TW201226416A - Phosphorus-containing diol monomer and flame retardant polyester copolymer thereof - Google Patents
Phosphorus-containing diol monomer and flame retardant polyester copolymer thereof Download PDFInfo
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- TW201226416A TW201226416A TW99146962A TW99146962A TW201226416A TW 201226416 A TW201226416 A TW 201226416A TW 99146962 A TW99146962 A TW 99146962A TW 99146962 A TW99146962 A TW 99146962A TW 201226416 A TW201226416 A TW 201226416A
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- phosphorus
- polyester copolymer
- flame retardant
- diol monomer
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- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 63
- 239000011574 phosphorus Substances 0.000 title claims abstract description 61
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 58
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 title claims abstract description 49
- 239000003063 flame retardant Substances 0.000 title claims abstract description 49
- 229920000728 polyester Polymers 0.000 title claims abstract description 31
- 239000000178 monomer Substances 0.000 title claims abstract description 24
- 150000002009 diols Chemical class 0.000 title claims abstract description 19
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 11
- 239000003054 catalyst Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 238000012360 testing method Methods 0.000 claims description 9
- 229920001577 copolymer Polymers 0.000 claims description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 239000001257 hydrogen Substances 0.000 claims description 6
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 5
- 125000004429 atom Chemical group 0.000 claims description 4
- 125000000008 (C1-C10) alkyl group Chemical group 0.000 claims description 3
- 125000005843 halogen group Chemical group 0.000 claims description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 2
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 2
- 125000003983 fluorenyl group Chemical group C1(=CC=CC=2C3=CC=CC=C3CC12)* 0.000 claims 3
- 125000000217 alkyl group Chemical group 0.000 claims 2
- AIYUHDOJVYHVIT-UHFFFAOYSA-M caesium chloride Chemical compound [Cl-].[Cs+] AIYUHDOJVYHVIT-UHFFFAOYSA-M 0.000 claims 2
- 238000004519 manufacturing process Methods 0.000 claims 1
- 229910000029 sodium carbonate Inorganic materials 0.000 claims 1
- 150000002148 esters Chemical class 0.000 abstract description 2
- 238000006116 polymerization reaction Methods 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 description 16
- 238000003786 synthesis reaction Methods 0.000 description 16
- 229920000642 polymer Polymers 0.000 description 13
- 239000000047 product Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 8
- 238000006068 polycondensation reaction Methods 0.000 description 8
- 230000009477 glass transition Effects 0.000 description 7
- 229940011182 cobalt acetate Drugs 0.000 description 5
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- -1 phosphorus compound Chemical class 0.000 description 5
- 239000000470 constituent Substances 0.000 description 4
- 239000004744 fabric Substances 0.000 description 4
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 4
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- BQGYHQOWXOZWOJ-UHFFFAOYSA-N n-butyl-n-(2-hydroxyethyl)nitrous amide Chemical compound CCCCN(N=O)CCO BQGYHQOWXOZWOJ-UHFFFAOYSA-N 0.000 description 3
- 125000006376 (C3-C10) cycloalkyl group Chemical group 0.000 description 2
- QPKOBORKPHRBPS-UHFFFAOYSA-N bis(2-hydroxyethyl) terephthalate Chemical compound OCCOC(=O)C1=CC=C(C(=O)OCCO)C=C1 QPKOBORKPHRBPS-UHFFFAOYSA-N 0.000 description 2
- XSIFPSYPOVKYCO-UHFFFAOYSA-N butyl benzoate Chemical compound CCCCOC(=O)C1=CC=CC=C1 XSIFPSYPOVKYCO-UHFFFAOYSA-N 0.000 description 2
- 125000004437 phosphorous atom Chemical group 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000000425 proton nuclear magnetic resonance spectrum Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- 239000012209 synthetic fiber Substances 0.000 description 2
- 229920002994 synthetic fiber Polymers 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- VOFOZYPOSUYPPG-UHFFFAOYSA-N 2,3-bis(2-hydroxyethyl)naphthalene-1-carboxylic acid Chemical compound C1=CC=C2C(C(O)=O)=C(CCO)C(CCO)=CC2=C1 VOFOZYPOSUYPPG-UHFFFAOYSA-N 0.000 description 1
- OTSSKELQKOKVFV-UHFFFAOYSA-N 2-hydroxyethyl naphthalene-1-carboxylate Chemical compound C1=CC=C2C(C(=O)OCCO)=CC=CC2=C1 OTSSKELQKOKVFV-UHFFFAOYSA-N 0.000 description 1
- XNCOSPRUTUOJCJ-UHFFFAOYSA-N Biguanide Chemical compound NC(N)=NC(N)=N XNCOSPRUTUOJCJ-UHFFFAOYSA-N 0.000 description 1
- 229940123208 Biguanide Drugs 0.000 description 1
- 229930185605 Bisphenol Natural products 0.000 description 1
- 229920001634 Copolyester Polymers 0.000 description 1
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- 229930182558 Sterol Natural products 0.000 description 1
- SVMCDCBHSKARBQ-UHFFFAOYSA-N acetic acid;cobalt Chemical compound [Co].CC(O)=O SVMCDCBHSKARBQ-UHFFFAOYSA-N 0.000 description 1
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-N benzene-dicarboxylic acid Natural products OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 1
- MTZQAGJQAFMTAQ-UHFFFAOYSA-N benzoic acid ethyl ester Natural products CCOC(=O)C1=CC=CC=C1 MTZQAGJQAFMTAQ-UHFFFAOYSA-N 0.000 description 1
- FUZUFZCLXLEROD-UHFFFAOYSA-N bis(4-hydroxybutyl) benzene-1,2-dicarboxylate Chemical compound OCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCO FUZUFZCLXLEROD-UHFFFAOYSA-N 0.000 description 1
- MRLFFZIIRRKXBJ-UHFFFAOYSA-N bis(4-hydroxybutyl) benzene-1,4-dicarboxylate Chemical compound OCCCCOC(=O)C1=CC=C(C(=O)OCCCCO)C=C1 MRLFFZIIRRKXBJ-UHFFFAOYSA-N 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000010183 spectrum analysis Methods 0.000 description 1
- 150000003432 sterols Chemical class 0.000 description 1
- 235000003702 sterols Nutrition 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
Landscapes
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
201226416 六、發明說明: 【發明所屬之技術領域】 I發明是有關於-種碟系二醇單體及其難燃聚醋共聚 物’且特別是有關於一種以磷系二醇為組成單體之難燃磷 系聚自旨共聚物。 【先前技術】 聚酉旨(polyester)為重要的塑膠材料,其具有良好的機 械及化學特性,被廣泛地應用於合成纖維、織物、薄膜等 相關產業。由於聚g旨高分子大量應用於民生相關產業,因 此合成纖維的耐燃特性逐漸受到重視。 為使聚醋高分子達到難燃效果,可使用摻混(blending) 方式添加難燃劑或將纖維成品進行處理將難燃劑附著於纖 維表面。然而’將聚酯高分子與難燃劑摻混雖然簡便,但 常會有相容性不佳及難燃劑遷移(migration)造成難燃性 下降的情形。另外’以難燃劑加工處理過的織物’在洗滌 次數增加後,織物的難燃性則會下降。 另一方面’可以共聚(COp〇lymer)方式將難燃劑鍵結 於高分子鏈上,此方法利用化學鍵結將難燃劑導入高分子 鏈中’使其不受加工程序的影響而遷移至表面。先前文獻 提出以具有雙醇結構的磷系化合物以共聚方式與萘二甲酸 乙酯(bis(hydroxyethyl) naphthalate ; BHEN)及萘二曱酸 丁酯(bis(hydroxybutyl) naphthalate ; BHBN)進行酯交換 反應得到具有難燃特性的聚酯高分子。(Wang C.S.; Lin, 201226416 C.H. "Synthesis and properties of phosphorus-containing PEN and PBN copolyesters” Polymer, 1999, 40, 747.)。 【發明内容】 因此’本發明之一態樣是在提供一種磷系二醇,可作 為聚醋共聚物之組成單體’提供聚酯共聚物之難燃特性 的。依照本發明之一或多個實施例,填系二醇單體具有如 下式(I)所示之結構:201226416 VI. Description of the invention: [Technical field to which the invention pertains] The invention is related to a dish-type diol monomer and a flame-retardant polyester copolymer thereof, and particularly relates to a phosphorus-based diol as a constituent monomer The flame retardant phosphorus is a self-assembled copolymer. [Prior Art] Polyester is an important plastic material with good mechanical and chemical properties and is widely used in synthetic fibers, fabrics, films and other related industries. Since the poly-g-polymer is widely used in the industry of people's livelihood, the flame-resistant properties of synthetic fibers have gradually received attention. In order to achieve a flame retardant effect on the polyester polymer, a flame retardant may be added by using a blending method or the finished fiber may be treated to attach the flame retardant to the surface of the fiber. However, it is convenient to blend a polyester polymer with a flame retardant, but there is often a case where the compatibility is poor and the flame retardant migration causes a decrease in flame retardancy. Further, when the number of washings is increased by the number of washings treated with the flame retardant, the flame retardancy of the fabric is lowered. On the other hand, it is possible to bond a flame retardant to a polymer chain by means of a COp〇lymer method. This method uses a chemical bond to introduce a flame retardant into the polymer chain to migrate to the polymer chain without being affected by the processing procedure. surface. The prior literature proposes transesterification of bis(hydroxyethyl)naphthalate; BHEN and bis(hydroxybutyl)phthalate (BHBN) in a copolymerized manner with a phosphorus compound having a diol structure. A polyester polymer having flame retardant properties is obtained. (Wang CS; Lin, 201226416 CH " Synthesis and properties of phosphorus-containing PEN and PBN copolyesters" Polymer, 1999, 40, 747.) [Invention] Therefore, one aspect of the present invention is to provide a phosphorus system. The diol, which is a constituent monomer of the polyester copolymer, provides the flame retardant properties of the polyester copolymer. According to one or more embodiments of the present invention, the diol-filling monomer has the following formula (I) Structure:
〇ch2choh〇ch2choh
X 其中,X為氫或甲基,R為氫原子、苯基、C1_C10烷基、 C3-C10環烷基或鹵原子。 本發明之一態樣是在提供一種製備如式(1)所示之磷 系二醇單體的方法。包括利用一磷系化合物(a)、式(b) φ 化合物與一鹼觸媒反應,其中鹼觸媒為CsF、KF、KI、CsCh KC1、K2C〇3、NasCO3、K0H 或 NaOH,且鹼觸媒用量為 鱗系化合物(a)用量的0· 1 wt%〜1〇 wt〇/。:X wherein X is hydrogen or a methyl group, and R is a hydrogen atom, a phenyl group, a C1_C10 alkyl group, a C3-C10 cycloalkyl group or a halogen atom. One aspect of the present invention provides a method of preparing a phosphorus-based diol monomer represented by the formula (1). Including the use of a phosphorus compound (a), a compound of formula (b) φ and a base catalyst, wherein the base catalyst is CsF, KF, KI, CsCh KC1, K2C〇3, NasCO3, K0H or NaOH, and the alkali contact The amount of the medium used is 0·1 wt% to 1〇wt〇/ of the amount of the scaly compound (a). :
(b) 種以式(I)所示之磷系二 本發明之一態樣是在提供一種以茨 醇為組成單體之難燃磷系聚酯共聚物。 201226416 依照本發明之一實施例,難燃磷系聚酯共聚物具有如 下式(II)所示之結構:(b) A phosphorus-based polyester represented by the formula (I) In one aspect of the invention, a flame-retardant phosphorus-based polyester copolymer comprising a sterol as a constituent monomer is provided. 201226416 According to an embodiment of the present invention, the flame-retardant phosphorus-based polyester copolymer has a structure represented by the following formula (II):
(II) 其中’ X為氫或甲基,R為氣原子、苯基、Cl-C10燒基、 C3-C10環烧基或鹵原子,n=2-8,填含量為共聚物的〇 5_3 〇 _ 重量百分比。 依照本發明之另一實施例,難燃填系聚g旨共聚物具有 如下式(III)所示之結構:(II) wherein 'X is hydrogen or methyl, R is a gas atom, phenyl, Cl-C10 alkyl, C3-C10 cycloalkyl or halogen atom, n=2-8, and the content of the copolymer is 〇5_3 〇 _ weight percentage. According to another embodiment of the present invention, the flame-retardant packing copolymer has a structure represented by the following formula (III):
其中,X為氫或甲基,R為氫原子、笨基、CKci〇 、 C3 -C10環烧基或_原子,n=2_8,含量為共聚物的^ 重量百分比。 · 知本發明實施例以磷原子取代傳統造成 方法導入以旨〜、u #单體’應用共聚 万法導入聚“分子中,可在少量的難 κ 良好的阻燃效果,並維持難 Ρ可有 持久穩定。 ^原㈣㈣’使難燃效果 【實施方式】 201226416 (一)磷系二醇單體之合成 本發明實施例之磷系二·醇具有如式(1)所示之結構’ 可作為聚酯共聚物之組成單體,可與一醇酯單體進行酯交 換,經由聚縮合反應形成磷系難燃聚酯共聚物。Wherein X is hydrogen or methyl, R is a hydrogen atom, a strepyl group, a CKci 、, a C3 - C10 cycloalkyl group or a _ atom, and n = 2_8, and the content is a weight percent of the copolymer. · It is understood that the embodiment of the present invention replaces the conventional method by using a phosphorus atom to introduce a method for the introduction of a poly-molecular molecule into a poly-molecular group, which can be used in a small amount of difficult-to-consistence and has a good flame retardant effect and is difficult to maintain. It is durable and stable. ^Original (four) (4) 'Making flame retardant effect 【Embodiment】 201226416 (I) Synthesis of phosphorus-based diol monomer The phosphorus-based diol of the embodiment of the present invention has a structure as shown in formula (1) As a constituent monomer of the polyester copolymer, it can be transesterified with a monool ester monomer to form a phosphorus-based flame retardant polyester copolymer via a polycondensation reaction.
合成例1 :磷系二醇單體DMP-EC DMP-EC是以雙酚單體DMP與碳酸乙烯酯(ethylene carbonate,EC)在驗性觸媒催化下反應而得。其中雙酴單 體DMP如前述式(a)所示,R為甲基。磷系二醇單體DMP-EC • 合成步驟如下: 在一附有溫度指示裝置之0.5升三頸反應器中,加入 42.81克(0.1莫耳)的DMP、碳酸乙烯酯26.4克(0.3莫耳), 鹼觸媒為碳酸鉀30.34克(0.22莫耳),溶劑為DMAc。升高 反應溫度達120°C,將反應系統溫度維持在120°C並反應12 小時後,滴入水中攪拌析出,抽氣過濾後之濾餅再用大量 的去離子水洗務。經過滤分離出之遽餅在11 〇°C下真空烘乾 即為產物(1 )’產率為78%。產物之分子量以高解析質譜 φ 儀鑑定之。Synthesis Example 1: Phosphorus-based diol monomer DMP-EC DMP-EC is obtained by reacting a bisphenol monomer DMP with ethylene carbonate (EC) under a catalytic catalyst. Wherein the biguanide monomer DMP is represented by the above formula (a), and R is a methyl group. Phosphorus diol monomer DMP-EC • The synthesis procedure is as follows: In a 0.5 liter three-neck reactor equipped with a temperature indicating device, 42.81 g (0.1 mol) of DMP and 26.4 g of ethylene carbonate (0.3 mol) were added. The base catalyst is 30.34 g (0.22 mol) of potassium carbonate, and the solvent is DMAc. The reaction temperature was raised to 120 ° C, the reaction system temperature was maintained at 120 ° C and reacted for 12 hours, and then dropped into water to be stirred and precipitated, and the filter cake after suction filtration was washed with a large amount of deionized water. The cake separated by filtration was vacuum dried at 11 ° C to give a product (1 )' yield of 78%. The molecular weight of the product was identified by a high resolution mass spectrometer φ instrument.
第1圖為產物(1)之1H NMR圖譜。光譜分析的結果顯 示,產物(1)為DMP-EC,分子式為c30H29O6P,分子量為 516.1698。 201226416 (二)破系難燃聚輯共聚物之合成 根據本發明之一實施方式,難燃磷系聚酯共聚物可利 用上述之碌系二醇單體與對苯二甲酸醇酯進行聚縮合反應 而得,反應式如第2圖所示,可合成如式(11)所示之結構:Figure 1 is a 1H NMR spectrum of the product (1). The results of the spectral analysis revealed that the product (1) was DMP-EC, the molecular formula was c30H29O6P, and the molecular weight was 516.1698. 201226416 (II) Synthesis of broken flame-retardant polymer copolymer According to an embodiment of the present invention, the flame-retardant phosphorus-based polyester copolymer can be polycondensed by using the above-mentioned diol monomer and terephthalic acid ester. The reaction is obtained, and the reaction formula is as shown in Fig. 2, and the structure shown in the formula (11) can be synthesized:
(II) 合成例2 :磷含量1.5 wt%之磷系難燃聚酯共聚物之合成 取 21.77 克(42.18 mmol)的產物(1)、90 克(354 mmol) 之對苯曱酸乙酯(bis(hydroxyethyl) terephthalate ; BHET )、 觸媒Ti(OBu)4及醋酸鈷,置入500毫升三頸反應器中。將溫 度升至270°C維持80分鐘後,將反應器内的壓力降至1-3 mmHg,並將溫度維持在約280°C進行聚縮合反應即可得到 磷含量1.5 wt%之磷系難燃聚酯共聚物peh s。 合成出的PET-1.5,其性質包括:極限黏度為〇.58dl/g, 極限黏度可反應出高分子在溶液中的流體力學尺寸。利用 4 NMR積分面積所計算出來的實際磷含量為1.47 wt%,與 預期值接近。利用動態機械測定儀(Dynamic Mechanical Analyzer ; DMA)所測得玻璃轉移溫度為85°C,在UL-94 垂直燃燒性質測試上則為VI等級。 合成例3 :磷含量1.8wt%之PET-1.8之合成 取27.69克(53.65 mmol)產物(1 )、90g ( 354 mmol) 201226416 之對笨曱酸乙酯、觸媒Ti(OBu)4及醋酸鈷,置入500毫升三 頸反應器中。將溫度升至270°C維持80分鐘後,將反應器内 的壓力降至1-3 mmHg,並將溫度維持在約280DC進行聚縮 合反應即可得到填含量1.8 wt%之磷系難燃聚酯共聚物 PET-1.8。 合成出的PET-1.5,其性質包括:極限黏度為0.56 dl/g, 實際磷含量為1.76 wt% ’與預期值接近。DMA所測得玻璃 轉移溫度為90°C,在UL-94測試上則達到v〇等級。 合成例4 :磷含量1.8wt%之PBT-1.8之合成 取 10.40克(20.15 mmol)產物(1 )、90g ( 290 mmol) 之對笨甲酸丁酯(bis( hydroxybutyl) terephthalate; BHBT )、 觸媒Ti(OBu)4及醋酸鈷,置入500毫升三頸反應器中。將溫 度升至270°C維持80分鐘後,將反應器内的壓力降至1_3 mmHg,並將溫度維持在約260°C進行聚縮合反應即可得到 填含量1.8 wt%之磷系難燃聚酯共聚物ΡΒτ_ 1.8。 合成出的PBT-1.8 ’其性質包括:極限黏度為0.55 dl/g, 實際磷含量為1.76 wt% ’與預期值接近。DMA所測得玻璃 轉移溫度為65 °C,在UL-94測試上則達到v 1等級。 合成例5 :磷含量2.3 wt%之PBT-2.3之合成 取 14.63克(28.34 mmol)產物(1)、9〇g ( 290 mmol) 之對笨曱酸丁酯、觸媒Ti(OBu)4及醋酸鈷置入500毫升三頸 反應器中。將溫度升至260°C維持80分鐘後,將反應器内的 壓力降至1-3 mmHg’並將溫度維持在約26〇°C進行聚縮合 201226416 反應即可得到磷含量2.3 wt°/〇之磷系難燃聚酯共聚物 PBT-2.3。 合成出的PBT-2.3,其性質包括:極限黏度為0.53 dl/g, 實際磷含量為1.76 wt% ’與估算值接近。利用DMA所測得 玻璃轉移溫度為72 °C,在UL-94測試上則可達到V0等級。 根據本發明之另一實施方式,難燃磷系聚酯共聚物可 利用上述之磷系二醇單體與對2,6-萘二曱酸醇酯進行聚縮 合反應而得’反應式如第3圖所示,可合成如式(hi)所示 φ 之結構··(II) Synthesis Example 2: Synthesis of phosphorus-based flame retardant polyester copolymer having a phosphorus content of 1.5 wt% 21.77 g (42.18 mmol) of product (1), 90 g (354 mmol) of ethyl p-benzoate ( Bis(hydroxyethyl) terephthalate; BHET), catalyst Ti(OBu)4 and cobalt acetate were placed in a 500 ml three-neck reactor. After the temperature was raised to 270 ° C for 80 minutes, the pressure in the reactor was lowered to 1-3 mmHg, and the temperature was maintained at about 280 ° C for polycondensation reaction to obtain a phosphorus content of 1.5 wt% phosphorus. Burning polyester copolymer peh s. The synthesized PET-1.5 has properties including an ultimate viscosity of 58.58 dl/g, and the ultimate viscosity can reflect the hydrodynamic size of the polymer in solution. The actual phosphorus content calculated using the 4 NMR integrated area was 1.47 wt%, which was close to the expected value. The glass transition temperature was measured at 85 ° C using a Dynamic Mechanical Analyzer (DMA) and at the UL-94 vertical burning property test. Synthesis Example 3: Synthesis of PET-1.8 having a phosphorus content of 1.8% by weight 27.69 g (53.65 mmol) of product (1), 90 g (354 mmol) of 201226416 of ethyl acenamate, catalyst Ti(OBu)4 and acetic acid Cobalt was placed in a 500 ml three-neck reactor. After the temperature was raised to 270 ° C for 80 minutes, the pressure in the reactor was lowered to 1-3 mmHg, and the temperature was maintained at about 280 DC to carry out a polycondensation reaction to obtain a phosphorus-based flame retardant polymer having a filling content of 1.8 wt%. Ester copolymer PET-1.8. The synthesized PET-1.5 has properties including an ultimate viscosity of 0.56 dl/g and an actual phosphorus content of 1.76 wt% 'close to the expected value. The DMA measured a glass transition temperature of 90 ° C and achieved a v 〇 rating on the UL-94 test. Synthesis Example 4: Synthesis of PBT-1.8 having a phosphorus content of 1.8% by weight 10.40 g (20.15 mmol) of product (1), 90 g (290 mmol) of bis(hydroxybutyl) terephthalate; BHBT, catalyst Ti(OBu)4 and cobalt acetate were placed in a 500 ml three-neck reactor. After the temperature was raised to 270 ° C for 80 minutes, the pressure in the reactor was reduced to 1-3 mmHg, and the temperature was maintained at about 260 ° C for polycondensation reaction to obtain a phosphorus-based flame retardant polymer with a filling content of 1.8 wt%. Ester copolymer ΡΒτ_ 1.8. The synthesized PBT-1.8' properties include: an ultimate viscosity of 0.55 dl/g and an actual phosphorus content of 1.76 wt% 'close to the expected value. The glass transition temperature measured by DMA was 65 °C, and the v-1 rating was achieved on the UL-94 test. Synthesis Example 5: Synthesis of PBT-2.3 having a phosphorus content of 2.3 wt% 14.63 g (28.34 mmol) of product (1), 9 〇g (290 mmol) of butyl benzoate, catalyst Ti(OBu) 4 and Cobalt acetate was placed in a 500 ml three-neck reactor. After the temperature was raised to 260 ° C for 80 minutes, the pressure in the reactor was lowered to 1-3 mmHg ' and the temperature was maintained at about 26 ° C to carry out polycondensation 201226416 reaction to obtain a phosphorus content of 2.3 wt ° / 〇 Phosphorus-based flame retardant polyester copolymer PBT-2.3. The synthesized PBT-2.3 has properties including: ultimate viscosity of 0.53 dl/g and actual phosphorus content of 1.76 wt% 'close to the estimated value. The glass transition temperature measured by DMA was 72 °C, and the V0 rating was achieved on the UL-94 test. According to another embodiment of the present invention, the flame-retardant phosphorus-based polyester copolymer can be obtained by a polycondensation reaction of the above-mentioned phosphorus-based diol monomer with 2,6-naphthalene dinonanoate, and the reaction form is as follows. As shown in Fig. 3, it is possible to synthesize the structure of φ as shown in the formula (hi)··
(III) 合成例6 :雄含量0.5 wt%之PBN-0.5之合成 取6.69克(12.96111111〇1)產物(1)、9(^(25〇111111〇1) 之對-萘二曱酸醇酯(bis ( hydroxyethyl ) naphthalate ; BHEN)、Ti(0Bu)4及醋酸鈷,置入500毫升三顯反應器中。 將溫度升至260°C維持80分鐘後,將反應器内的壓力降至 1-3 mmHg’並將溫度維持在約265°C進行聚縮合反應即可 得到磷含量0.5 wt%之磷系難燃聚酯共聚物5。 合成出的PBN-0.5,其性質包括:極限黏度為〇 56 m/g, 實際磷含量為0.48 wt%,與估算值接近。利用〇]^人所測得 玻璃轉移溫度為126°C,在UL-94測試上則達到v〇冑級。 實例7 :磷含量1.0 wt%之PBN-1.0之合成 201226416 取 13.03克(12.96 mmol)產物(l)、90g ( 250 mmol) 之對-萘一曱酸醇酉旨(bis ( hydroxyethyl ) naphthalate ; BHEN)、Ti(OBu)4及醋酸鈷,置入5〇〇毫升三頸反應器中。 將溫度升至260°C維持8〇分鐘後,將反應器内的壓力降至 1-3 mtnHg ’並將溫度維持在約265〇c進行聚縮合反應即可 得到磷含量1.0 wt%之磷系難燃聚酯共聚物pBN-l.O。(III) Synthesis Example 6: Synthesis of PBN-0.5 having a male content of 0.5 wt% 6.69 g (12.96111111〇1) of the product (1), 9 (^(25〇111111〇1) of p-naphthalene dinonanoate (bis ( hydroxyethyl ) naphthalate ; BHEN), Ti(0Bu) 4 and cobalt acetate, placed in a 500 ml three-display reactor. After the temperature was raised to 260 ° C for 80 minutes, the pressure in the reactor was reduced to 1 -3 mmHg' and maintaining the temperature at about 265 ° C for polycondensation reaction to obtain a phosphorus-based flame retardant polyester copolymer 5 having a phosphorus content of 0.5 wt%. The synthesized PBN-0.5 has properties including: ultimate viscosity is 〇56 m/g, the actual phosphorus content is 0.48 wt%, which is close to the estimated value. The glass transition temperature measured by 〇^^^ is 126 °C, and the UL-94 test reaches v〇胄 level. : Synthesis of PBN-1.0 with a phosphorus content of 1.0 wt% 201226416 Take 13.03 g (12.96 mmol) of product (1), 90 g (250 mmol) of p-naphthyl phthalate (BHEN), Ti(OBu)4 and cobalt acetate were placed in a 5 〇〇 ml three-neck reactor. After the temperature was raised to 260 ° C for 8 〇 minutes, the pressure in the reactor was reduced to 1-3 mtnHg ' The temperature was maintained at about 265〇c polycondensation reaction was performed to obtain a phosphorus content of 1.0 wt% of the phosphorus-based flame retardant polyester copolymer pBN-l.O.
其極限黏度為0.53 dl/g,利用1H NMR積分面積所計算 出來的實際磷含量為0.98 wt%,與預估值接近。利用DMA φ 所測得玻璃轉移溫度為92。(:,在UL-94測試上則可達到V0 等級。 合成出的PBN-0.5,其性質包括:極限黏度為0.53The ultimate viscosity is 0.53 dl/g, and the actual phosphorus content calculated using the 1H NMR integrated area is 0.98 wt%, which is close to the estimated value. The glass transition temperature measured by DMA φ was 92. (:, V0 grade can be achieved on UL-94 test. Synthetic PBN-0.5, its properties include: ultimate viscosity is 0.53
dl/g,實際磷含量為0.98 wt°/Q,與估算值接近。利用DMA 所測得玻璃轉移溫度為126°c,在UL_94測試上則達到V0 等級。 、 由上述本發明實施方式可知,本發明實施例以磷原子 取代傳統造成環境危害的齒素原子合成難燃的磷系二醇單 #體’應用共聚方法導入聚酿高分子中,可在少量的難燃劑 存在下即可有良好的阻燃效果,並維持難燃劑原有的特 性,使難燃效果持久穩定。 本發明實施例之磷系難燃聚酯共聚物,可應用於難燃 纖維、難燃織物、難燃不織物、難燃薄膜、難燃接著劍及 難燃塑膠領域。 雖然本發明已以實施方式揭露如上,然其並非用以眼 定本發明,任何熟習此技藝者,在不脫離本發明之精神和 201226416 【圖式簡單說明】 為讓本發明之上述和其他目的、特徵、優點與實施例 能更明顯易懂,所附圖式之說明如下: 第1圖為產物(1 )之1H NMR圖譜。 第2圖為依照本發明一實施例之合成難燃磷系聚酯共 • 聚物(Π)的反應流程圖。 第3圖為依照本發明一實施例之合成難燃磷系聚酯共 聚物(III)的反應流程圖。 【主要元件符號說明】 無元件符號Dl / g, the actual phosphorus content is 0.98 wt ° / Q, close to the estimated value. The glass transition temperature measured by DMA was 126 ° C, and the V0 rating was achieved on the UL_94 test. According to the embodiment of the present invention, the embodiment of the present invention introduces a phosphorus atom to replace a conventionally toxic phosphatide diol olefinic single-body composite copolymerization method into a poly-bulk polymer, which can be used in a small amount. The flame retardant can have a good flame retardant effect in the presence of the flame retardant, and maintain the original characteristics of the flame retardant to make the flame retardant effect lasting and stable. The phosphorus-based flame retardant polyester copolymer of the embodiment of the invention can be applied to the fields of flame retardant fibers, flame retardant fabrics, flame retardant fabrics, flame retardant films, flame retardant swords and flame retardant plastics. While the invention has been described above in terms of the embodiments of the present invention, it is not intended to limit the scope of the invention, and The features, advantages and embodiments are more apparent and the description of the drawings is as follows: Figure 1 is a 1H NMR spectrum of the product (1). Fig. 2 is a flow chart showing the reaction of synthesizing a flame retardant phosphorus-based polyester copolymer (Π) according to an embodiment of the present invention. Fig. 3 is a flow chart showing the reaction of synthesizing a flame retardant phosphorus-based polyester copolymer (III) according to an embodiment of the present invention. [Main component symbol description] No component symbol
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