polishing pad and process for production of polishing pad |
| JP5289787B2 (en) * | 2007-02-01 | 2013-09-11 | 株式会社クラレ | Polishing pad and polishing pad manufacturing method |
| US20100075143A1 (en) * | 2007-03-07 | 2010-03-25 | Toray Industries, Inc. | Fiber structure and method for production thereof |
| JP2009083093A (en) * | 2007-09-13 | 2009-04-23 | Toray Ind Inc | Polishing cloth |
| JP5248152B2 (en) * | 2008-03-12 | 2013-07-31 | 東洋ゴム工業株式会社 | Polishing pad |
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2010
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- 2010-10-22 WO PCT/JP2010/006269 patent/WO2011052173A1/en not_active Ceased
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI610389B (en) * | 2016-09-05 | 2018-01-01 | 詠巨科技有限公司 | Polishing pad conditioning method, polishing pad conditioning device and chemical mechanical planarization system |
| TWI808227B (en) * | 2018-08-09 | 2023-07-11 | 日商荏原製作所股份有限公司 | Substrate cleaning device and substrate cleaning method |
Also Published As
| Publication number | Publication date |
|---|---|
| TWI513871B (en) | 2015-12-21 |
| JPWO2011052173A1 (en) | 2013-03-14 |
| WO2011052173A1 (en) | 2011-05-05 |
| JP5629266B2 (en) | 2014-11-19 |
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