TW201206972A - Fluorochemical composition for treatment of paper - Google Patents
Fluorochemical composition for treatment of paper Download PDFInfo
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- TW201206972A TW201206972A TW100112461A TW100112461A TW201206972A TW 201206972 A TW201206972 A TW 201206972A TW 100112461 A TW100112461 A TW 100112461A TW 100112461 A TW100112461 A TW 100112461A TW 201206972 A TW201206972 A TW 201206972A
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/57—Polyureas; Polyurethanes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/0804—Manufacture of polymers containing ionic or ionogenic groups
- C08G18/0809—Manufacture of polymers containing ionic or ionogenic groups containing cationic or cationogenic groups
- C08G18/0814—Manufacture of polymers containing ionic or ionogenic groups containing cationic or cationogenic groups containing ammonium groups or groups forming them
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/0838—Manufacture of polymers in the presence of non-reactive compounds
- C08G18/0842—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents
- C08G18/0861—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers
- C08G18/0866—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers the dispersing or dispersed phase being an aqueous medium
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/50—Polyethers having heteroatoms other than oxygen
- C08G18/5003—Polyethers having heteroatoms other than oxygen having halogens
- C08G18/5015—Polyethers having heteroatoms other than oxygen having halogens having fluorine atoms
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/50—Polyethers having heteroatoms other than oxygen
- C08G18/5021—Polyethers having heteroatoms other than oxygen having nitrogen
- C08G18/5036—Polyethers having heteroatoms other than oxygen having nitrogen containing -N-C=O groups
- C08G18/5039—Polyethers having heteroatoms other than oxygen having nitrogen containing -N-C=O groups containing amide groups
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/77—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
- C08G18/78—Nitrogen
- C08G18/79—Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates
- C08G18/791—Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates containing isocyanurate groups
- C08G18/792—Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates containing isocyanurate groups formed by oligomerisation of aliphatic and/or cycloaliphatic isocyanates or isothiocyanates
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
- C09D175/04—Polyurethanes
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/10—Coatings without pigments
- D21H19/12—Coatings without pigments applied as a solution using water as the only solvent, e.g. in the presence of acid or alkaline compounds
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/16—Sizing or water-repelling agents
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/10—Packing paper
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
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- Polyurethanes Or Polyureas (AREA)
Abstract
Description
201206972 六、發明說明: 【發明所屬之技術領域】 本發明係關於氟化學組成物,其可藉由聚異氰酸酯化 合物與至少一種具有至少一個陽離子基團的異氰酸酯反應 性氟化聚醚化合物反應獲得,及其使紙防油的用途。 【先前技術】 0 紙工業製作極多種用於包裝食品且與食品接觸之包裝 材料。與油性或油脂食品接觸之紙需要防污及防滲漏阻障 性。藉由施加在紙表面上或藉由在紙形成之前添加至紙漿 中,氟化學品通常提供此種阻障性。 關於處理紙以使其適用於與食品接觸的重要要求是使 所包裝之食品受任何有害或潛在有害人類或動物健康之物 質的污染的危險最小化。最佳的狀況是當該紙一點也不含 有任何有害物質或至少在其使用期間不釋出有害物質。該 Q 氟化學品應將疏油特性賦予所處理之紙。 全氟烷基衍生物通常是含有4至20個碳原子之不同鏈 長的分子混合物。此類化學品之缺點是難以完全消除非所 欲、頑固且生物累積性的污染物全氟辛酸(PFOA )及全 氟辛烷磺酸(PFOS)。艱鉅的事是要發現不含PFOA/PFOS 之氟化學品,其與現有之產品相比,具有相同或類似之應 用效能。 令人驚訝地,據發現:具有至少一個陽離子基團之異 氰酸酯反應性氟化學之聚醚,在與多官能異氰酸酯反應時 -5- 201206972 ,使不含PFOA/PFOS的氟化學化合物在用於紙上時顯出令 人意外之良好效能。 【發明內容】 因此本發明係關於一種化合物COMP,其可藉由至少 二反應物A及B以及隨意之一或多種異氰酸酯反應性共反應 物C之反應獲得,其中A是式(I )化合物:201206972 VI. Description of the Invention: [Technical Field] The present invention relates to a fluorine chemical composition obtainable by reacting a polyisocyanate compound with at least one isocyanate-reactive fluorinated polyether compound having at least one cationic group, And the use of paper to prevent oil. [Prior Art] 0 The paper industry produces a wide variety of packaging materials for packaging foods and in contact with food. Paper that comes into contact with oily or fat foods requires anti-fouling and leak-proof barrier properties. Fluorochemicals generally provide such barrier properties by application to the surface of the paper or by addition to the pulp prior to paper formation. An important requirement for treating paper to make it suitable for contact with food is to minimize the risk of contamination of the packaged food by any material that is harmful or potentially harmful to human or animal health. The best condition is when the paper is not containing any harmful substances at all or at least not releasing harmful substances during its use. The Q fluorochemical should impart oleophobic properties to the treated paper. The perfluoroalkyl derivative is usually a mixture of molecules having different chain lengths of 4 to 20 carbon atoms. A disadvantage of this type of chemical is that it is difficult to completely eliminate the undesired, stubborn and bioaccumulative contaminants perfluorooctanoic acid (PFOA) and perfluorooctane sulfonate (PFOS). The hard part is to find fluorochemicals that do not contain PFOA/PFOS, which have the same or similar application performance compared to existing products. Surprisingly, it has been found that isocyanate-reactive fluorochemical polyethers having at least one cationic group, when reacted with polyfunctional isocyanates -5 to 201206972, make fluorochemical compounds free of PFOA/PFOS on paper It shows unexpectedly good performance. SUMMARY OF THE INVENTION The present invention therefore relates to a compound COMP obtainable by the reaction of at least two reactants A and B and optionally one or more isocyanate-reactive co-reactants C, wherein A is a compound of formula (I):
Rr0-(CF(CF3)CF20)mCF(CF3)-X-Y-Z (I) 其中Rr0-(CF(CF3)CF20)mCF(CF3)-X-Y-Z (I)
Rf是全氟烷基; m是3至2 5 ; X是羰基或CH2 ; Y是化學鍵結或具有單一官能或雙官能異氰酸酯反應 性基團之有機雙鍵或三鍵連結基團; Z是具有至少一個陽離子基團之有機基圑, 且反應物B是多官能異氰酸酯或其混合物。 較佳地,反應物A是式(I)化合物混合物’其中m是4 至22。 較佳地,反應物A具有750至4000克/莫耳,更佳地具 有10 00至3000克/莫耳且甚至更佳地具有I5 〇〇至2500克/ 莫耳之平均分子量。 較佳地,反應物A另外含有0至10重量% ’更佳地〇至5 重量%,甚至更佳地〇至1重量%,特佳地〇至〇 · 1重量%之具 有少於750克/莫耳分子量的化合物,該重量%係以反應物 -6- 201206972 A之總重量計。 較佳地,反應物A是一種式(I)化合物,其中X是羰 基。 較佳地,反應物A是一種式(I)化合物,其中Y是包 含一或二個異氰酸酯反應性基團(包括硫醇、羥基及胺基 ,更佳是胺基,甚至更佳是二級胺基)之連結基團。 較佳地,反應物A是式(I)化合物,其中Z是具有至 0 少一個陽離子基團(包括三級胺、N-氧化物或銨基團)之 連結基團。N-氧化物或銨基團也可以藉由在反應物A與B 間之反應後三級胺基的處理而獲得。 更佳地,反應物A是是(II )化合物: Rr0-(CF(CF3)CF20)mCF(CF3)-C0N(R1)-R2-NH-R3-N(R4)2 (II) 其中 以及m係如以上所定義與其全部較佳具體例, R1是氫或例如1至4個碳原子之烷基, Q R2及R3獨立地是具有1至15個碳原子之伸烷基,且 R4是具有1至4個碳原子之烷基。 較佳地,反應物A是式(II )化合物,其中Rf及m係如 以上定義與其所有較佳具體例,R1是氫,R2及R3是2或3碳 原子之伸烷基,且R4是甲基。 較佳地,反應物B是具有至少3個異氰酸酯基團的聚異 氰酸酯或平均每一分子具有多於2個異氰酸酯基團的聚異 氰酸酯化合物之混合物,例如二異氰酸酯化合物及具有至 少3個異氰酸酯之聚異氰酸酯化合物的混合物。該聚異氰 201206972 酸酯可以是脂族或芳族。實例包括伸己基二異氰酸酯、 2,2,4-三甲基-1,6-伸己基二異氰酸酯、1,2-伸乙基二異氰 酸酯、二環己基甲烷-4,4’-二異氰酸酯、1,3,6-伸己基三異 氰酸酯、伸己基二異氰酸酯之環狀三聚物、異佛爾酮二異 氰酸酯之環狀三聚物、4,4’-伸甲基二苯基二異氰酸酯、 4,6-二-(三氟甲基)-1,3-苯二異氰酸酯、2,4-甲苯二異氰 酸酯、2,6 -甲苯二異氰酸酯、鄰-、間-及對-二甲苯二異氰 酸酯、4,4’-二異氰醯二苯醚、3,3-二氯-4,4’-二異氰醯二 苯基甲烷、4,5’-二苯基二異氰酸酯、4,4’-二異氰醯苄基、 3,3’-二甲氧基-4,4’-二異氰醯二苯基、3,3’-二甲基_4,4,_二 異氰醯二苯基、2,2’-二氯-5,5’-二甲氧基_4,4’-二異氰醯二 苯基、1,3-二異氰醯苯、1,2-萘二異氰酸酯、4-氯-l,2-萘 二異氰酸酯、1,3-萘二異氰酸酯、1,8-二硝基-2,7-萘二異 氰酸酯、聚伸苯基聚苯基異氰酸酯、3-異氰醯甲基-3,5,5_ 三甲基環己基異氰酸酯、聚伸甲基聚伸苯基異氰酸酯、含 有自身縮合部分之異氰酸酯類諸如含有縮二脲或異氰脲酸 酯之聚異氰酸酯、或含有阿特定二酮(azetedinedione ) 之二異氰酸酯類。 較佳地,使用共反應物C,其包含具有一或多個異氰 酸酯反應性基團之非氟化的或氟化的有機化合物。 較佳地,使用共反應物C是具有一或多個異氰酸酯反 應性基團之氟化的有機化合物。 更佳地,共反應物C是式(III )之化合物 (Rr〇-(CF(CF3)CF2〇)mCF(CF3)-X)n-Q (III) 201206972 其中Rf is a perfluoroalkyl group; m is 3 to 2 5 ; X is a carbonyl group or CH 2 ; Y is a chemically bonded or organic double or triple bond group having a monofunctional or difunctional isocyanate reactive group; At least one organic group of a cationic group, and the reactant B is a polyfunctional isocyanate or a mixture thereof. Preferably, reactant A is a mixture of compounds of formula (I) wherein m is from 4 to 22. Preferably, reactant A has from 750 to 4000 g/mole, more preferably from 100 to 3000 g/mol and even more preferably has an average molecular weight of from 1 5 Å to 2500 g/mole. Preferably, the reactant A additionally contains 0 to 10% by weight, more preferably 5% to 5% by weight, even more preferably 〇 to 1% by weight, particularly preferably 〇 to 1% by weight, having less than 750 g. /Mole molecular weight compound, the weight % based on the total weight of the reactant-6-201206972 A. Preferably, reactant A is a compound of formula (I) wherein X is a carbonyl group. Preferably, reactant A is a compound of formula (I) wherein Y is one or two isocyanate-reactive groups (including mercaptans, hydroxyl groups and amine groups, more preferably amine groups, even more preferably secondary A linking group of an amine group. Preferably, reactant A is a compound of formula (I) wherein Z is a linking group having one cationic group to less than zero, including a tertiary amine, N-oxide or ammonium group. The N-oxide or ammonium group can also be obtained by treatment of a tertiary amine group after the reaction between reactants A and B. More preferably, the reactant A is a compound of (II): Rr0-(CF(CF3)CF20)mCF(CF3)-C0N(R1)-R2-NH-R3-N(R4)2 (II) wherein m As defined above, and all preferred embodiments thereof, R1 is hydrogen or an alkyl group such as 1 to 4 carbon atoms, Q R2 and R3 are independently an alkylene group having 1 to 15 carbon atoms, and R 4 is An alkyl group of 1 to 4 carbon atoms. Preferably, reactant A is a compound of formula (II) wherein Rf and m are as defined above and all preferred embodiments thereof, R1 is hydrogen, R2 and R3 are alkylene groups of 2 or 3 carbon atoms, and R4 is methyl. Preferably, reactant B is a mixture of polyisocyanates having at least 3 isocyanate groups or polyisocyanate compounds having an average of more than 2 isocyanate groups per molecule, such as diisocyanate compounds and having at least 3 isocyanates A mixture of isocyanate compounds. The polyisocyanate 201206972 acid ester can be aliphatic or aromatic. Examples include hexyl diisocyanate, 2,2,4-trimethyl-1,6-extended hexyl diisocyanate, 1,2-extended ethyl diisocyanate, dicyclohexylmethane-4,4'-diisocyanate, 1 , 3,6-extended hexyl isocyanate, cyclic trimer of hexyl diisocyanate, cyclic trimer of isophorone diisocyanate, 4,4'-methyldiphenyl diisocyanate, 4, 6-di-(trifluoromethyl)-1,3-benzenediisocyanate, 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, o-, m- and p-xylene diisocyanate, 4, 4'-diisocyanoquinone diphenyl ether, 3,3-dichloro-4,4'-diisocyanoquinone diphenylmethane, 4,5'-diphenyl diisocyanate, 4,4'-diiso Cyanonylbenzyl, 3,3'-dimethoxy-4,4'-diisocyanide diphenyl, 3,3'-dimethyl-4,4,-diisocyanide diphenyl, 2,2'-Dichloro-5,5'-dimethoxy_4,4'-diisocyanide diphenyl, 1,3-diisocyanoquinone, 1,2-naphthalene diisocyanate, 4 -Chloro-l,2-naphthalene diisocyanate, 1,3-naphthalene diisocyanate, 1,8-dinitro-2,7-naphthalene diisocyanate, polyphenylene polyphenyl isocyanate, 3-isocyanide Methyl-3,5,5-trimethylcyclohexyl isocyanate, polymethylene polyphenylene isocyanate, isocyanate containing self-condensing moiety such as polyisocyanate containing biuret or isocyanurate, or a diisocyanate of a specific diketone (azetedinedione). Preferably, a co-reactant C comprising a non-fluorinated or fluorinated organic compound having one or more isocyanate-reactive groups is used. Preferably, the co-reactant C is a fluorinated organic compound having one or more isocyanate-reactive groups. More preferably, the co-reactant C is a compound of the formula (III) (Rr〇-(CF(CF3)CF2〇)mCF(CF3)-X)n-Q (III) 201206972 wherein
Rf、X及m係如以上定義與其全部較佳具體例, Q是具有單一官能或雙官能之異氰酸酯反應性基團之 有機基團或有機二價或三價連結基團; η是1或2。 較佳地’共反應物C是式(III)化合物,其中Q是包 含一或二個異氰酸酯反應性基團(諸如硫醇、羥基、及胺 0 基’更佳是胺基’甚至更佳是二級胺基)的有機基團。 更佳地,共反應物C是式(IVa )或(IVb )之化合物 或二者之混合物:Rf, X and m are as defined above and all preferred embodiments thereof, Q is an organic group having a monofunctional or difunctional isocyanate-reactive group or an organic divalent or trivalent linking group; η is 1 or 2 . Preferably, the co-reactant C is a compound of the formula (III) wherein Q is one or two isocyanate-reactive groups (such as a thiol, a hydroxyl group, and an amine group 'preferably an amine group' or even more preferably The organic group of the secondary amine group. More preferably, the co-reactant C is a compound of formula (IVa) or (IVb) or a mixture of the two:
Rr〇-(CF(CF3)CF20)mCF(CF3)-CON(R1)-R2-OH (IVa) (Rr〇-(CF(CF3)CF20)mCF(CF3)-C〇N(R1)-R2)n-N(R5)H (IVb) 其中Rf、R1、R2、m及n係如先前定義與其全部較佳具體例 ,R5是氫(若η是1)或具有1至4個碳原子之烷基。 β 甚至更佳地,共反應物C是式(IVb )之化合物。 ❹ 較佳地,反應物A及共反應物C之異氰酸酯反應性基團 的總化學計量是少於或等於反應物B之異氰酸酯基團的總 化學計量;更佳地,反應物A及共反應物C之異氰酸醋反應 性基團的總化學計量是反應物B之異氰酸醋基團的總化學 計量的0.8至1倍。 在一甚至更佳的具體例中,反應物A及共反應物C之異 氰酸酯反應性基團的總化學計量是反應物B之異氯酸醋基 團的總化學計量的0.9至1倍。 較佳地,共反應物C之異氰酸酯反應性基團之總化學 -9 - 201206972 計量是反應物A之異氰酸酯反應性基團之總化學計量的0至 倍’更佳是〇至7倍’且甚至更佳是0至4倍’甚至更佳是 〇至1倍。 若反應物A及共反應物C之異氰酸醋反應性基團之總化 學計量少於反應物B之異氰酸酯基團之總化學計量’則過 量之異氰酸酯基團較佳經由自身聚合作用或與多官能異氰 酸酯反應性化合物(包括水、多元醇或多元胺)的反應進 一步聚合。 另外,本發明之主題是一種製造化合物COMP之方法 ’其特徵在於使反應物B與反應物A及隨意地共反應物C反 應’而反應物A、B及C具有如上述之意義’也與其所有較 佳具體例。 可以使用任何添加順序。較佳地’反應物A及共反應 物C同時添加至反應物B。 較佳地,反應物A、B及C之化學計量具有如上述之意 義與其所有較佳具體例。 較佳地,反應溫度是〇至120°C且更佳是20至8〇°C ;較 佳地,壓力是在大氣壓至2巴之間,且更佳在大氣壓至1.2 巴之間。 較佳地,反應時間是1分鐘至4 8小時,且更佳是1 〇分 鐘至6小時。 該反應可以在有或沒有觸媒存在下進行。適合之觸媒 包栝胺;錫鹽如二月桂酸二丁基錫、二乙酸二丁基錫、二 (2-乙基己酸)二丁基錫、辛酸亞錫、油酸亞錫、氯化亞 -10- 201206972 錫;鉍鹽如及其他精於此技藝者已知的。通常,觸媒之較 佳濃度以反應物之總重量計係0.001重量%至1 〇重量%,且 較佳0.1重量%至5重量%。 較佳地,反應係在無任何觸媒存在下進行。 在另一較佳具體例中,反應係在非質子溶劑或非質子 溶劑混合物中進行。較佳之溶劑是丙酮、乙酸乙酯、甲基 異丁酮、環己酮、四氫呋喃、乙醚、第三丁基甲醚、氫氟 0 醚(諸如甲氧基九氟丁烷)、三氟甲苯、1,3-雙(三氟甲 基)苯及其混合物。 該反應可例如藉由紅外(IR )光譜測定法控制。 未反應之反應物B可以藉由利用不能溶解COMP之非氟 化之有機溶劑清洗COMP而移除。 本發明之另外的主題是化合物COMP之水性分散液 DISP或溶液SOL。 較佳地,分散液DISP或溶液SOL包含0.5至40重量%之 Q 化合物COMP,更佳是5至30重量%,該重量%是以分散液 D I S P或溶液S Ο L之總重量計。因此,化合物C Ο Μ P較佳被 分散或溶解在水中。 除了水之外,該分散液或溶液也可以有或沒有共溶劑 之存在。 較佳地,共溶劑可以緩慢地添加至反應混合物’同時 在製備化合物COMP期間所用之任何溶劑被蒸出’然後所 得之產物利用酸中和,然後添加水。 較佳地,反應之溶劑的蒸餾係在真空下進行。 -11 - 201206972 較佳地,用於中和之酸係選自以下族群:乙酸及乳酸 、己酸、苯甲酸、卡伯酸(caPrilic acid)、檸檬酸、甲 酸、壬二酸、硼酸、異苯二甲酸、衣康酸、月桂酸、順丁 烯二酸、蘋果酸、草酸、磷酸、苯二甲酸、苯均四酸、丁 二酸、對苯二甲酸、抗壞血酸、次磷酸、波丕酸( propionic acid)、擴酸、硫酸氫鈉或對苯振酸、戊一酸、 對羥基苯甲酸、樹脂酸及松香酸、水楊酸、癸二酸。 用於分散液或溶液之共溶劑較佳是水可溶的或至少部 分水可溶的,更佳地共溶劑具有至少一個羥基,甚至更佳 地共溶劑是二醇。在一較佳具體例中,共溶劑係選自以下 族群:乙二醇、二乙二醇、三乙二醇、多元乙二醇、丙二 醇、二丙二醇、三丙二醇、多元丙二醇、己二醇-Π,6]、 己二醇、聚四氫呋喃、這些二醇之單烷基醚、及這些溶劑 之混合物。 隨意地,化合物COMP可分散或溶解於共溶劑或不含 水之混合物中,而共溶劑係如以上定義與其全部的具體例 〇 較佳地,用於分散液或用於溶解之溫度是2 5至2 0 0 °C ,更佳是25至150 °C,仍更佳是25至100 °C。 較佳地,用於分散或溶解之反應時間是5分鐘至6小時 〇 本發明之另一主題是化合物COMP之用途’較佳係以 分散液DISP或溶液SOL形式,用於處理紙以使紙防油。 本發明之另外的主題是一種製紙的方法’其特徵在於 -12- 201206972 利用化合物COMP處理紙。 較佳地,紙利用分散液DISP或溶液SOL形式之化合物 COMP處理。 再者,本發明係關於利用包含化合物COMP之溶液或 分散液處理的紙張。藉由使用先前技藝已知之施加方法, 本發明之化合物COMP可用於紙上膠。例如,彼可以藉由 表面處理(上膠加壓及/或塗覆)已形成之紙而被施加。 ❹ 另一方法是濕部法(wet-end ),其是在紙獎中之施加法 〇 對於該施加法而言,紙、紙板等係利用合適介質(水 或水及溶劑混合物)之分散液D I S P或溶液S Ο L處理。在表 面處理之事例中,化合物COMP可以藉由塗佈、浸漬、塗 覆、或上膠加壓施加。在藉由塗覆之典型的施加中,化合 物COMP之用量相對於所用之塗覆用懸浮液是0.2至2重量% ,該懸浮液可以含有無機塡料(諸如碳酸鈣、高嶺土、二 〇 氧化鈦)、及黏合劑(例如用於顏料之以苯乙烯-丁二烯 共聚物、丙烯酸系共聚物或含乙酸乙烯酯之共聚物爲底質 者)。在藉由上膠壓機中之紙上膠的典型應用中,化合物 COMP之用量相對紙係0.2至2重量%,係以水性懸浮液形式 被使用,該懸浮液係在20 °C至90 °C之溫度下饋於該上膠壓 機裝置之各滾筒間。可將其他添加劑(例如澱粉、官能化 澱粉、聚乙烯醇、羧甲基纖維素、三聚氰醯胺樹脂、脲甲 醛樹脂、含醛基之化合物、丙烯酸系樹脂、苯乙烯-丁二 烯共聚物)添加至懸浮液。通常添加消泡劑以改良機器之 •13- 201206972 運轉性。 依照在紙工業中所用之—般技術’可在9 0至13 0 °c範 圍內之溫度進行乾燥。 分散液DISP或溶液SOL也可以含有其他產物’諸如維 持、改良或改變紙之性質所需的已知添加劑’諸如以上所 述的。 據發現:具有至少一個陽離子基團的異氰酸酯反應性 氟化學聚醚在與多官能異氰酸酯反應時’使不含 PFOA/PFOS之氟化學化合物在用於紙上時顯出意外良好的 效能。此外,所得之聚合物具有良好之熱安定性。 【實施方式】 測試方法: KIT測試Rr〇-(CF(CF3)CF20)mCF(CF3)-CON(R1)-R2-OH (IVa) (Rr〇-(CF(CF3)CF20)mCF(CF3)-C〇N(R1)-R2 nN(R5)H (IVb) wherein Rf, R1, R2, m and n are as defined above and all preferred embodiments thereof, R5 is hydrogen (if η is 1) or an alkyl group having 1 to 4 carbon atoms .甚至 Even more preferably, the co-reactant C is a compound of the formula (IVb). Preferably, the total stoichiometry of the isocyanate-reactive groups of reactant A and co-reactant C is less than or equal to the total stoichiometry of the isocyanate groups of reactant B; more preferably, reactant A and co-reaction The total stoichiometry of the isocyanate-reactive group of the substance C is 0.8 to 1 times the total stoichiometric amount of the isocyanate group of the reactant B. In an even more preferred embodiment, the total stoichiometry of the isocyanate-reactive groups of reactant A and co-reactant C is from 0.9 to 1 times the total stoichiometric amount of the isocyanate group of reactant B. Preferably, the total chemistry of the isocyanate-reactive group of the co-reactant C-9 - 201206972 is 0 to times the total stoichiometry of the isocyanate-reactive group of the reactant A, more preferably 〇 to 7 times' Even better is 0 to 4 times 'even better, it is up to 1 time. If the total stoichiometry of the isocyanate-reactive groups of reactant A and co-reactant C is less than the total stoichiometry of the isocyanate groups of reactant B, then the excess isocyanate groups are preferably via self-polymerization or The reaction of the polyfunctional isocyanate-reactive compound (including water, polyol or polyamine) is further polymerized. Further, the subject of the present invention is a method for producing a compound COMP, which is characterized in that reactant B is reacted with reactant A and optionally co-reactant C, and reactants A, B and C have the meanings as described above. All preferred examples. Any order of addition can be used. Preferably, reactant A and co-reactant C are simultaneously added to reactant B. Preferably, the stoichiometry of reactants A, B and C has the same meaning as described above and all preferred embodiments thereof. Preferably, the reaction temperature is 〇 to 120 ° C and more preferably 20 to 8 ° C; more preferably, the pressure is between atmospheric pressure and 2 bar, and more preferably between atmospheric pressure and 1.2 bar. Preferably, the reaction time is from 1 minute to 48 hours, and more preferably from 1 minute to 6 hours. The reaction can be carried out in the presence or absence of a catalyst. Suitable catalyst for the absorption of guanamine; tin salts such as dibutyltin dilaurate, dibutyltin diacetate, dibutyltin di(2-ethylhexanoate), stannous octoate, stannous oleate, chlorinated -10-201206972 Tin; barium salts and others are known to those skilled in the art. Generally, the preferred concentration of the catalyst is from 0.001% by weight to 1% by weight, based on the total weight of the reactants, and preferably from 0.1% by weight to 5% by weight. Preferably, the reaction is carried out in the absence of any catalyst. In another preferred embodiment, the reaction is carried out in an aprotic solvent or aprotic solvent mixture. Preferred solvents are acetone, ethyl acetate, methyl isobutyl ketone, cyclohexanone, tetrahydrofuran, diethyl ether, tert-butyl methyl ether, hydrofluoroether (such as methoxy nonafluorobutane), trifluorotoluene, 1, 3-bis(trifluoromethyl)benzene and mixtures thereof. This reaction can be controlled, for example, by infrared (IR) spectrometry. Unreacted reactant B can be removed by washing COMP with a non-fluorinated organic solvent that does not dissolve COMP. A further subject of the invention is an aqueous dispersion of the compound COMP, DISP or solution SOL. Preferably, the dispersion DISP or solution SOL comprises 0.5 to 40% by weight of the Q compound COMP, more preferably 5 to 30% by weight, based on the total weight of the dispersion D I S P or the solution S Ο L. Therefore, the compound C Ο Μ P is preferably dispersed or dissolved in water. In addition to water, the dispersion or solution may or may not be present as a cosolvent. Preferably, the cosolvent can be slowly added to the reaction mixture' while any solvent used during the preparation of the compound COMP is distilled off' and the resulting product is neutralized with acid and then water is added. Preferably, the distillation of the solvent of the reaction is carried out under vacuum. -11 - 201206972 Preferably, the acid used for neutralization is selected from the group consisting of acetic acid and lactic acid, caproic acid, benzoic acid, caPrilic acid, citric acid, formic acid, sebacic acid, boric acid, and different Phthalic acid, itaconic acid, lauric acid, maleic acid, malic acid, oxalic acid, phosphoric acid, phthalic acid, pyromellitic acid, succinic acid, terephthalic acid, ascorbic acid, hypophosphorous acid, hydroquinone (propionic acid), acid extension, sodium hydrogen sulfate or terephthalic acid, valeric acid, p-hydroxybenzoic acid, resin acid and rosin acid, salicylic acid, sebacic acid. The cosolvent used in the dispersion or solution is preferably water soluble or at least partially water soluble, more preferably the cosolvent has at least one hydroxyl group, and even more preferably the cosolvent is a diol. In a preferred embodiment, the cosolvent is selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, tripropylene glycol, polypropylene glycol, hexanediol- Π, 6], hexanediol, polytetrahydrofuran, monoalkyl ethers of these diols, and mixtures of these solvents. Optionally, the compound COMP can be dispersed or dissolved in a cosolvent or a mixture which does not contain water, and the cosolvent is as defined above and all of its specific examples. Preferably, the temperature for the dispersion or for dissolution is 25 to 2 0 0 ° C, more preferably 25 to 150 ° C, still more preferably 25 to 100 ° C. Preferably, the reaction time for dispersion or dissolution is from 5 minutes to 6 hours. Another subject of the invention is that the use of the compound COMP is preferably in the form of a dispersion DISP or solution SOL for treating paper to make paper oil-proof. A further subject of the invention is a method of making paper' which is characterized in that -12-201206972 treats paper with compound COMP. Preferably, the paper is treated with the compound COMP in the form of dispersion DISP or solution SOL. Further, the present invention relates to a paper treated with a solution or dispersion containing the compound COMP. The compound COMP of the present invention can be used for paper sizing by using an application method known in the prior art. For example, it can be applied by surface treatment (gluing and/or coating) the formed paper.另一 Another method is the wet-end method, which is the application method in paper awards. For the application method, paper, paperboard, etc. are dispersed using a suitable medium (water or water and solvent mixture). DISP or solution S Ο L treatment. In the case of surface treatment, the compound COMP can be applied by coating, dipping, coating, or gluing. In a typical application by coating, the amount of compound COMP is from 0.2 to 2% by weight relative to the coating suspension used, and the suspension may contain inorganic tantalum (such as calcium carbonate, kaolin, titanium dioxide). And a binder (for example, a styrene-butadiene copolymer, an acrylic copolymer or a copolymer containing vinyl acetate as a substrate for the pigment). In a typical application of paper sizing by a press, the amount of compound COMP is from 0.2 to 2% by weight relative to the paper system and is used as an aqueous suspension at 20 ° C to 90 ° C. The temperature is fed between the rollers of the upper press device. Other additives (such as starch, functionalized starch, polyvinyl alcohol, carboxymethyl cellulose, melamine resin, urea formaldehyde resin, aldehyde group-containing compound, acrylic resin, styrene-butadiene copolymerization) ()) added to the suspension. Defoamers are usually added to improve the machine's 13-201206972 runnability. Drying can be carried out at a temperature in the range of 90 to 130 ° C according to the general technique used in the paper industry. The dispersion DISP or solution SOL may also contain other products such as known additives required to maintain, modify or modify the properties of the paper, such as those described above. It has been found that an isocyanate-reactive fluorochemical polyether having at least one cationic group, when reacted with a polyfunctional isocyanate, renders a fluorochemical compound free of PFOA/PFOS exhibiting unexpectedly good performance when applied to paper. In addition, the resulting polymer has good thermal stability. [Embodiment] Test method: KIT test
Kit測試是一種將紙之抗油脂性特徵化的程序。Kit測 試包含一邊評估一邊將編號1至16之測試溶液施加至樣品 。照著用於紙及紙板τ 55 9之Tappi測試方法之測試指導方 針進行測試。 當製成kit溶液時,對蓖蔴油進行重量測量,因爲其之 高黏度使體積測量較不準確。 -14- 201206972The Kit test is a procedure that characterizes the anti-grease properties of paper. The Kit test involves applying the test solutions Nos. 1 to 16 to the sample while evaluating. Tested according to the test instructions for the Tappi test method for paper and paperboard τ 55 9 . When making a kit solution, the castor oil is weighed because its high viscosity makes the volume measurement less accurate. -14- 201206972
編號 麵油 甲苯 正赚 升] 酬 mm 1 96.90/100 0 0 2 87.21/90 5 5 3 77.52/80 10 10 4 67.83 / 70 15 15 5 58.14/60 20 20 6 48.45/50 25 25 7 38.76() 40 30 30 8 29.07/30 35 35 9 19.38/20 40 40 10 9.69/10 45 45 11 0 50 50 12 0 45 55 13 0 35 65 14 0 25 75 15 0 15 85 16 0 0 100 在一良好照明之煙廚中,使用暗板進行ut測試以顯示 滲透作爲較暗之點。 1 )將每一測試樣品放置在所選之必須乾淨、乾燥、 測試面向上之表面上。 2 )選擇中間編號的Kit測試溶液且小心地在不使樣品 接觸滴管下施加成約2公分長之條紋狀至樣品且開 始計時。 -15- 201206972 3 )在1 5秒之後,快速地利用清潔的薄紙移除過多之 測試溶液,施加最小之壓力至該紙表面,且立即 檢查該測試區。 不合格係由測試樣品之變暗指明,若使用暗的背 景;或由明亮光點指明,若使用光盒。 顏色之改變係因樣品受潮,因測試溶液滲入該紙 片。 若測試區沒有立即檢查,則測試溶液之揮發成份 的蒸發將發生且樣品可以再次獲得其原初外觀且 評爲合格。 4 )若樣品沒有通過此第一測試,則選擇該片之未受 測試的區且使用較低編號之溶液重複測試。 重複測試直至確定最高編號的Kit溶液,其停置在 表面上15秒且不引起不合格。 5 )若樣品通過此第一測試,則使用較高編號之Kit溶 液對樣品之未受測試區重複測試。 重複測試直至確定最高編號的Kit溶液,其停置在 表面上I5秒且不引起不合格。 合格之最高編號的kit溶液是該樣品之kit等級。 此測試應至少進行二次。 吸油測試 使用伸幅器切割1 5公分X 1 5公分之正方形紙樣品。測 試樣品被調節(2 3 t / 5 0 %相對溼度)且在天平上秤重, 201206972 紀錄重量以供測試完成後計算吸油量。將測試用油分散於 測量用圓筒中’此測試需要7至8毫升之量。油快速地倒在 測試樣品表面上成1 0公分X 1 〇公分之大約螺旋/正方圖 形。在此之後’立即將12公分X 12公分之濾紙放置在油 上’以致將油完全蓋住。油立即滲入濾紙,且快速擴散以 致整個12公分X 12公分的測試面積完全與油接觸。同時 開始計時。 測試進行1 0分鐘。然後’將濾紙由測試樣品移除,在 此之後,在測試樣品上之殘留的油立即被擦拭,然後,使 用吸收性薄紙擦掉直至樣品表面無油。樣品在測試後再次 秤重且油之重力吸油量被計算一此稱爲“玉米油吸收度”: 玉繼收度 ΟNo. Face oil toluene is making a rise] Reward mm 1 96.90/100 0 0 2 87.21/90 5 5 3 77.52/80 10 10 4 67.83 / 70 15 15 5 58.14/60 20 20 6 48.45/50 25 25 7 38.76() 40 30 30 8 29.07/30 35 35 9 19.38/20 40 40 10 9.69/10 45 45 11 0 50 50 12 0 45 55 13 0 35 65 14 0 25 75 15 0 15 85 16 0 0 100 In a good lighting In the smoke cooker, a dark plate was used for the ut test to show the penetration as a darker point. 1) Place each test sample on the surface of the selected clean, dry, test-facing surface. 2) Select the middle numbered Kit test solution and carefully apply a stripe of about 2 cm length to the sample without starting the sample contact dropper and start timing. -15- 201206972 3 ) After 15 seconds, quickly remove excess test solution with clean tissue, apply minimal pressure to the paper surface, and immediately inspect the test area. The failure is indicated by the darkening of the test sample, if a dark background is used; or by a bright spot, if a light box is used. The change in color is due to moisture in the sample as the test solution penetrates into the paper. If the test area is not immediately inspected, evaporation of the volatile components of the test solution will occur and the sample will again obtain its original appearance and be rated as acceptable. 4) If the sample does not pass this first test, select the untested area of the piece and repeat the test using the lower numbered solution. The test was repeated until the highest numbered Kit solution was determined, which was placed on the surface for 15 seconds and did not cause a failure. 5) If the sample passes this first test, repeat the test for the untested area of the sample using the higher numbered Kit solution. The test was repeated until the highest numbered Kit solution was determined, which was placed on the surface for 1 5 seconds without causing a failure. The highest rated kit solution that is qualified is the kit grade of the sample. This test should be performed at least twice. Oil absorption test Use a stretcher to cut a sample of 1 5 cm X 1 5 cm square paper. The test sample is adjusted (2 3 t / 50% relative humidity) and weighed on the balance. 201206972 Record the weight for the oil absorption after the test is completed. Disperse the test oil in the measuring cylinder. This test requires 7 to 8 ml. The oil quickly fell on the surface of the test sample to an approximately spiral/square pattern of 10 cm x 1 cm. Immediately thereafter, '12 cm X 12 cm filter paper was placed on the oil' so that the oil was completely covered. The oil immediately penetrates the filter paper and spreads rapidly so that the entire 12 cm x 12 cm test area is completely in contact with the oil. At the same time, start timing. The test was carried out for 10 minutes. The filter paper is then removed from the test sample, after which the residual oil on the test sample is immediately wiped and then wiped off with absorbent tissue until the sample surface is free of oil. The sample is weighed again after the test and the gravity of the oil is calculated. This is called “corn oil absorption”: Jade is collected Ο
Wl=測試前之樣品重量 W2 =測試後之樣品重量 s=與油接觸之表面積 所得之玉米油吸收値以克/平方公尺之形式報告。可 以重複測試以確定獲得統計上有意義的結果。 所用材料之列述: B1:聚(二異氰酸伸己酯),Isocyanurate,193克/ NC0 B2:聚(二異氰酸伸己酯),Uretdion,193克/ NC0 B3 :聚(二異氰酸伸己酯),Isocyanurate,195.5 克 / NC0 -17- 201206972Wl = sample weight before test W2 = sample weight after test s = surface area in contact with oil The resulting corn oil absorption is reported in grams per square meter. Tests can be repeated to determine statistically meaningful results. List of materials used: B1: poly(dihexyl isocyanate), Isocyanurate, 193 g / NC0 B2: poly(diisocyanato), Uretdion, 193 g / NC0 B3: poly (diiso) Cetylhexanoate), Isocyanurate, 195.5 g / NC0 -17- 201206972
El : CF3CF2CF2O(CF(CF3)CF20)nCF(CF3)C0OCH3 ,其係依照WO/2009/ 1 1 83 48製備,Mw 1 947克/莫耳,不 含具有少於1000克/莫耳之Mw的寡聚物。 E2 : CF3CF2CF2〇(CF(CF3)CF20)nCF(CF3)COOCH3 ,其係依照WO/2009/ 1 1 8348製備,Mw 1971克/莫耳,不 含具有少於1000克/莫耳之Mw的寡聚物。 E3 : CF3CF2CF20(CF(CF3)CF20)nCF(CF3)C00CH3 ,其係依照WO/2009/ 1 1 8348製備,Mw 1 905克/莫耳,不 含具有少於1 000克/莫耳之Mw的寡聚物。 E4 : CF3CF2CF20(CF(CF3)CF20)nCF(CF3)C00CH3 ,其係依照WO/2009/ 1 1 8348製備,Mw 1871克/莫耳,不 含具有少於1 000克/莫耳之Mw的寡聚物。 DMAPAPA : H2NCH2CH2CH2NHCH2CH2CH2N(CH3)2 MAPA : H2NCH2CH2CH2NHCH3 DETA : H2NCH2CH2NHCH2CH2NH2 TBME :第三丁基甲基醚 BTFMB : 1,3-雙(三氟甲基)苯 MNFB :甲氧基九氟丁烷 PRG :丙二醇 A c Ο Η :酸性酸 A 1之製備 19 4.7克之E1裝塡於配備溫度計、機械攪拌器及真空 蒸餾裝置之玻璃反應器中且冷卻至-1CTC 。將16.0克之 -18- 201206972 DMAPAPA在攪拌下緩慢地添加且保持在-10°C -〇°C之溫度 下。然後混合物另外攪拌過夜。所得之甲醇在真空下移除 以獲得A 1。 A3之製備 由40.00克之E3及3.36克之DMAPAPA開始,依照在A1 之製備中所述之方法製備A3。 〇 C 1之製備 由194.7克之丑1及8.86克之厘八?八開始,依照在入1之製 備中所述之方法製備C1。 C3之製備 由187.1克之E4及5.17克之DETA開始,依照在A1之製 備中所述之方法製備C3。 ❹ A1/C1混合物1之製備 由 58_41 克之 E1、3.200 克之 DMAPAPA 及 0.8 8 6 克之 MAPA開始,依照在A1之製備中所述之方法製備A1/C1混 合物1。 A2/C2混合物1之製備 由 40.00 克之 E2、2.32 克之 DMAPAPA 及 0.51 克之 MAPA 開始,依照在A1之製備中所述之方法製備A2/C2混合物1。 -19- 201206972 A2/C2混合物2之製備 由 40.00 克之 E2、2.05克之DMAPAPA及0·67之MAPA開 始,依照在A1之製備中所述之方法製備AhC2混合物2。 COMP1之製備 12.11克之B1裝塡於配備溫度計、機械攪拌器及真空 蒸餾裝置之玻璃反應器中且利用由70克之TBME及27克之 BTFMB組成之溶劑混合物稀釋。在攪拌下添加83.00克之 A1及40.22克之C1的混合物。混合物在25 °C下攪拌過夜, 然後在56-6 5 °C下加熱以移除TBME,直至使混合物增稠成 爲具有約20%之BTFMB含量之COMP1糊膏,其將直接用於 從42.18克之八2/(:2混合物開始之〇13?1的製備。然後5克之 所得的COMP1糊膏在40 °C /50毫巴下乾燥24小時以獲得 COMP1。COMP1之DSC分析顯示無放熱直至250。。。 COMP2之製備 由42.18克之人2/(:2混合物1及4.07克之81開始,依照 COMP1之製備中所述的方法製備具有約20 %之BTFMB含量 的COMP2糊膏。COMP2糊膏將直接用於製備DISP3。約1克 之所得的COMP2糊膏在40 °C /50毫巴下乾燥24小時以獲得 COMP2。COMP2之DSC分析顯示無放熱直至25〇°C。 COMP3之製備 -20 - 201206972 由42.0克之A2/C2混合物2及4.07克之B1開始,依照 COMP1之製備中所述的方法製備具有約20%之BTFMB含量 的COMP3糊膏。COMP3糊膏將直接用於製備DISP4。約1克 之所得的COMP3糊膏在40 °C /50毫巴下乾燥24小時以獲得 COMP3。COMP3之DSC分析顯示無放熱直至250°C。 COMP4之製備 0 由22.84克之人1、11.26克之(:1及3.34克之82開始,依 照COMP 1之製備中所述的方法製備具有約2 0%之BTFMB含 量的COMP4糊膏。COMP4糊膏將直接用於製備DISP5。約1 克之所得的COMP4糊膏在40°C /50毫巴下乾燥24小時以獲 得COMP4。COMP4之DSC分析顯示無放熱直至250°C。 COMP5之製備 由42.7克之A3及3.34克之B3開始,依照COMP1之製備 Q 中所述的方法製備具有約1 5%之BTFMB含量的COMP5糊膏 。COMP5糊膏將直接用於製備DISP6。約1克之所得的 COMP5糊膏在40°C /50毫巴下乾燥24小時以獲得COMP5。 COMP5之DSC分析顯示無放熱直至250°C。 COMP6之製備 由32.25克之A3、15克之C3及4.03克之B3開始,依照 COMP1之製備中所述的方法製備具有約25%之TBME含量 的COMP6糊膏。COMP6糊膏將直接用於製備DISP6。約1克 -21 - 201206972 之所得的COMP5糊膏在4(TC /50毫巴下乾燥24小時以獲得 COMP5。COMP5之DSC分析顯示無放熱直至250°C。 DISP1之製備 42.5克之COMP1糊膏放置於配備溫度計、機械攪拌器 及真空蒸餾裝置之玻璃反應器中。混合物加熱至1 〇〇 °C。 0.5克之AcOH在攪拌下被添加,接著在約1小時期間緩慢添 加51克之PRG,同時殘留之BTFMB在100°C /800-50毫巴下 移除。然後停止加熱且添加0.4克之AcOH,接著逐滴添加 1 1 4克之蒸餾水。在結束水之添加時,混合物進一步冷卻 至25它。然後,卩11利用人£:011調節至4.5以獲得013?1。 DISP2之製備 61.5克之A1/C1混合物1利用60克之MNFB稀釋。6·02 克之B1在攪拌下被添加。混合物在25 °C下攪拌過夜,然後 迴流4小時。添加0.9克之AcOH,接著在約1小時期間緩慢 添加92.3克之PRG,同時蒸餾NFB。最後,殘留之MNFB在 100°C /800-200毫巴下移除。然後停止加熱且添加0.76克之 AcOH,接著逐滴添加206克之蒸餾水。在結束水之添加時 ,混合物進一步冷卻至25 t。然後,pH利用AcOH調節至 4.5以獲得018卩2。 DISP3之製備 由56.8克之COMP2糊膏開始,依照DISP1之製備中所 -22- 201206972 述之方法製備DISP3。 DISP4之製備 由56.8克之COMP3糊膏開始,依照DISP1之製備中所 述之方法製備DISP4。 DISP5之製備 由45.8克之COMP4糊膏開始,依照DISP1之製備中所 述之方法製備DISP5。 DISP6之製備 由27.63克之COMP5糊膏開始,依照DISP1之製備中所 述之方法製備DISP6。 由56克之COMP5糊膏開始,依照DISP1之製備中所述 之方法製備DISP7。 〇 應用實例 在100 °C下製備16 %之澱粉TCF 07311的水溶液15分鐘 ,然後冷卻至75°C。1克、2克、3克及4克之分散液DISP分 別稀釋成50克且添加50克之16%的澱粉溶液以獲得應用液 。紙樣品(68克/平方公尺)在Mathis Typ HFP 56700上 膠壓機上在3巴/10公尺/分鐘下處理,然後在95°C之 Schroeter乾燥機上乾燥2分鐘。基於濕的吸收量及DISP濃 度計算化合物C Ο Μ P之吸收量。使乾燥的紙被調節,然後 -23- 201206972 依照所述之Kit測試,使用用於紙及 Tappi測試方法,依照所述之Kit測試 Kit等級。測試結果摘述於下表中。 板T5 5 9之抗油脂性 依照吸油性,測量 -24- 201206972El: CF3CF2CF2O(CF(CF3)CF20)nCF(CF3)COOCH3, prepared according to WO/2009/1 1 83 48, Mw 1 947 g/mole, free of Mw having less than 1000 g/mole Oligomer. E2: CF3CF2CF2 〇 (CF(CF3)CF20)nCF(CF3)COOCH3, prepared according to WO/2009/1 1 8348, Mw 1971 g/mole, excluding oligo with Mw less than 1000 g/mole Polymer. E3: CF3CF2CF20(CF(CF3)CF20)nCF(CF3)C00CH3, prepared according to WO/2009/1 1 8348, Mw 1 905 g/mole, without Mw having less than 1 000 g/mole Oligomer. E4: CF3CF2CF20(CF(CF3)CF20)nCF(CF3)C00CH3, prepared according to WO/2009/1 1 8348, Mw 1871 g/mole, excluding oligo with Mw less than 1 000 g/mole Polymer. DMAPAPA : H2NCH2CH2CH2NHCH2CH2CH2N(CH3)2 MAPA : H2NCH2CH2CH2NHCH3 DETA : H2NCH2CH2NHCH2CH2NH2 TBME : Third butyl methyl ether BTFMB : 1,3-bis(trifluoromethyl)benzene MNFB : methoxy nonafluorobutane PRG : propylene glycol A c Ο Η : Preparation of Acidic Acid A 1 19 4.7 g of E1 was mounted in a glass reactor equipped with a thermometer, mechanical stirrer and vacuum distillation apparatus and cooled to -1 CTC. 16.0 g of -18-201206972 DMAPAPA was slowly added with stirring and maintained at a temperature of -10 °C - 〇 °C. The mixture was then stirred overnight. The resulting methanol was removed under vacuum to obtain A1. Preparation of A3 Starting from 40.00 grams of E3 and 3.36 grams of DMAPAPA, A3 was prepared according to the procedure described in the preparation of A1. 〇 Preparation of C 1 From 194.7 grams of ugly 1 and 8.86 grams of 8%? At the beginning of eight, C1 was prepared in accordance with the method described in Preparation of Into. Preparation of C3 Starting from 187.1 g of E4 and 5.17 g of DETA, C3 was prepared according to the method described in the preparation of A1. Preparation of ❹ A1/C1 Mix 1 Starting from 58_41 g of E1, 3.200 g of DMAPAPA and 0.886 g of MAPA, A1/C1 Blend 1 was prepared according to the procedure described in the preparation of A1. Preparation of A2/C2 Mixture 1 Starting from 40.00 grams of E2, 2.32 grams of DMAPAPA and 0.51 grams of MAPA, the A2/C2 mixture 1 was prepared according to the procedure described in the preparation of A1. -19- 201206972 Preparation of A2/C2 Mixture 2 Starting from 40.00 g of E2, 2.05 g of DMAPAPA and MAPA of 0.66, the AhC2 mixture 2 was prepared according to the method described in the preparation of A1. Preparation of COMP1 12.11 g of B1 was mounted in a glass reactor equipped with a thermometer, a mechanical stirrer and a vacuum distillation apparatus and diluted with a solvent mixture consisting of 70 g of TBME and 27 g of BTFMB. A mixture of 83.00 grams of A1 and 40.22 grams of C1 was added with stirring. The mixture was stirred at 25 ° C overnight and then heated at 56-6 5 ° C to remove TBME until the mixture thickened to a COMP1 paste with a BTFMB content of about 20%, which would be used directly from 42.18 grams. Eight 2/(:2 Preparation of the mixture starting at 13?1. Then 5 grams of the resulting COMP1 paste was dried at 40 °C / 50 mbar for 24 hours to obtain COMP1. DSC analysis of COMP1 showed no exotherm up to 250. The preparation of COMP2 was started by 42.18 g of human 2/(: 2 mixture 1 and 4.07 g of 81, and a COMP2 paste having a BTFMB content of about 20% was prepared according to the method described in the preparation of COMP1. The COMP2 paste was used directly. For the preparation of DISP3, about 1 gram of the obtained COMP2 paste was dried at 40 ° C / 50 mbar for 24 hours to obtain COMP 2. The DSC analysis of COMP 2 showed no exotherm up to 25 ° C. Preparation of COMP 3 - 201206972 by 42.0 Starting with A2/C2 mixture 2 and 4.07 g of B1, a COMP3 paste having a BTFMB content of about 20% was prepared according to the method described in the preparation of COMP 1. The COMP3 paste was directly used to prepare DISP4. About 1 gram of the obtained COMP3 The paste is dried at 40 ° C / 50 mbar for 24 hours to obtain DSC analysis of COMP3.COMP3 showed no exotherm up to 250 ° C. Preparation of COMP4 0 Starting from 22.84 g of human 1, 11.26 g (: 1 and 3.34 g of 82, prepared according to the method described in the preparation of COMP 1 with approximately 20 % BTFMB content of COMP4 paste. COMP4 paste will be used directly to prepare DISP5. About 1 gram of the resulting COMP4 paste is dried at 40 ° C / 50 mbar for 24 hours to obtain COMP4. DSC analysis of COMP4 shows no exotherm Up to 250 ° C. Preparation of COMP5 Starting from 42.7 g of A3 and 3.34 g of B3, COMP5 paste with a BTFMB content of about 1 5% was prepared according to the method described in Preparation Q of COMP 1. COMP5 paste was used directly for preparation. DISP6. About 1 gram of the resulting COMP5 paste was dried at 40 ° C / 50 mbar for 24 hours to obtain COMP 5. The DSC analysis of COMP5 showed no exotherm up to 250 ° C. The preparation of COMP6 consisted of 32.25 g of A3, 15 g of C3 and Starting with 4.03 grams of B3, a COMP6 paste having a TBME content of about 25% was prepared according to the method described in the preparation of COMP 1. The COMP6 paste was directly used to prepare DISP6. The resulting COMP5 paste of about 1 gram - 21 - 201206972 Dry at 4 (TC / 50 mbar for 24 hours) Was COMP5. DSC analysis of COMP5 showed no exotherm up to 250 °C. Preparation of DISP1 42.5 grams of COMP1 paste was placed in a glass reactor equipped with a thermometer, mechanical stirrer and vacuum distillation unit. The mixture is heated to 1 〇〇 °C. 0.5 g of AcOH was added with stirring, followed by a slow addition of 51 g of PRG over a period of about 1 hour, while residual BTFMB was removed at 100 ° C / 800-50 mbar. Heating was then stopped and 0.4 g of AcOH was added, followed by dropwise addition of 141 g of distilled water. At the end of the addition of water, the mixture was further cooled to 25 it. Then, 卩11 is adjusted to 4.5 by the person £:011 to obtain 013?1. Preparation of DISP2 61.5 grams of A1/C1 Mix 1 was diluted with 60 grams of MNFB. 6·02 gram of B1 was added under stirring. The mixture was stirred at 25 ° C overnight and then refluxed for 4 hours. 0.9 g of AcOH was added, followed by the slow addition of 92.3 g of PRG over about 1 hour while distilling NFB. Finally, the residual MNFB is removed at 100 ° C / 800-200 mbar. Heating was then stopped and 0.76 grams of AcOH was added, followed by the dropwise addition of 206 grams of distilled water. At the end of the addition of water, the mixture was further cooled to 25 t. Then, the pH was adjusted to 4.5 with AcOH to obtain 018 卩2. Preparation of DISP3 Starting from 56.8 grams of COMP2 paste, DISP3 was prepared according to the method described in the preparation of DISP1, -22-201206972. Preparation of DISP4 DISP4 was prepared according to the procedure described in the preparation of DISP1 starting with 56.8 grams of COMP3 paste. Preparation of DISP5 Starting from 45.8 grams of COMP4 paste, DISP5 was prepared according to the method described in the preparation of DISP1. Preparation of DISP6 DISP6 was prepared according to the method described in the preparation of DISP1 starting with 27.63 grams of COMP5 paste. Starting with 56 grams of COMP5 paste, DISP7 was prepared as described in the preparation of DISP1. 〇 Application Example An aqueous solution of 16% starch TCF 07311 was prepared at 100 °C for 15 minutes and then cooled to 75 °C. The dispersions of 1 g, 2 g, 3 g and 4 g of DISP were diluted to 50 g and 50 g of a 16% starch solution was added to obtain an application liquid. Paper samples (68 g/m2) were processed on a Mathis Typ HFP 56700 press at 3 bar/10 m/min and then dried on a 95 °C Schroeter dryer for 2 minutes. The absorption of the compound C Ο Μ P was calculated based on the wet absorption amount and the DISP concentration. The dried paper is adjusted, then -23-201206972 according to the Kit test described, using the paper and Tappi test methods, according to the Kit test Kit rating. The test results are summarized in the table below. Resistance to grease of plate T5 5 9 According to oil absorption, measurement -24- 201206972
應用實例編號 平均吸收量 平均Kit等級 吸油度 (測試之DISP編號) [克/平方公尺] [克/平方公尺] 應用實例1 0.057 4 2 (DISP1) 0.116 7 4 0.170 10 4 0.220 13 2 應用實例2 0.055 3 2 (DISP2) 0.118 7 6 0.172 11 4 0.226 14 4 應用實例3 0.071 3 7 (DISP3) 0.134 7 2 0.213 10 3 0.305 13 3 應用實例4 0.060 4 13 (DISP4) 0.103 5 4 0.158 11 3 0.217 14 3 應用實例5 0.071 3 5 (DISP5) 0.149 8 3 0.213 1114 3 0.272 3 應用實例6 0.057 3 7 (DISP6) 0.114 5 2 0.168 9 1 0.221 10 1 應用實例7 0.056 0 5 (DISP7) 0.114 5 2 0.168 9 1 0.222 11 1 -25-Application example number Average absorption average Kit grade oil absorption (tested DISP number) [g/m2] [g/m2] Application example 1 0.057 4 2 (DISP1) 0.116 7 4 0.170 10 4 0.220 13 2 Application Example 2 0.055 3 2 (DISP2) 0.118 7 6 0.172 11 4 0.226 14 4 Application Example 3 0.071 3 7 (DISP3) 0.134 7 2 0.213 10 3 0.305 13 3 Application Example 4 0.060 4 13 (DISP4) 0.103 5 4 0.158 11 3 0.217 14 3 Application example 5 0.071 3 5 (DISP5) 0.149 8 3 0.213 1114 3 0.272 3 Application example 6 0.057 3 7 (DISP6) 0.114 5 2 0.168 9 1 0.221 10 1 Application example 7 0.056 0 5 (DISP7) 0.114 5 2 0.168 9 1 0.222 11 1 -25-
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