CN1727377A - Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene - Google Patents

Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene Download PDF

Info

Publication number
CN1727377A
CN1727377A CN 200510043018 CN200510043018A CN1727377A CN 1727377 A CN1727377 A CN 1727377A CN 200510043018 CN200510043018 CN 200510043018 CN 200510043018 A CN200510043018 A CN 200510043018A CN 1727377 A CN1727377 A CN 1727377A
Authority
CN
China
Prior art keywords
reactor
alkyl ketene
mass ratio
reaction
ketene dimer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN 200510043018
Other languages
Chinese (zh)
Other versions
CN1298760C (en
Inventor
沈一丁
李刚辉
费贵强
李小瑞
王海花
任庆海
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shaanxi University of Science and Technology
Original Assignee
Shaanxi University of Science and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shaanxi University of Science and Technology filed Critical Shaanxi University of Science and Technology
Priority to CNB2005100430180A priority Critical patent/CN1298760C/en
Publication of CN1727377A publication Critical patent/CN1727377A/en
Application granted granted Critical
Publication of CN1298760C publication Critical patent/CN1298760C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Polyurethanes Or Polyureas (AREA)

Abstract

A process for preparing the composite cationic polyurethane/alkylketene bipolymer emulsion includes such steps as adding alkylketene bipolymer to dried reactor, heating for fusing it, adding toluene diisocyanate, polydiol and dibutyltin laurate to the reactor, polycondensating reaction to obtain alkylketene bipolymer solution, adding N-methyl diethanolamine, chain extending reaction, adding dimethyl sulfate, quatenary ammoniating reaction, adding glacic acetic acid to make pH=4.5-6.5, and adding deionized water.

Description

The preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene
Technical field
The invention belongs to fine chemicals preparation technology field, particularly a kind of preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene.
Background technology
Be widely used owing to polyaminoester emulsion has good physical and chemical performance, but in its preparation process, need to use a large amount of organic solvents and emulsifying agent, staff, environment and effect are had a negative impact.Alkyl ketene dimer has long fat hydrocarbon chain (C 14~16) and quaternary lactonic ring, be lyophobic dust, be commonly used for the paper sizing agent after it is emulsified, but contain a large amount of emulsifying agents equally in the alkyl ketene dimer emulsion, all unfavorable to handling papermaking wastewater and effect, especially to the sizing efficiency of paper.
Summary of the invention
The objective of the invention is to overcome the shortcoming of above-mentioned prior art, provide a kind of and can improve the product application effect, simultaneously the preparation method of the compound emulsion of dimmer of cation polyurethane and alkyl ketene that can not pollute and damage environment and operator.
For achieving the above object, the technical solution used in the present invention is: at first by mass ratio 6.83~10.65% alkyl ketene dimers are joined in the dry reactor, and reactor is heated to 75~90 ℃, after making the alkyl ketene dimer fusion in the reactor, and then by mass ratio the dibutyl tin laurate of 25.63%~30% tolylene diisocyanate, 40~51.26% polyglycol and 0.40~0.47% is joined in the reactor and to carry out polycondensation 1.0~2.5 hours at 75~90 ℃, form the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 12.82~15.77% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 55~70 ℃, and the reaction times is 0.5~1.5 hour; Be that 3.0~5.0% methyl-sulfates join and carry out quaterisation in the reactor again with mass ratio, temperature of reaction is between 65~80 ℃, and the time is 1.0~2.0 hours; Add glacial acetic acid at last and regulate after pH value is 4.5~6.5, stir that to add temperature down be 20-90 ℃ deionized water, get solids content and be 25% white emulsion.
Polyglycol of the present invention is polyether Glycols or polyester diol, and polyether Glycols and polyester diol number average relative molecular mass are respectively 1000 or 2000.
The present invention carries out the fused alkyl ketene dimer building-up reactions of cation polyurethane as organic solvent, not only eliminated the organic solvent that needs in the polyurethane preparation process, and do not need to add emulsifying agent in the whole preparation process, so both eliminated pollution and infringement, also improved the effect of product environment and operator; Simultaneously, the product that can obtain expecting by the kind of regulating polyglycol.
Embodiment
Embodiment 1, at first 6.83% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 90 ℃, after making the alkyl ketene dimer fusion in the reactor, adding 30% tolylene diisocyanate, 44.88% relative molecular mass by mass ratio again is that the dibutyl tin laurate of 1000 polyether Glycols and 0.47% joins in the reactor and carried out polycondensation 1.0 hours at 90 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 12.82% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 55 ℃, and the reaction times is 0.5 hour; Be that 5% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 65 ℃, and the time is 1.0 hours; Add glacial acetic acid at last and regulate after pH value is 4.5, stir that to add temperature down be 20 ℃ deionized water, get solids content and be 25% white emulsion.
Embodiment 2, at first 10.65% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 75 ℃, after making the alkyl ketene dimer fusion in the reactor, adding 25.63% tolylene diisocyanate, 44.55% relative molecular mass by mass ratio again is that the dibutyl tin laurate of 2000 polyether Glycols and 0.40% joins in the reactor and carried out polycondensation 1.8 hours at 75 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 15.77% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 60 ℃, and the reaction times is 1.5 hours; Be that 3% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 80 ℃, and the time is 1.2 hours; Add glacial acetic acid at last and regulate after pH value is 6.0, stir that to add temperature down be 90 ℃ deionized water, get solids content and be 25% white emulsion.
Embodiment 3, at first 10% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 80 ℃, after making the alkyl ketene dimer fusion in the reactor, adding 30% tolylene diisocyanate, 40% relative molecular mass by mass ratio again is that the dibutyl tin laurate of 1000 polyester binary pure and mild 0.45% joins in the reactor and carried out polycondensation 2.3 hours at 80 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 15.55% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 65 ℃, and the reaction times is 0.8 hour; Be that 4% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 76 ℃, and the time is 1.8 hours; Add glacial acetic acid at last and regulate after pH value is 5.0, stir that to add temperature down be 60 ℃ deionized water, get solids content and be 25% white emulsion.
Embodiment 4, at first 7% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 85 ℃, after making the alkyl ketene dimer fusion in the reactor, adding 25% tolylene diisocyanate, 51.26% relative molecular mass by mass ratio again is that the dibutyl tin laurate of 2000 polyester binary pure and mild 0.46% joins in the reactor and carried out polycondensation 1.5 hours at 85 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 13.28% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 70 ℃, and the reaction times is 1.2 hours; Be that 3% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 72 ℃, and the time is 1.6 hours; Add glacial acetic acid at last and regulate after pH value is 5.5, stir that to add temperature down be 40 ℃ deionized water, get solids content and be 25% white emulsion.
Embodiment 5, at first 8% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 83 ℃, after making the alkyl ketene dimer fusion in the reactor, adding 28% tolylene diisocyanate, 46% relative molecular mass by mass ratio again is that the dibutyl tin laurate of 1000 polyether Glycols and 0.42% joins in the reactor and carried out polycondensation 1.2 hours at 83 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 13.58% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 67 ℃, and the reaction times is 1.0 hours; Be that 4% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 75 ℃, and the time is 1.5 hours; Add glacial acetic acid at last and regulate after pH value is 6.5, stir that to add temperature down be 80 ℃ deionized water, get solids content and be 25% white emulsion.
Embodiment 6, at first 9% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 78 ℃, after making the alkyl ketene dimer fusion in the reactor, adding 26% tolylene diisocyanate, 48% relative molecular mass by mass ratio again is that the dibutyl tin laurate of 2000 polyester binary pure and mild 0.43% joins in the reactor and carried out polycondensation 2.5 hours at 78 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 13.57% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 58 ℃, and the reaction times is 1.4 hours; Be that 3% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 68 ℃, and the time is 2.0 hours; Add glacial acetic acid at last and regulate after pH value is 5.7, stir that to add temperature down be 50 ℃ deionized water, get solids content and be 25% white emulsion.

Claims (8)

1, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene is characterized in that:
1) at first 6.83~10.65% alkyl ketene dimers is joined in the dry reactor by mass ratio, and reactor is heated to 75~90 ℃, after making the alkyl ketene dimer fusion in the reactor, and then by mass ratio the dibutyl tin laurate of 25.63%~30% tolylene diisocyanate, 40~51.26% polyglycol and 0.40~0.47% is joined in the reactor and to carry out polycondensation 1.0~2.5 hours at 75~90 ℃, form the alkyl ketene dimer solution of base polyurethane prepolymer for use as;
2) be that 12.82~15.77% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution with mass ratio, temperature of reaction is 55~70 ℃, and the reaction times is 0.5~1.5 hour;
3) be that 3.0~5.0% methyl-sulfates join and carry out quaterisation in the reactor again with mass ratio, temperature of reaction is between 65~80 ℃, and the time is 1.0~2.0 hours;
4) add glacial acetic acid at last and regulate after pH value is 4.5~6.5, stir that to add temperature down be 20-90 ℃ deionized water, get solids content and be 25% white emulsion.
2, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: said polyglycol is polyether Glycols or polyester diol, and polyether Glycols and polyester diol number average relative molecular mass are respectively 1000 or 2000.
3, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: at first 6.83% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 90 ℃, after making the alkyl ketene dimer fusion in the reactor, press the tolylene diisocyanate of mass ratio adding 30% again, 44.88% relative molecular mass is that the dibutyl tin laurate of 1000 polyether Glycols and 0.47% joins in the reactor and carried out polycondensation 1.0 hours at 90 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 12.82% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 55 ℃, and the reaction times is 0.5 hour; Be that 5% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 65 ℃, and the time is 1.0 hours; Add glacial acetic acid at last and regulate after pH value is 4.5, stir that to add temperature down be 20 ℃ deionized water, get solids content and be 25% white emulsion.
4, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: at first 10.65% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 75 ℃, after making the alkyl ketene dimer fusion in the reactor, press the tolylene diisocyanate of mass ratio adding 25.63% again, 44.55% relative molecular mass is that the dibutyl tin laurate of 2000 polyether Glycols and 0.40% joins in the reactor and carried out polycondensation 1.8 hours at 75 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 15.77% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 60 ℃, and the reaction times is 1.5 hours; Be that 3% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 80 ℃, and the time is 1.2 hours; Add glacial acetic acid at last and regulate after pH value is 6.0, stir that to add temperature down be 90 ℃ deionized water, get solids content and be 25% white emulsion.
5, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: at first 10% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 80 ℃, after making the alkyl ketene dimer fusion in the reactor, press the tolylene diisocyanate of mass ratio adding 30% again, 40% relative molecular mass is that the dibutyl tin laurate of 1000 polyester binary pure and mild 0.45% joins in the reactor and carried out polycondensation 2.3 hours at 80 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 15.55% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 65 ℃, and the reaction times is 0.8 hour; Be that 4% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 76 ℃, and the time is 1.8 hours; Add glacial acetic acid at last and regulate after pH value is 5.0, stir that to add temperature down be 60 ℃ deionized water, get solids content and be 25% white emulsion.
6, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: at first 7% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 85 ℃, after making the alkyl ketene dimer fusion in the reactor, press the tolylene diisocyanate of mass ratio adding 25% again, 51.26% relative molecular mass is that the dibutyl tin laurate of 2000 polyester binary pure and mild 0.46% joins in the reactor and carried out polycondensation 1.5 hours at 85 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 13.28% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 70 ℃, and the reaction times is 1.2 hours; Be that 3% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 72 ℃, and the time is 1.6 hours; Add glacial acetic acid at last and regulate after pH value is 5.5, stir that to add temperature down be 40 ℃ deionized water, get solids content and be 25% white emulsion.
7, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: at first 8% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 83 ℃, after making the alkyl ketene dimer fusion in the reactor, press the tolylene diisocyanate of mass ratio adding 28% again, 46% relative molecular mass is that the dibutyl tin laurate of 1000 polyether Glycols and 0.42% joins in the reactor and carried out polycondensation 1.2 hours at 83 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 13.58% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 67 ℃, and the reaction times is 1.0 hours; Be that 4% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 75 ℃, and the time is 1.5 hours; Add glacial acetic acid at last and regulate after pH value is 6.5, stir that to add temperature down be 80 ℃ deionized water, get solids content and be 25% white emulsion.
8, the preparation method of compound emulsion of dimmer of cation polyurethane and alkyl ketene according to claim 1, it is characterized in that: at first 9% alkyl ketene dimer is joined in the dry reactor by mass ratio, and reactor is heated to 78 ℃, after making the alkyl ketene dimer fusion in the reactor, press the tolylene diisocyanate of mass ratio adding 26% again, 48% relative molecular mass is that the dibutyl tin laurate of 2000 polyester binary pure and mild 0.43% joins in the reactor and carried out polycondensation 2.5 hours at 78 ℃, forms the alkyl ketene dimer solution of base polyurethane prepolymer for use as; With mass ratio is that 13.57% N methyldiethanol amine joins and carries out chain extending reaction in the alkyl ketene dimer solution, and temperature of reaction is 58 ℃, and the reaction times is 1.4 hours; Be that 3% methyl-sulfate joins and carries out quaterisation in the reactor again with mass ratio, temperature of reaction is 68 ℃, and the time is 2.0 hours; Add glacial acetic acid at last and regulate after pH value is 5.7, stir that to add temperature down be 50 ℃ deionized water, get solids content and be 25% white emulsion.
CNB2005100430180A 2005-07-28 2005-07-28 Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene Expired - Fee Related CN1298760C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2005100430180A CN1298760C (en) 2005-07-28 2005-07-28 Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2005100430180A CN1298760C (en) 2005-07-28 2005-07-28 Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene

Publications (2)

Publication Number Publication Date
CN1727377A true CN1727377A (en) 2006-02-01
CN1298760C CN1298760C (en) 2007-02-07

Family

ID=35926916

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2005100430180A Expired - Fee Related CN1298760C (en) 2005-07-28 2005-07-28 Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene

Country Status (1)

Country Link
CN (1) CN1298760C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101096829B (en) * 2007-07-13 2010-08-04 天津科技大学 Cation alkyl ketene dimer sizing agent and method for making same
CN108951285A (en) * 2018-08-02 2018-12-07 宁波高新区诠宝绶新材料科技有限公司 A kind of preparation method of Neutral Papermaking polymeric material
CN111593598A (en) * 2020-04-13 2020-08-28 仙鹤股份有限公司 Preparation method of artificial leather release base paper with uniform sizing

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2640955B2 (en) * 1988-02-02 1997-08-13 星光化学工業株式会社 Manufacturing method of polyurethane resin

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101096829B (en) * 2007-07-13 2010-08-04 天津科技大学 Cation alkyl ketene dimer sizing agent and method for making same
CN108951285A (en) * 2018-08-02 2018-12-07 宁波高新区诠宝绶新材料科技有限公司 A kind of preparation method of Neutral Papermaking polymeric material
CN111593598A (en) * 2020-04-13 2020-08-28 仙鹤股份有限公司 Preparation method of artificial leather release base paper with uniform sizing

Also Published As

Publication number Publication date
CN1298760C (en) 2007-02-07

Similar Documents

Publication Publication Date Title
CN109252387B (en) Leather/synthetic leather based on self-repairing waterborne polyurethane and preparation method thereof
CN101665675A (en) Method for preparing aqueous polyurethane adhesive and superfine fiber synthetic leather
CN103073876B (en) Preparation method of aromatic high solid content water-borne polyurethane
CN111607064A (en) Light/heat synergistic repair type waterborne polyurethane coating material and preparation method thereof
CN1727377A (en) Method for preparing compound emulsion of dimmer of cation polyurethane and alkyl ketene
CN109821473A (en) Multi-functional, the high activity cation Gemini surfactant of one kind and production method
CN102114396A (en) Non-quinoline dispersant MF and production process
CN102786648A (en) Cross-linking type shape memory polyurethane
CN108947845A (en) A kind of production method of 2,4-dinitrophenol sodium
CN104592469A (en) Anionic polyurethane aqueous dispersion, prepolymer monomer and preparation process thereof
CN102505489A (en) Preparation method of aqueous polyurethane antistatic finishing agent
CN101423478B (en) Method for producing hexane diacid and hexanediamine by using nylon-66 disaggregation
CN115895339A (en) High-waterproof water-based dye ink and preparation method and application thereof
CN100443506C (en) Low acid value solvent process of preparing chlorinated rubber
CN104628605A (en) Continuous catalytic sulfonation method of naphthalene and device thereof
CN100340718C (en) Method for preparing ceramic paper
CN110229378B (en) Crystallization drying process for recycling polyester bottle flakes
CN112898520A (en) Aqueous polyurethane dispersion and synthesis method thereof
CN101435173B (en) Paper making neutral sizing agent and preparing method thereof
JPS5996174A (en) Reactive dye for cellulose fiber
CN105131700A (en) LIP type nonionic surfactant, preparation method and applications thereof
CN101148492A (en) Method for preparing water polyurethane hot dissolving coating adhesive used for sofa-like leatheret
CN109811584A (en) A kind of preparation method and applications of the aqueous polyurethane fluorescent brightening lotion for paper surface
CN107557351A (en) One kind processing mthod of white water from paper making embedded particles immobilization mixed enzyme and preparation method thereof
CN109810240B (en) Preparation method and application of polyurethane fluorescent whitening emulsion containing piperidine amine

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee