TWI284055B - Microporous filter media, filtration systems containing same, and methods of making and using - Google Patents
Microporous filter media, filtration systems containing same, and methods of making and using Download PDFInfo
- Publication number
- TWI284055B TWI284055B TW092102104A TW92102104A TWI284055B TW I284055 B TWI284055 B TW I284055B TW 092102104 A TW092102104 A TW 092102104A TW 92102104 A TW92102104 A TW 92102104A TW I284055 B TWI284055 B TW I284055B
- Authority
- TW
- Taiwan
- Prior art keywords
- microbial
- microporous structure
- active particles
- filter medium
- particles
- Prior art date
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
- A61L2/022—Filtration
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
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- A61L2103/05—
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
- B01D29/13—Supported filter elements
- B01D29/15—Supported filter elements arranged for inward flow filtration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/39—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with hollow discs side by side on, or around, one or more tubes, e.g. of the leaf type
- B01D29/41—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with hollow discs side by side on, or around, one or more tubes, e.g. of the leaf type mounted transversely on the tube
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D37/02—Precoating the filter medium; Addition of filter aids to the liquid being filtered
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/18—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being cellulose or derivatives thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2003—Glass or glassy material
- B01D39/2017—Glass or glassy material the material being filamentary or fibrous
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- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
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- B01J20/08—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
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- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
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- B01J20/165—Natural alumino-silicates, e.g. zeolites
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- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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Description
1284055 玖、發明說明: 【發明所屬之技術領域】 本發明係關於具有微生物攔截能力之過濾介質、包含此 種過濾介質之過濾系統、及製造與使用該介質之方法。 【先前技術】 現代消費者濾水器時常提供“健康訴求”,包括粒子、重 金屬、毒性有機化學品、及特定之微生物威脅之減少。使 用約ι·ο微米結構,此等過濾系統已能夠攔截微生物諸如應 孢子蟲(Cryptosporidium)反梨形鞭毛蟲(Giardia) °然而,為 了提供甚至更小之微生物威脅諸如病毒之微生物攔截,具 有次微米微多孔性結構之過濾介質係需要的。先前技藝過 滤系統時常使用具有不足夠小之細孔尺寸及具有不良之物 理完整性之過濾介質,以企圖達成寬廣範圍之微生物攔 截。於對於成功之微生物攔截所需要之必要之細孔結構與 令人滿意之過滤性能所需要之必要之細孔結構之間之平衡 尚未達成。 【發明内容】 發明摘述 於第一項態樣中,本發明係關於一種過濾介質,該過滤 介負包含·包含活性粒子之排列之微多孔性結構,該微多 孔性結構具有小於約2微米之平均流動路徑;及微生物搁截 增進劑,該微生物攔截增進劑包含吸附於至少—部分之該 微多孔性結構上之具有中等至高之電荷密度及大於約 5,000道耳呑(Daltons)之分子量之陽離子性材料、及於直接 鄰近於該陽離-子性材料並亦於至少一部分之謗微多孔性結 83162 1284055 構上之生物活性之金屬。 於另一項態樣中,本發明係關於一種過滤系統,該過減 系統包含··具有一入口及一出口之殼;位於該殼之内於與 該等入口及出口流體相通之過濾介質,該過濾介質包含: 具有小於約2微米之平均流動路徑包含活性碳、活性鋁氧' 沸石、矽藻土、矽酸鹽、鋁矽酸鹽、鈦酸鹽、骨炭、氫氧 磷灰石鈣、鎂氧化物、鐵氧化物、鎂氧、珍珠岩、滑石、 聚合之粒子、黏土、經碘化之樹脂、離子交換樹脂、陶磁、 或其等之組合之活性粒子之微多孔性結構;及微生物攔截 增進劑’該微生物攔截增進劑包含具有高之電荷密度、大 於約5,000道耳呑之分子量及具有與其缔合之相對離子之 陽離子性材料,該陽離子性材料吸附於至少一部分之該微 多孔性結構上,及其中使生物活性之金屬與至少一部分之 與涘1%離子性材料缔合之相對離子沉澱,其中流動通過該 殼及接觸該過濾介質之微生物污染之流入液,具有於自該 π又流動離開之流出液中之微生物污染物之至少約4對數減 少。 於再另一項態樣中,本發明係關於製造具有增進之微生 物攔截能力之過濾介質之一種方法,該方法包含下列步 騾:提供具有約0.1微米至約5,〇〇〇微米之平均粒子尺寸之活 性粒子;以微生物攔截增進劑處理該等活性粒子,該微生 物攔截增進劑包含具有高電荷密度及大於約5,000道耳呑 之刀子量之險離子性材料、及生物活性之金屬;及將該等 、、’二處理之/舌性粒子成型為具有低於約2微米之平均流動路 83162 1284055 徑之微多孔性結構。 再另員態樣中,本發明係關於製造具有增進之微生 物搁截能力之過滤介質之—種方法,該方法包含下列步 驟:提供具有約(U微米至約5,_微米之平均粒子尺寸之活 性粒子;將該等活性粒子聚結成為具有小於約2微米之平均 流,路徑之微多孔性結構;及以微生物攔截增進劑處理該 微多孔性結構’該微生物攔截增進劑包含具有高電荷密度 及大於約5,_道耳吞之分子量之陽離子性材料及生物活 性之金屬。 於另一項態樣中,本發明係關於自流體中移除微生物污 染物4 一種方法,該方法包含下列步驟:提供包含微多孔 性結構之過濾介質,該微多孔性結構包含活性粒子及具有 小於約2微米之平均流動路徑;及於至少一部分之該微多孔 性結構上吸附之微生物攔截增進劑,該微生物攔截增進劑 包含具有中等至高之電荷密度及大於約5,000道耳呑之分 子量之陽離子性材料、及生物活性之金屬;將微生物丨亏染 之流體接觸該過濾介質歷時小於或等於約丨2秒鐘之時間期 間,及獲得具有微生物污染物之大於約4對數去除率(4 i〇g reduction)之流出液。 發明之詳細說明 於敘述本發明之較佳具體實施例中,於本文中將參考圖 式之圖1。 定義 如於本文中使用,“吸收劑”應意表具有吸引物質進入其 83162 1284055 之内部結構中之能力之任何材料。 ‘如於本文中使用,“吸附劑,,應意表具有經由物理方法及 無任何共價鍵結而吸引物質至其之表面纟能力之任何材 料0 如於本文中使用,“黏合劑”應意表主要使用以將其他材 料保持一起之材料。 如於本文中使用,“污染物減少”應意表於流體中之雜質 之減少,該雜質係化學地、機械地或生物學地攔截、移除、 及/或使其不活性,俾能使該流體變成較安全如,例如,用 於人類使用,或較有用,如於工業應用中。 如於本文中使用,“空床接觸時間,,或“EBct”應意表當流 體流動通過粒子之床時,於粒子(諸如,例如,活性碳)與流 體之間發生多少接觸之量度。 如於本文中使用,“纖維,,應意表以高之長度對於直徑之 縱橫比(例如,數百比1)為特徵之固體。纖維之任何討論應 亦認為包括鬚晶。 如於本文中使用,“過濾介質,,應意表執行流體過濾之材 料。 如於本文中使用,“流體,,應意表液體、氣體、或其等之 組合。 如於本文中使用,“攔截,,或“攔截作用,,係採用以意表干 擾、或阻止通過,以求影響、移除、使去活性或改變。 如於本文中使用,“對數減少值,,或“LRV”應意表以於流入 液中之生物數目除以於流動通過濾器之後之流出液中之生 83162 -9- 1284055 物數目之i〇glQ。 如於本文中使用,“金屬,,應意表以包括指定之金屬元素 之鹽、膠體、沉澱、本體金屬(base metal)、及所有之其他 形式。 如於本文中使用,“微生物攔截增進之過濾介質,,應意表 具有微多孔性結構之過濾介質,其中至少一部份之該微多 孔性結構係以微生物攔截增進劑處理。 如於本文中使用,“微生物攔截增進劑,,應意表具有與其 缔合之相對離子之陽離子性材料與生物活性之金屬。 如於本文中使用,“微生物,,應意表可係懸浮於流體中之 任何活之生物,包括但不限於,細菌、病毒、真菌、原生 動物、及其等之可繁殖之形式,包括胞囊及孢子。 如於本文中使用,“微多孔性結構,,應意表具有小於約2〇 微米,及時常小於約1·〇微米,之平均流動路徑之結構。 如於本文中使用,“天然有機物質,,或“N〇M”應意表時常 於飲用水或非飲用水中找到之有機物質,其之一部份降低 或抑制帶正電荷之過濾介質之滲透,或仄他,電位。典型 之NOM係多陰離子酸諸如,但不限於,腐植酸及黃酸。 如於本文中使用,“非織物,,意表具有個別纖維(其等係互 相舖置,但不是於很有組織之方式如於針織或梭織之織品 中)之結構之網層或織品或其他介質。非織物網層通常可係 經由於此技藝中熟知之方法而製備。此等方法之實例包 括,但不限於,及僅當作舉例說明,橡吹、纺絲黏合、梳 理、及氣流舖置。 83162 • 10 - 1284055 如於本文中使用,“粒子”應意表具有膠體至肉眼可見之 範圍内之尺寸,及對於形狀無特定之限制,但通常屬於受 限制之長度比寬度比例之固體。 如於本文中使用,“預濾器”應意表通常於自其他過濾 層、結構或裝置之上游安置及具有於流入液接觸其後之過 濾層、結構或裝置之前減少粒子污染物之能力之過滤介質。 如於本文中使用,“鬚晶”應意表具有受限制之形狀比例 及於粒子與纖維之縱橫比之間之中間值之絲狀纖維。纖維 之任何討論應亦認為包括鬚晶。 微生物攔截增進之過濾介質 本發明之過滤介質具有微多孔性結構,其使用適合之細 孔結構與化學處理之組合而提供微生物攔截能力。該微多 孔性結構包含活性粒子之排列,其具有特定之細孔結構、 以及吸附劑及/或吸收劑性質。該排列可係使用黏合劑或支 持之纖維、及其類似物而形成為一致之介質之結合或固定 之粒子之固體複合物團塊、巨大之結構、陶瓷蝶燭形物、 平直之片板複合物。此等粒子排列可係經由於此技藝中已 知之方法而製造,諸如,例如,擠製、模製、或滑移澆鑄 (slip casting)。使用以處理微多孔性結構之表面之化學處理 方法利用於1%離子性材料與生物活性金屬之間之增效之交 互作用,當組合此等物質時,於接觸後提供微生物污染物 之寬廣範圍減少。由陽離子性材料提供予過濾介質之電荷 有助於微生物污染物之動電學之攔截,而緊密之細孔結構 提供短之擴散路徑及,因此,於流動之流體中之微生物污 83162 -11- 1284055 染物之快速擴散運動至微多孔性結構之表面。微多孔性於 構亦提供微生物污染物之補充之直接機械攔截。由於擴散 對於極小粒子之攔截之顯著之作用,因此於病毒粒子之對 數減少值與流入液於過濾介質内之接觸時間之間具有直接 之關係,而非依賴過濾介質之厚度而定。 微生物摘截增進之過濾介質之特性 為了提供完全之微生物攔截能力,本發明之微生物攔截 增進之過濾介質具有小於約2微米之平均流動路徑,及更佳 係小於或等於約1微米。倘若平均流動路徑係大於約2微 米’則病毒粒子之擴散效率快速地降低及不達成有效率之 微生物攔截。與通過本發明之微生物攔截增進之過濾介質 之流體之流率比較,該過濾介質之體積必須係足夠,以提 供對於污染物擴散至該過濾介質之表面係適合之接觸時 間。為了提供微生物(其之大部分係帶負電荷的)之增進之電 動之攔截,至少一部分之微多孔性結構係以陽離子性材料 塗佈,以於至少一部分之此微多孔性結構上產生正電荷。 該陽離子性材料係屬於足夠之分子大小,以避免活性粒子 之微-細孔及中_細孔之垢積。 天然有機物質(NOM),諸如多陰離子酸,即,腐植酸或 黃酸,其等可降低或移除於微生物攔截增進之過濾介質上 之電荷,較佳係經由實質上移除該1^〇汹之吸附劑預濾器之 使用而避免接觸該帶電荷之微多孔性結構。將移除之 材料直接組合入微生物攔截增進之過濾介質中,因而消除 分離之吸附劑預濾器之需要,係可能的。而且,視使用之 83162 -12- 1284055 活性粒子之類型而定,微生物攔截增進之過濾介質本身之 上游邵份可自然地減少或移除NOM及避免該微生物攔截增 進之過濾介質之下游部份之功能之損失。 當於重力·流動水過濾系統之情況下使用時,該微生物攔 截增進之過濾介質係以親水性材料製造或以潤濕劑處理以 提供良好、自發之可潤濕性,係較佳的。或者,於其他應 用中’可處理微生物攔截增進之過濾介質,以如需要提供 親水或疏水之特性。微生物攔截增進之過濾介質可具有帶 正電荷及帶負電荷及不帶電荷之區域,及/或親水及疏水之 區域,係可能的。例如,可使用帶負電荷之區域以增進較 不常見之帶正電荷之污染物之攔截,及可使用不帶電荷之 疏水之區域以提供吸引至疏水性表面之污染物之增進之攔 截。 活性粒子 本發明之具有增進之微生物攔截能力之微生物攔截增進 之過滤介質包含具有80x325篩目附隨約20%至約24%盤中 剩餘物(pan)(小於-325篩目之粒子)之粒子尺寸分布之吸附 劑及/吸收劑活性粒子之排列。該等活性粒子可包括,但不 限於,活性碳、活性鋁氧、沸石、矽藻土、矽酸鹽、銘碎 酸鹽、鈦酸鹽、骨炭、氫氧磷灰石鈣、鎂氧化物、鐵氧化 物、鎂氧、珍珠岩、滑石、聚合之粒子、黏土、經琪化之 樹脂、離子交換樹脂、陶磁、超吸收劑(SAP)、及其等之組 合。具有需要之性質之微生物攔截增進之過濾介質可係經 由組合一種或多種之此等活性粒子而獲得。 83162 -13- 1284055 一種較佳之微多孔性結構包含活性碳之活性粒子,該等 粒子本能地抵抗由NOM之垢積及對於吸附於微多孔性結構 之周圍區域中之潛在地干擾之NOM係有效率的,而同時保 護較内部區域。較佳地,該活性碳係經酸洗之以煙煤為基 礎之活性碳。適合於使用於本發明中之市售之活性碳可係 自 Pittsburgh,Pennsylvania之 Calgon Carbon Corporation以 商品名稱 TOG-NDS、或自 Wilmington,California之 California Carbon Company以商品名稱1240ALC獲得。最佳地,該等 活性粒子係由來自Calgon Carbon Corporation之經酸洗之 以煙煤為基礎之活性碳組成,具有如下之粒子尺寸分布: 约3%至約7%,較佳係約5%,80篩目尺寸粒子;約12%至約 18%,較佳係約15%,100篩目尺寸粒子;約44%至約50%, 較佳係47%,200篩目尺寸粒子;約8%至約14%,較佳係約 11%,325篩目尺寸粒子;及約20%至約24%盤中剩餘物, 較佳係約22%盤中剩餘物。 微生物攔截増進劑 微多孔性結構之活性粒子係以具有於該等活性粒子之表 面上產生正電荷之能力之微生物攔截增進劑化學處理。該 化學處理於經處理之表面上產生強之正電荷,如使用滲透 電位分析而測量,及於低於10之氫標(pH)值下維持此種正 電荷。陽離子性金屬錯合物係經由以陽離子性材料處理活 性粒子而於该等活性粒子之至少一部分之表面上生成。該 陽離子性材料可係小之帶電荷之分子、或沿著聚合物鏈之 長度具有帶正電荷之原子之線型或分枝之聚合物。 83162 -14- 1284055 倘若該陽離子性材料係聚合物,則電荷密度較佳係大於 · 、’·勺帶電%之原子母約每2〇埃(較佳係大於約i帶電荷之原 子每約每10埃,及更佳係大於約丨帶電荷之原子每約每5埃) 之分子長度。於陽離子性材料上之電荷密度愈高,則與其· 、’帝口之相對離子之濃度愈高。可使用高濃度之適合之相對 離子以驅動金屬錯合物之沉澱作用。該陽離子性聚合物之· 咼黾荷绝度提供吸附活性粒子諸如碳及重大地反轉其等之 r 正常負電荷之能力。不論於高或低之?11環境中,該陽離子 , 性材料應對於微多孔性結構均勻地提供高度帶正電荷之表 _ 面’如經由滲透或仄他電位分析器而測定。 足夠地高之分子量之聚合物之使用容許活性粒子之表面 之處理,而對於活性粒子之中-細孔及微-細孔之吸附能力無 嚴重之附隨影響。該陽離子性材料可具有大於或等於約 5,000道耳呑之分子量,較佳係大於或等於1〇〇 〇〇〇道耳呑, 更佳係大於或等於約400,000道耳呑,及可係大於或等於約 5,000,000道耳呑。 陽離子性材料包括,但不限於,成季鹼之胺、成季鹼之 籲 醯胺、第四級銨鹽、成季鹼之醯亞胺、苯二甲烴銨化合物 (benzalkonium compounds)、縮二胍、陽離子性胺基矽化合 物、陽離子性纖維素衍生物、陽離子性澱粉、成季鹼之聚 · 乙二醇胺縮合物、成季鹼之膠原蛋白多肽、陽離子性甲殼 * 素衍生物、陽離子性瓜爾豆膠、膠體諸如陽離子性三聚氰 胺-甲醛酸膠體、無機之經處理之矽石膠體、聚醯胺-表氯醇 樹脂、陽離子性丙晞醯胺、其等之聚合物及共聚物、其等 83162 -15- 1284055 之組合、及其類似物。對於此種應用,有用之帶電荷之分 子可係具有單一之帶電荷單位、並具有連結於至少一部份 之該微多孔性結構之能力之小分子。陽離子性材料較佳地 具有一種或多種與其缔合之相對離子,此等相對離子,當 曝露於生物活性之金屬鹽溶液時,造成於陽離子性表面鄰 近中之金屬之優先之沉澱作用,以生成陽離子性金屬沉搬 錯合物。 胺之典型可係吡咯、表氯醇衍生之胺、其聚合物、及其 類似物。醯胺之典型可係於國際專利申請案世界智慧財產 權組織專利(WO)第01/07090號中揭示之聚醯胺類、及其類 似物。第四級銨鹽之典型可係函化二晞丙基二甲基銨之同 元聚合物、表氯醇衍生之多元第四級胺聚合物、自二胺與 二鹵化物衍生之第四級銨鹽諸如於美國專利第2,261,〇〇2 號、第2,271,378號、第 2,388,614 號、及第 2,454,547號(所有 之此等專利係以提及之方式併入)及於國際專利申請案世 界智慧財產權組織專利第97/23 594號(亦係以提及之方式併 入)中揭示者、聚溴化六亞甲基二甲基銨、及其類似物。陽 離子性材料可係化學地鍵結、吸附、或交聯於本身及/或於 活性粒子。 此外,適合於作為陽離子性材料使用之其他材料包括自 BioShield Technologies,Inc·,Norcross,Georgia可獲得之 BIOSHIELD®。BIOSHIELD®係包含以重量計約5%氯化十八 基胺基二甲基三甲氧基矽烷基丙基銨、及少於3%氯丙基三 甲氧基矽烷之有機矽烷產品。可使用之另一種材料係自 83162 -16- 1284055
Surfacine Development Company LLC, Tyngsboro, Massachusetts 可獲得之SURFACINE®。SURFACINE®包含經由以4,4,-亞甲 基-雙-N,N-二縮水甘油基苯胺(MBGDA)(—種交聯劑)反應 聚(六亞甲基縮二胍)(PHMB),以將PHMB共價地鍵結於聚 合物之表面而獲得之三度空間聚合之網狀結構。銀,於碘 化銀之形式,係引進入該網狀結構中,及係如次微米尺寸 之粒子陷於其中。該組合係有效之殺生物劑,其可係使用 於本發明中。視活性粒子而定,MBGDA可將或可不將PHMB 交聯於微多孔性結構。 將陽離子性材料曝露於生物活性之金屬鹽溶液中,以使 金屬錯合物沉澱於至少部份之活性粒子之至少一部份之表 面上。用於此種目地,生物活性之金屬係較佳的。此等生 物活性之金屬包括,但不限於,銀、銅、鋅、鎬、汞、錄、 金、链、銘、免、及其等之組合。最佳之生物活性之金屬 係銀及銅。較佳地選擇生物活性之金屬鹽溶液,以使該金 屬與該陽離子性材料之相對離子實質上係不溶於水性環境 中,以驅動金屬錯合物之沉澱作用。較佳地,金屬係以總 組合物之以重量計約0.01%至約2.0%之數量存在。 一種特別有用之微生物攔截增進劑係銀-胺-南化物錯合 物。該陽離子性胺較佳係具有約400,000道耳呑之分子量之 鹵化二烯丙基二甲基铵之同元聚合物、或具有相似之電荷 密度及分子量之其他第四級铵鹽之同元聚合物。於本發明 中有用之氣化二烯丙基二甲基銨之一種同元聚合物係自 Naperville,Illinois之 Nalco Chemical Company,以商品名稱 83162 -17- 1284055 MERQUAT⑧,1 〇〇市售的。該氯化物相對離子可係以溴化物 或琪化物相對離子替代。當與硝酸銀溶液接觸時,銀_胺_ 鹵化物錯合物於該微生物攔截增進之過濾介質之微多孔性 結構之至少一部份之活性粒子上沉殿。 於活性粒子包含活性碳之情況下,陽離子性材料較佳地 具有高電荷密度及足夠高之分子量,以對於活性碳之帶負 電荷之表面基產生強之吸引及高之配位能。而且,於生物 活性之金屬之膠體之存在下,使用活性碳之帶電荷之表面 之增進之攔截係由活性碳之疏水性吸附作用機構補充。此 種疏水性機構對於由NOM之垢積之效應通常係抵抗的,及 於南離子強度之條件下實質上係較有效的。碳表面之未經 處理之部份,由於彼等之富含氧之化學,趨於具有負電荷, 其可繼續吸附帶正電荷之粒子。對於小粒子之航行,帶正 電荷、帶負電荷、及疏水性表面之組合呈現出幾乎不能超 越之障礙。於以微生物攔截增進劑處理碳之後,生物活性 之金屬及其之缔合之相對離子於活性粒子上之存在可係使 用X射線螢光而偵測。 製造微生物攔截增進之過濾介質之方法 本發明之微生物攔截增進之過濾介質可係根據熟諳此技 藝者已知之方法製造。此等方法包括擠製、模製、滑移洗 ~、於底材上固定活性粒子、及其類似方法。示範之方法 係於美國專利第5,〇19,311號、及第5,792,513號中揭示。 活性粒子係使用熟諳此技藝者已知之方法諸如,例如, 喷射塗佈,而以陽離子性材料處理。較佳地,活性粒子係 83162 -18- 1284055 以微生物攔截增進之過濾介質之總重量之以重量計約05% 至約3%,及更佳係以重量計約1%,塗佈。一旦陽離子性材 係塗佈於至少一部份之活性粒子上之後,將該等粒子曝露 於生物活性之金屬鹽。該金屬鹽之溶液滲透入該等粒子 中,以造成生物活性之金屬於活性粒子之至少一部份之表 面上之沉濺。由於與陽離子性塗層缔合之相對離子與塗伟 之金屬鹽反應以生成膠體粒子,因此該沉澱方法將大部分 之金屬膠體精確地沉積於直接鄰接此種陽離子性塗層。金 屬鹽可係噴射於經處理之粒子上或使用熟諳此技藝者已知 之方法而以其他方式塗佈。%離子性材料及金屬鹽之溶液 較佳係以幾乎不含離子之水製造,以使與陽離子性材料缔 合之相對離子係緊密地吸引至經處理之活性粒子之陽離子 性表面上、及消除不受歡迎之離子,該等離子可造成該生 物活性之金屬進入遠離該陽離子性表面之位置中之不受控 制之沉澱作用。 然後過里之水分係自該等粒子移除,通常以加熱或於真 空下,至需要之水分含量。較佳地,倘若該等粒子其後係 使用熱塑性黏合劑而擠製或模製,則水分含量應係小於約 10%,及更佳係小於約5%。 一旦微生物攔截增進劑係塗佈於至少一部份之活性粒子 上之後’將活性粒子研磨至需要之尺寸及與黏合劑材料潛 在地混合’以於將活性粒子固定成為具有需要之微多孔性 結構之期望之最後形式之前,形成均句之混合物。選擇黏 合劑,以使該黏合劑材料之熔點係比活性粒子之熔點充分 83162 -19- 1284055 地較低,以使可加熱該微生物攔截增進之過濾介質以活化 ,黏合劑材料,而同時該微多孔性結構不熔解及因而損失 多孔性。黏合劑粒子較佳係充分均勻地分布於整個活性粒 子中以使後者,於轉化成微多孔性結構之後,該黏合劑粒 子將陷入或結合於實質上所有之活性粒子。 於本發明中,於將活性粒子聚結成為微多孔性結構中有 用之黏合劑材料潛在地可包括於此技藝中已知於纖維、粉 末或粒子形式之任何熱塑性或熱固性材料。有用之黏合劑 材料可包括材料諸如,但不限於,聚晞烴、聚南乙烯、聚 乙埽基酯、聚乙婦基醚、聚硫酸乙缔基酯、聚磷酸乙缔基 酯、聚乙婦基胺、聚醯胺、聚醯亞胺、聚氧基二唑、聚三 唑、聚羰二亞胺、聚砜、聚碳酸酯、聚醚、聚伸芳基氧化 物、聚酯、聚芳酯(p〇lyarylates)、酚-甲醛樹脂、三聚氰胺· 甲醛樹脂、甲醛-尿素樹脂、乙晞_乙酸乙缔酯共聚物、其等 之共聚物及欲段互聚物(block interp〇lymers)、及其等之組 a。以上材料之變異之形式及其他有用之聚合物包括基(諸 如羥基、齒素、低碳烷基、低碳烷氧基、單環芳基、及其 類似物)之取代作用。 於本發明中可係有用之黏合劑之較詳細之表列包括末端 -封閉之聚縮醛,諸如聚(氧基亞甲基)或聚甲醛、聚(三氯乙 醛)、聚(正戊醛)、聚(乙醛)、及聚(丙醛);丙缔酸聚合物, 諸如聚丙烯醯胺、聚(丙晞酸)、聚(甲基丙烯酸)、聚(丙缔 酸乙酯)、及聚(甲基丙晞酸甲酯);氟碳聚合物,諸如聚(四 氟乙烯)、全氟化之乙晞-丙烯共聚物、乙晞_四氟乙婦共聚 83162 -20- 1284055 物、聚(氯三·氟乙缔)、乙烯-氯三氟乙烯共聚物、聚(二氟亞 乙烯)、及聚(氟乙烯);聚醯胺,諸如聚(6-胺基己酸)或聚(ε-己内醯胺)、聚(六亞甲基己二醯胺)、聚(六亞甲基癸二醢 胺)、及聚(11-胺基十一酸);芳香族聚醯胺’諸如聚(亞胺 基-1,3-伸苯基亞胺基異酞醯基)或聚(間-伸苯基異s太驢 胺);二苯并蒽,諸如聚-2-苯二甲基、及聚(氯—苯二甲基); 聚芳基醚,諸如聚(氧基-2,6-二甲基-1,4-伸苯基)或聚對苯 醚(poly(p-phenyleneoxide));聚芳基戚’諸如聚(氧基-1,4· 伸苯基颯基-1,4-伸苯基氧基-ΐ,4-伸苯基異亞丙基-1,4-伸苯 基)、及聚(颯基-1,4-伸苯基-氧基-1,4-伸苯基颯基4,4’-亞聯 苯基);聚碳酸酯,諸如聚(丙二酚)或聚(羰基二氧基-1,4- 伸苯基異亞丙基-1,4_伸苯基);聚酯,諸如聚(對献酸乙二 酯)、聚(對i太酸丁二酯)、及聚(對酞酸環伸己基_1,4_二亞甲 基酿)或1(乳基亞甲基_1,4_環伸己基亞甲基氧基對g太酿 基);聚芳基硫化物,諸如聚對苯硫醚(p〇ly(p-phenylene sulfide))或聚(硫基-1,4-伸苯基);聚醯亞胺,諸如聚(1,2,4,5_ 私四甲酸醯亞胺-1,4-伸苯基);聚晞烴,諸如聚乙晞、聚丙 烯、聚(1-丁晞)、聚(2-丁烯)、聚(1-戊晞)、聚(2_戊晞)、聚 (3-甲小戊晞)、及聚(4-甲小戊烯);乙烯基聚合物,諸如聚 (乙酸乙烯酯)、聚(二氯亞乙埽)、及聚(氯乙缔);二烯聚合 物,諸如U2·聚-i,3丁二晞、i终π 丁二烯、聚異戊二 烯、及聚氯丁二烯;聚苯乙烯·芬a^ # 邱,及則述又共聚物,諸如丙 烯腈-丁二烯-苯乙烯(ABS)共聚铷士 、物可係有用之聚烯烴包括 聚乙晞、線性低密度聚乙烯、帘^ ^ ^ 聚丙烯、聚(1·丁晞)、聚(2_ 83162 •21· 1284055 丁埽)、聚(1-戊缔)、聚(2-戊缔)、聚(3-甲-1-戊晞)、聚(4-甲-1_戊烯)、及其類似物。 其他潛在地可應用之材料包括聚合物諸如聚苯乙烯及丙 缔腈-苯乙晞共聚物、苯乙埽-丁二缔共聚物、及其他非結晶 或非晶形聚合物及結構。 較佳之黏合劑材料包括聚乙烯、聚(乙缔-乙酸乙缔酯)、 及尼龍。作為黏合劑之特別較佳者係自Equistar Chemicals, L.P·,Tuscola,Illinois,以商品名稱MICR〇THENE®F市售之 等級FN 5 10微細之聚乙晞。 黏合劑可具有約0·1微米至約250微米,較佳係約i微米至 約100微米,及更佳係約5微米至約20微米,之平均粒子尺 寸。黏合劑材料具有比活性粒子之軟化點重大地較低之軟 化點,以使可加熱微生物攔截增進之過濾介質以活化該黏 合劑材料,而同時微多孔性結構不熔解及因而損失多孔 性,係較佳的。 使用之黏合劑材料之數量係視該微多孔性結構如何經由 擠製、模製、或其他方法生成而定。例如,當活性粒子係 擠製或模製成為固體複合物團塊時,黏合劑材料較佳係以 微生物攔截增進之過滤介質之以重量計約丨5%至約Μ%之 數里存在’及更佳係以重量計約17%至約19%。當活性粒子 係於底材(諸如,例如,非織物材料)上固定時,黏合劑材料 較佳係於總組合物之以重量計約5。/。至約2〇%之數量存在, 及較佳係約9%至約15〇/〇。 於粒子、纖維、鬚晶、或粉末形式之一種或多種添加劑 83162 -22- 1284055 亦可係與活性粒子混合,以於微多孔性結構之生成及微生 物污染物之攔截中協助其他污染物或粒子之吸附或吸收。 有用之添加劑可包括,但不限於,金屬粒子、活性銘氧、 活性碳、矽石、聚合之粉末及纖維、玻璃珠粒或纖維、纖 維素纖維、離子交換樹脂、工程樹脂、陶磁、滞石、碎藻 土、活性鋁土礦、漂白土、硫酸鈣、其他吸附劑或吸收劑 材料、或其等之組合。視特定之應用而定,亦可化學地處 理添加劑以提供微生物搁截能力。此等添加劑較佳地係以 足夠之數量存在,以使當生成之微生物攔截增進之過濾媒 介係使用於過濾應用中時,於該生成之微生物攔截增進之 過濾介質中之流體流動實質上不受阻礙。添加劑之數量係 視過濾系統之特定用途而定。 或者’最後之微多孔性結構可係經由將粒子或纖維或此 等混合物滑移澆鑄或濕成型及其後致使黏合劑或粒子燒結 該等成分一起而生成。於某些案例中,粒子可形成彼等之 本身之黏合劑,如於雙組份纖維或低熔點樹脂中。於某些 案例中,黏合劑可係水溶性或可交聯之樹脂或鹽,當容許 其等乾燥、或加熱其等、或容許其等反應時,生成需要之 鍵結。亦可使用化學黏合劑、以及沉澱之黏合劑,諸如某 些磷酸鹽。 利用微生物攔截増進之過濾介質之過濾系統 本發明之微生物攔截增進之過濾介質可係容易地組合入 先岫技藝過濾系統中,此等系統利用固定之粒子過濾介質 如固體複合物團塊、平直、螺旋或摺疊之片版、巨大之結 83162 -23- 1284055 構、或蟻燭形物。較佳地,置於自微生物攔截增進之過滤 介質之上游之粒子預濾器係與微生物攔截增進之過滤介質 共同使用,以於流入液接觸該微生物攔截增進之過滤介質 之前,自該流入液移除儘可能多之粒子污染物。 【實施方式】 實例 下列之實例係提供以舉例說明本發明及不應解釋為限制 本發明之範圍。 多孔性研究係以自 Porous Materials,Inc.,Ithaca,New
York可獲得之自動化毛細管流動多孔計進行。使用由設備 製造商發表之標準程序而測定之參數包括平均流動細孔尺 寸及氣體(空氣)穿透性。空氣之流動係於可變之壓力,對於 乾及濕微生物攔截增進之過濾介質檢定。 微生物攔截增進之過攄介質之細菌激發係使用美國菌種 中心(ATCC)第11775號之大腸桿菌之懸浮液以評估對於細 菌激發之回應而進行。對於病毒激發之回應係使用美國菌 種中心第15597-Bi號之MS2噬菌體而評估。試驗之其他微生 物包括美國菌種中心第4335號之缺陷短波單胞菌 ⑽似Am/⑽仏)、美國菌種中心第9375號之枯草 芽孢桿菌(亦以BG知曉)。使用美國菌種中心之標準操作程 序以用於細菌及噬菌體之繁殖,及使用標準微生物程序, 如於此技藝中熟知,以用於製備及量化於以該等微生物之 懸浮液激發之過濾器之流入液及流出液中之微生物。 個別之過濾器係一式兩份地以每種微生物於改良版本之 83162 -24- 1284055 美國國家衛生基金會(NSF)國際標準53胞囊降低試驗方案 (protocol)之下試驗。此方案係設計以評估過濾器於加速曝 露於微細粒子之期間之功能,以模擬污穢之積聚。過滤器 係以逆滲透/去離子(RO/DI)水沖洗及校正至〇.5至1·〇加命/ 分鍾(gpm)之最初流率。過濾介質之平均流動路徑皆係約ο” 微米至1.1微米。 於試驗之期間’最初之樣本係於試車系統沖洗期間内自 流入液及流出液取樣口抽出,以確保不具有來自未適當地 消毒之試驗裝置之背景干擾。然後以微生物之懸浮液激發 過;慮器’樣本係於最少2升激發溶液之後採取,以確保於取 樣之前,激發水通過整個試驗裝置之流動。 將所有之流入液及流出液樣本如需要地連續稀釋、及以 一式三份地舖於平板上培養。於某些案例中,特定設計之 碳團塊係以數種流率試驗,以確定彼等對於改變之流率之 回應。 具有增進之微生物攔截能力之活性碳團塊過濾器係製備 =下。將20磅之12x40篩目經酸洗滌之以煙煤為基礎之活性 奴,自 Calgon Carbon Company獲得,與3% MERquat® 1〇〇 於去離子水中之溶液緩和地混合,以完整地塗佈碳粒子及 確保MERQUAT® 1GG已吸附於至少_部分之竣粒子上。其 後,將硝酸銀之溶液(70克結晶硝酸銀於1〇升去離子水中) 加入該經贿QUAT1理之碳中,以容許銀以氯化銀膠體 〈形式於碳粒子之至少-部分之表面上之沉澱作用。將铖 處理之碳粒子於⑽乾燥,直到於碳粒子中僅具有低於 83162 -25- 1284055 5 /〇水伤存在為止。乾燥時間於約3至約$小時之間變動。將 乾燥之碳於一雙輥粉碎機中研磨至8〇χ325篩目尺寸,具有-以重量汁約14%之-325篩目盤中剩餘物,及將其與於以重量 計約17%之FN510 (低密度聚乙缔黏合劑材料)混合。於適合 之熱、壓力及溫度條件下,擠製該混合物,如於美國專利 第5,019,3 11號中敘述。使用生成之各種尺寸之碳團塊過濾- 器,以經由使用熱熔樹脂施加末端蓋板而建造水過滤系 · 統,如於此技藝中熟知。 ~ 蔹等過濾器係於最初清潔條件下、然後於污穢積聚後之 _ 間隔檢定微生物欄截功能,於此等間隔,與於原來、清潔 過漉器上測量之流率比較,流率係以25%、50%及75%減少。 為了達成於流率中之需要之降低,利用“名目,,試驗灰塵 激發水。名目試驗灰塵係具有約〇至5·〇微米直徑、及具有 以重量計96%之粒子於此範圍内及2〇%至40%之該等粒子 大於2.5微米之矽酸鹽粉末。當已完成需要之流率降低之 後’減縮名目試驗灰塵激發及以4·0升之逆滲透/去離子 (RO/DI)水沖洗過濾器,以自進入液及流出液管線中移除任 魯 何殘餘之試驗灰塵。然後以微生物之懸浮液激發過滤器, 如以上敘述。 本發明之微生物攔截增進之過濾介質之功效係於以下之 表I及II中表示。 、 83162 -26- 1284055 表i 微生物攔截增進之活性碳團塊過濾介質之LRV 實例 號碼 過濾器尺寸 外徑x内徑x長度 (吋) 流率 (gpm) 缺陷短波 單胞菌(B. diminuta) (LRV) 大腸桿菌 (LRV) 枯草芽孢 桿菌 (LRV) MS2 (LRV) 1 1.85x0.375x2.94 0.50 3.82 2 1.375x0.375x4.735 0.25 8.20 4.83 3 1.85x0.50x2.94 0.75 2.15 4 2.00x0.75x2.55 0.75 4.92 5 2.25x1.00x4.00 0.50 8.49 8.88 8.97 8.35 6 2.40x1.19x9.628 1.0 5.79 7 1.50x0.375x6.055 0.50 8.80 5.31 8 1.50x0.375x6.055 0.60 3.51 9 1.50x0.375x6.055 0.75 8.79 3.16 10 2.00x0.50x5.82 0.50 9.45 9.45 9.46 9.27 83162 27- 1284055
表π 微生物攔截增進之活性碳團塊過濾介質 於最初及減少之流率之LRV 實例 號碼 最初流率 (gpm) 過濾器尺寸 外徑X内徑X長度 (吋) 流率減少 大腸桿菌 (LRV) MS2 (LRV) 11 0.50 2.50x1.25x7.236 0% 8.39 5.14 25% 8.46 5.73 50% 8.48 5.26 75% 8.61 6.99 12 0.50 1.50x0.375x6.055 0% 5.31 25% 50% 7.03 75% 8.17 13 0.60 1.50x0.375x6.055 0% 3.52 25% 4.88 50% 4.89 75% 5.71 14 0.75 1.50x0.375x6.055 0% 8.79 3.16 25% 8.79 4.27 50% 8.76 4.08 75% 8.74 4.86 15 0.50 2.25x1.00x4.00 0% 8.88 8.35 25% 8.88 9.50 50% 8.87 8.34 75% 8.91 8.22 16 0.50 2.00x0.50x5.82 0% 9.45 9.27 25% 9.41 9.25 50% 9.48 9.25 75% 9.44 9.25 本發明之微生物攔截增進之活性碳團塊過濾介質提供較 83162 -28- 1284055 大生物諸如缺陷短波單胞菌(及大腸桿菌及枯草 芽孢桿菌之大於8對數減少。事實上,於所有案例中此等生 物之攔截係為試驗方案之敏感度所不能及。滲透之結 果顯示’於壁厚度與攔截之水準之間無明顯之關係。此表 示對於MS2攔截,傳統之機械攔截機構不是可依賴的。然 而,於對數攔截與過濾器之空床接觸時間(EBCT)i間具有 直接之關係。圖1顯示於最初、清潔過濾器對數減少與 過濾器之EBCT之間之實質上線性之關係,表示具有約6秒 鐘EBCT之需要之擴散攔截機構,俾能於具有約〇·9至約u 微米之平均流動路徑之微生物攔截增進之過濾介質中達成 此種噬菌體之有效之減少。為了此理由,於較低之流率操 作之較大(過濾器比於提高之流率操作之小過濾器較有效 地執行。 雖然本發明係已連同-種特定之較佳具體實施例特定地 敘述,但是由於先前之說明,因此多種之可選擇方案、修 飾及改變對於熟諳此技藝者將係明顯的,此係顯然的。因 此希望’附隨之中請專利範圍將包含任何之此等可選擇方 案、修飾及改變’如於本發明之真實之範圍及精神之内。 【圖式簡單說明】 咸信本發明之特性係新顆的,及本發明之元件特性係於 附隨之中請專利範圍中特定地紀載。圖係僅驗舉例說明 目的及不是按照比例騎。然而’本發明本身,關於組織 及操作之万法,皆可係經由參考隨後連同附隨之圖式選澤 之-種或多種較佳具體實施例之說明而最佳地了解,於附 83162 -29- 1284055 隨之圖式中、 圖1係描繪本發明之微生物攔截增進之活性碳過濾介質 之空床接觸時間相對於MS2噬菌體之對數減少值之線圖。 83162 30-
Claims (1)
- 工284够备102104號專利申請案 皮私月分曰修(更)正替換頁j 中文申請專利範圍替換本(96年2月) 拾、申請專利範圍: 1· 一種過滤介質,其包含: 包含活性粒子之排列之微多孔性結構,該微多孔性結 構具有小於約2微米之平均流動路徑;及 微生物攔截增進劑,該微生物攔截增進劑包含吸附於 至少一部分之該微多孔性結構上之具有中等至高之電荷 密度及大於約5,000道耳呑之分子量之陽離子性材料 於直接鄰近於該陽離子性材料並亦於至少一部分之該微 夕孔性結構上之生物活性之金屬。 2. 4. 根據申請專利範圍第i項之過濾介質,其中 由活性碳™、衫、料土、州、= 鹽、鈦酸鹽、骨炭、氫氧磷灰石弼、鎂氧化物、鐵氧化 物、鎂氧、珍珠岩、滑石、聚合之粒子、黏土、經誠化 (樹脂、離子交換樹脂、陶磁、或其等之組合 進一步包含黏合劑。 很爆T請寻利範圍第1項之過濾介質,其中該微 構具有小於或等於約!微米之平均;虎動路徑。 根據申請專利範圍第丨項之過濾媒介 \ 增進劑係經由以具有㈣卜之相料广起物搠 撼走 ^.......香w又相對離子之陽離子性 =理至少-部份之該微孔性結構、接著生物活性之 人至少-邵份之與該陽離子性材料缔合 沉澱作用而生成。 ㈢野離子 5. 根據申請專利範圍第4項之過濾介質, 料包含具有大於或等於約4〇〇,〇〇〇遒耳 其中該陽離子性材 呑之分子量之氯化 83162-9602l3.doc 1284055 一埽丙基二甲基銨之同元聚合物。 6·根據申請專利範圍第1項之過濾介質,其中該微多孔性結 構包含活性粒子之固體複合物團塊、或固定之活性粒子 之平直片板結構。 7·根據申請專利範圍第1項之過濾介質,其中該微多孔性結 構係經由該等活性粒子之擠製、模製、滑移洗鑄、粉末 塗佈、濕成型或乾成型而生成。 8·根據申請專利範圍第i項之過濾介質,其中當流入液具有 /、為過滤介質接觸歷時少於約12秒鐘之空床接觸時間 時,泫過濾介質提供於該流入液中之微生物污染物之大 表Ή對數去除率(6 log reduction)。 9· 一種過濾系統,其包含: 具有一入口及一出口之殼; 位於該殼之内於與該等入口及出口流體相通之過濾介 質,該過濾介質包含: 产具有小於約2微米之平均流動路徑包含活性碳、活性 氧弗石碎义土、碎酸鹽、銘碎酸鹽、敛酸鹽、骨 ,、氫氧磷灰石_、鎂氧化物、鐵氧化物、凝氧、珍珠 岩、滑石、聚合之粒子、黏土、經琪化之樹脂、離子交 換樹脂、陶磁、或其等之組合之活性粒子之微多孔性妹 構;及 ^ 古、物攔截增進劑,該微生物攔截增進劑包含具有 南(電荷密度、大於約5,_道耳吞之分子量及具有與其 、’帝合之相對離子之陽離子性材料,該陽離子性材料吸附 83162-960213.doc 1284055 於至部分之該微多孔性結構上,及其中使生物活性 之金屬與至少一部分之與該陽離子性材料缔合之 子沉澱, 其中流動通過該殼及接觸該過濾介質之微生物污染之流 入液具有於自該殼流動離開之流出液中之微生物污染: 之至少約4對數減少。 ίο. 11. 12. 13. 根據申請專利_第9項之過m其中該微多孔性妹 構之活性粒子係固體複合物團塊、或固定之活性粒^ 平直片板結構。 根據申請專利範ϋ第9項之㈣系統,其中該微多孔性結 構之活性粒子係滑移澆鑄、濕-成型或乾-成型的。 種製k具有增進之微生物攔截能力之過遽介質之方 法,其包含下列步驟: 提供具有約0.1微米至約5,000微米之平均粒子尺寸之 活性粒子; 以微生物攔截增進劑處理該等活性粒子,該微生物攔 截增進劑包含具有高之電荷密度及大於約5,000道耳吞之 分子量足陽離子性材料、及生物活性之金屬;及 將孩等經處理之活性粒子成型為具有小於約2微米之 平均流動路徑之微多孔性結構。 一種製造具有増進之微生物攔截能力之過濾介質之方 法,其包含下列步騾: &供具有約0·1微米至約5,000微米之平均粒子尺寸之 活性粒子; 83162-960213 .doc 1284055 將該等活性粒子聚結成為具有小於約2微米之平均流 動路控之微多孔性結構;及 14. 15. 16. 17. 以铽生物攔截增進劑處理該微多孔性結構,該微生物 攔#^進劑包含具有高之電荷密度及大㈣、咖道耳呑 之分子量之陽離子性材料、及生物活性之金屬。 根據申請專利範圍第12或13項之—項之方法,其中該提 供活性粒子之步驟包含提供活性碳、活性銘氧、滞石、 碎藻土、料鹽、㈣酸鹽、骨炭、氫氧磷灰石舞、鐵 氧化物、鎂氧、珍珠岩、滑石、聚合之粒子、黏土、或 其等之組合之活性粒子,及進一步包含添加黏合劑之步 驟。 根據申請專利範圍第12或13項之一項之方法,其中該處 理之步驟包含下列之步驟: 以具有與其缔合之相對離子之陽離子性材料塗佈至少 —部份之該微多孔性結構或活性粒子;及 糸至4伤之1^微多孔性結構或活性粒子上致使生 物活性 < 金屬與至少一部分之與該陽離子性材料缔合之 相對離子之沉搬作用。 根據申請專利範圍第12或13項之一項之方法,其中於該 處理之步驟中,該陽離子性材料係自胺、第四級銨鹽、 苯二甲烴銨化合物(benzalk〇nium compounds)、縮二胍、 胺基矽化合物、其等之聚合物、及其等之組合組成之族 群中選出。 根據申請專利範圍第12或13項之一項之方法,其中於該 83162-9602l3.doc 1284055處理之步驟中,該生物活性之金屬係自銀、銅、鋅、鎮、 汞、銻、金、鋁、鉑、鈀、及其等之組合組成之族群中 選出。 18. 19 20. 根據申請專利範圍第12或13項之一項之方法,其中該成 型或聚結該等活性粒子成為該微多孔性結構之步驟包含 k 擠製、滑移澆鑄、或固定該等活性粒子成為平直之片板 · 結構。 一種自流體中移除微生物污染物之方法,其包含下列步 驟: 提供包含下列之過濾介質 械多孔性結構’該微多孔性結構包含活性粒子及具 有小於約2微米之平均流動路徑;及 於至少一部分之該微孔性結構上吸附之微生物攔截 增進劑,該微生物攔截增進劑包含具有中等至高之電荷 密度及大於約5,000道耳呑之分子量之陽離子性材料、及 生物活性之金屬; 將受微生物污染之流體接觸該過濾介質歷時小於 m 等於約12秒鐘之時間期間;及 獲得具有微生物污染物之大於約4對數去除率之流 出液。 b 根據申請專利範圍第19項之方法,其中於該提供過濟介· 質之步驟中’該微多孔性結構包含活性粒子,該 . 子包含活性碳。 83162-960213.doc
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| KR (1) | KR100917075B1 (zh) |
| CN (1) | CN1232333C (zh) |
| AT (1) | ATE390389T1 (zh) |
| AU (1) | AU2003202859B2 (zh) |
| BR (1) | BR0302962B1 (zh) |
| CA (1) | CA2444808C (zh) |
| DE (1) | DE60319952D1 (zh) |
| IL (1) | IL158362A (zh) |
| MX (1) | MXPA03010212A (zh) |
| TW (1) | TWI284055B (zh) |
| WO (1) | WO2003064330A1 (zh) |
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-
2002
- 2002-11-08 US US10/290,803 patent/US6630016B2/en not_active Expired - Lifetime
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2003
- 2003-01-02 AU AU2003202859A patent/AU2003202859B2/en not_active Expired - Fee Related
- 2003-01-02 JP JP2003563962A patent/JP2005515892A/ja active Pending
- 2003-01-02 AT AT03701971T patent/ATE390389T1/de not_active IP Right Cessation
- 2003-01-02 WO PCT/US2003/000065 patent/WO2003064330A1/en not_active Ceased
- 2003-01-02 MX MXPA03010212A patent/MXPA03010212A/es active IP Right Grant
- 2003-01-02 EP EP03701971A patent/EP1470083B1/en not_active Expired - Lifetime
- 2003-01-02 BR BRPI0302962-0A patent/BR0302962B1/pt not_active IP Right Cessation
- 2003-01-02 DE DE60319952T patent/DE60319952D1/de not_active Expired - Lifetime
- 2003-01-02 KR KR1020037012725A patent/KR100917075B1/ko not_active Expired - Lifetime
- 2003-01-02 CN CNB03800271XA patent/CN1232333C/zh not_active Expired - Lifetime
- 2003-01-02 IL IL158362A patent/IL158362A/en active IP Right Grant
- 2003-01-02 CA CA002444808A patent/CA2444808C/en not_active Expired - Lifetime
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Also Published As
| Publication number | Publication date |
|---|---|
| CN1232333C (zh) | 2005-12-21 |
| BR0302962A (pt) | 2004-07-06 |
| US20030140785A1 (en) | 2003-07-31 |
| CA2444808A1 (en) | 2003-08-07 |
| AU2003202859B2 (en) | 2008-01-31 |
| KR20040089440A (ko) | 2004-10-21 |
| JP2010279945A (ja) | 2010-12-16 |
| HK1065303A1 (zh) | 2005-02-18 |
| BR0302962B1 (pt) | 2012-11-27 |
| TW200400077A (en) | 2004-01-01 |
| JP2005515892A (ja) | 2005-06-02 |
| MXPA03010212A (es) | 2004-03-10 |
| DE60319952D1 (de) | 2008-05-08 |
| CN1509257A (zh) | 2004-06-30 |
| KR100917075B1 (ko) | 2009-09-15 |
| JP5244867B2 (ja) | 2013-07-24 |
| WO2003064330A1 (en) | 2003-08-07 |
| EP1470083A4 (en) | 2005-11-02 |
| IL158362A (en) | 2007-09-20 |
| CA2444808C (en) | 2009-12-22 |
| EP1470083A1 (en) | 2004-10-27 |
| IL158362A0 (en) | 2004-05-12 |
| ATE390389T1 (de) | 2008-04-15 |
| US6630016B2 (en) | 2003-10-07 |
| EP1470083B1 (en) | 2008-03-26 |
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