CN104356292B - A kind of preparation method of PAMC aqueous emulsion product - Google Patents

A kind of preparation method of PAMC aqueous emulsion product Download PDF

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CN104356292B
CN104356292B CN201410564516.9A CN201410564516A CN104356292B CN 104356292 B CN104356292 B CN 104356292B CN 201410564516 A CN201410564516 A CN 201410564516A CN 104356292 B CN104356292 B CN 104356292B
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王黎明
崔仕章
谷之辉
杨红梅
高瑞美
张旭
韩冬
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Deshi Energy Technology Group Co Ltd
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Shandong Deshi Petroleum Engineering Group Co Ltd
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Abstract

The present invention provides a kind of response type dispersant and the preparation method of polyacrylamide aqueous emulsion, and the method preparing this aqueous emulsion includes: first prepare a kind of response type dispersant;Then, in the presence of salting liquid system and dispersant, equalize number of free radical by multistage composite initiation system, carry out the aqueous emulsion dispersin polymerization of acrylamide and cationic monomer.It is high that this aqueous emulsion product has dissolving rapidly, HMW, good fluidity and stability, can be widely used in every profession and trade water treatment field.

Description

A kind of preparation method of PAMC aqueous emulsion product
Technical field
The invention belongs to Polymer Synthesizing field, relate to the preparation side of a kind of PAMC aqueous emulsion product Method.
Background technology
Polyacrylamide is referred to as " all trades auxiliary agent ", PAMC therein (CPAM) be then apply the widest One of general kind.CPAM is the acrylamide copolymer of cation construction unit, and strand is ionizable in water to be gone out to gather sun Ion and little anion, the addition of CPAM cationic increases polymer to electronegative colloid, polymer and solid The absorption cementitiousness on surface, can cause stronger charge neutrality effect, enhances its absorption, bonds, decolours, precipitates and wad a quilt with cotton Solidifying grade acts on, and is particularly well-suited to paper technology, food industry, architectural engineering, metallurgical engineering, ore dressing coal dust, oil recovery industry, aquatic products Sewage in the industry that the organic colloid content such as processing and fermentation are higher and the process of waste water.
Aqueous two-phase dispersion copolymerization method is a kind of novel method preparing water-soluble polymer, utilizes this new method can be by The dissolving of one or more water-soluble monomers is dispersed in the aqueous solution in the presence of dispersant, is polymerized under certain condition, is formed Immiscible water-soluble polymer dispersion, is also aqueous polymer dispersion.
It is relatively low that aqueous emulsion reaction system has viscosity, and solid content is big, can prepare the water solubility that relative molecular mass is bigger Polymer, the shortcoming which overcoming traditional aqueous polymerization, during preparation and use, there is not organic solvent pollution problem, And aqueous emulsion product dissolves rapidly, can directly dilute use, therefore have broad application prospects and the value of environmental protection.
At present, the report of the preparation method of research aqueous emulsion is few both at home and abroad, and properties of product are the most perfect.Subject matter Concentrate in the dispersion stabilization difference of aqueous emulsion product and the effective content of CPAM and the low these two aspects of molecular weight.In order to solve this Two problems, technical staff has done substantial amounts of research work.With tertiary butanol aqueous solution for dividing in patent CN201210097234.3 CPAM aqueous emulsion prepared by powder, and result shows the CPAM aqueous emulsion poor stability prepared using the tert-butyl alcohol as dispersant, when depositing Between the longest.The CPAM molecular weight of preparation is on the low side, less than 3,500,000.For the chain overcoming small molecular alcohol to cause as dispersant The problems such as transfer is strong, (Liu expires document again, " double-aqueous phase polymerization method synthesizing cationic polyacrylamide and flocculating property thereof ", should With chemistry, 2010,28 (8): 874 ~ 878) provide and a kind of substitute the tert-butyl alcohol dispersant as reaction system using polyethylene glycol, Prepare the aqueous emulsion that a kind of dispersion stabilization is good, but in the method, polyethylene glycol consumption is the biggest so that cost is inclined Height, and the viscosity of emulsion system is high, poor fluidity, and the molecular weight of CPAM is low.What recently Improvement was most is by sun from Obtained by sub-monomer homopolymerization, low molecular weight cationic polymer is as dispersant, achieves good result.Such as patent CN102321213B provides with the cationic monomers such as acrylyl oxy-ethyl-trimethyl salmiac depositing at molecular weight regulator At dispersant obtained by lower homopolymerization.And prepared dispersiveness and the preferable higher molecular of mobility by homemade dispersant The aqueous emulsion product of amount CPAM, but the stability of this aqueous emulsion product is unknown, and also the molecular weight of dispersant controls and water and milk It is high that liquid polymerization technique controls difficulty.
In current most aqueous emulsion preparation technology, due to " gel effect " in polyacrylamide polymerization mechanism, instead There is autoacceleration process during Ying so that the polymerization speed of acrylamide copolymer have substantially exceed from dispersion separate out The possibility of speed, if controlling improper, be easy to get gel products very much, causes and is polymerized unsuccessfully.
Summary of the invention
It is an object of the invention to overcome some shortcomings of existing CPAM aqueous emulsion product preparation process, it is provided that a kind of effective Content is high, molecular weight is high, the preparation method of easy to operate easily-controllable CPAM aqueous emulsion product.
Another object of the present invention is to provide a kind of system viscosity less than 200mPaS, good fluidity, dissolution velocity Hurry up, can be at the not stratified high stable CPAM aqueous emulsion product of 24 months long-term storage.
For reaching above technical purpose, the present invention realizes by the following technical solutions.
The preparation method of a kind of PAMC aqueous emulsion product, is made by the response type polymeric monomer shown in formula (1) For dispersant, acrylamide and cationic monomer copolymerization form,
Formula (1), in formula (1), m is The degree of polymerization of polymer segment cation in macromonomer;N is the degree of polymerization of vinylpyrrolidone in macromonomer;A is 2 ~3;A is H or CH3, B is O or atom N.
The mean molecule quantity of polymeric monomer dispersant is 2 × 105~8 × 105
Described PAMC aqueous emulsion, its dissolution time is less than 10min.
Described PAMC aqueous emulsion, its molecular weight is more than 8,000,000.
Described PAMC aqueous emulsion, its product system viscosity is less than 400 mPa s.
The preparation method of polymeric monomer dispersant is:
The cationic monomer of 20~30 parts and the N-vinylpyrrolidone of 0~5 part are added in reactor by step 1), add The solvent of 30~100 parts dissolves;Nitrogen deoxygenation 15~30 minutes it are passed through in reactor;0.01~1 part is added in reactor Chain-transferring agent and the initiator of 0.001~0.05 part;Stirring reaction 4~6 hours at 60~70 DEG C;Add NaOH molten Liquid regulation pH value is to 7~9, and decompression pumps most solvent, precipitates three times with 10~50 parts of precipitating reagents, centrifugation, is dried Obtain white solid polymeric monomer precursor, its structural formula as the formula (2):
Formula (2)
Step 2) in reactor, add the polymeric monomer precursor of aforementioned 10~20 parts and the oxolane of 50~100 parts, molten Solve uniformly;1~10 part of acryloyl chloride is dissolved in 20~50 parts of oxolanes, joins in above-mentioned solution under stirring, drip simultaneously Add a certain amount of aqueous sodium carbonate, control reaction temperature at 0~4 DEG C with the jacket reactor of band refrigerant;React 2~4 hours After, it is warming up to room temperature;Decompression pumps solvent, precipitates three times, obtain white solid response type after drying in 10~50 parts of ether Dispersant, its structural formula is as the formula (1).
Described PAMC aqueous emulsion, preparation method is: by the acrylamides of 5~10 parts, 1~7 part The molecular weight of cationic monomer, the above-mentioned response type dispersant of 0.1~2 part, the ammonium sulfate of 20~35 parts and 0.1~4 part is The polyethylene glycol of 20000 joins in reactor, adds the chain extender of 0.001~0.05 part and the complexing of 0.001~0.01 part Agent, adds the deionized water of 40~60 parts, stirring and dissolving, and regulating pH with NaOH solution and dilute sulfuric acid is 5~8, logical nitrogen deoxygenation After 15~40min, the oxidationreduction being warming up to 30~35 DEG C of Oxidizing and Reducing Agents compositions adding 0.0001~0.01 part draws Send out agent, regulate mixing speed, after system becomes milky, add the azo initiator of 0.0001~0.01 part, be warming up to After 50~55 DEG C are continued reaction 4~6h, add the ammonium sulfate of 2~5 parts, after cooling, i.e. obtain the stable of favorable dispersibility CPAM aqueous emulsion product, in described PAMC aqueous emulsion preparation process, cationic monomer is selected from acryloyl-oxy Ethyl-trimethyl salmiac, MethacryloyloxyethylTrimethyl Trimethyl Ammonium Chloride, acryloxyethyldimethyl benzyl ammonium chloride, first One in base acryloxyethyldimethyl benzyl ammonium chloride, 2-acrylamido-2-trimethoxysilyl propyl methacrylate ammonium chloride or Two kinds;Chain extender is selected from N, N-dimethylethanolamine, ethylene glycol, hexylene glycol, N, N-dimethyl-ethylenediamine, N, N-tetramethyl second two One or more in amine, triethylene tetramine, DMPM 3 methylaminopropionitrile;Complexing agent is EDTA;Oxidant is selected from ammonium persulfate, mistake One or more in sodium sulphate, potassium peroxydisulfate, hydrogen peroxide and 2-methylethyl ketone peroxide;Reducing agent is selected from ammonium sulfite, sulfurous acid One or more in potassium, sodium sulfite, ammonium bisulfite, sodium hydrogensulfite, potassium bisulfite and sodium formaldehyde sulphoxylate; Azo series initiators be 2,2 '-azo (2-amidine propane) dihydrochloride, 2,2 '-azo (2-imidazoline propane) dihydrochloride and One or more in 4,4 '-azo double (4-cyanopentanoic acid).
Relative to prior art, there is advantages that present invention employs and a kind of can participate in reaction Polymeric monomer dispersant, can preferably guide and the speed of separating out that controls in polymerization process is equilibrium with polymerization speed, thus obtains The aqueous emulsion of stably dispersing;
The present invention makes polymerization process the most controlled by segmented polymerization technique, and this method can obtain the sun of HMW Cationic polyacrylamide, molecular weight can reach more than 8,000,000 after testing;
In aqueous emulsion product prepared by the present invention, inclusion is inorganic salts and macromolecule, overcomes easily waving of tradition use The small organic molecule sent out, polymerization conversion ratio is high, meets the green and requirement of molecule economy synthesis, simultaneously to environment and operation people Member is the most friendly;Aqueous emulsion product obtained by the present invention, out has that traditional aqueous product dissolution velocity is fast, good fluidity Outside etc. feature, more excellent part is that it has good stability, can long-term storage and be not layered, coacervation.
Detailed description of the invention
The present invention is described in detail below with reference to embodiment.
In following example, the performance test of product uses following methods to carry out:
1, polycation macromer molecular weight is measured by gel permeation chromatography (GPC);
2, solid content is measured according to the method for regulation in GB12005.2-89;
3, dissolution time is measured according to the method for regulation in GB12005.8-89;
4, measure and calculate the molecular weight of CPAM according to the method for regulation in GB12005.1-89;
5, the apparent viscosity of emulsion system is to measure with NDJ-5 type viscosimeter at 25 DEG C.
Embodiment 1
(1) synthesis of response type dispersant Disp-1
The acrylyl oxy-ethyl-trimethyl salmiac of 150kg and the N-vinylpyrrolidone of 12kg are joined two cubes instead Answer in still, add 550kg ethanol and dissolve;Nitrogen deoxygenation it is passed through 20 minutes in reactor;The mercapto of 3.2kg is added in reactor Base b ammonium salt hydrochlorate and the azodiisobutyronitrile of 280g.Stirring reaction 4 hours at 70 DEG C.Add sodium hydroxide solution regulation pH Value is to 7.0, and decompression pumps most solvent, with each 60kg ether sedimentation three times, centrifugation, is dried to obtain white solid big Monomer precursor;
In reactor, add above-mentioned polymeric monomer precursor and the 460kg oxolane of aforementioned 100kg, be uniformly dissolved;Will 18.5kg acryloyl chloride is dissolved in 80kg oxolane, joins in above-mentioned solution under stirring, is simultaneously added dropwise the carbon of 50kg 30% Acid sodium aqueous solution, controls reaction temperature at 3 DEG C with the jacket reactor of band refrigerant;After reacting 4 hours, it is warming up to room temperature;Decompression Pump major part solvent, precipitate three times in 60kg ether, obtain white solid response type dispersant Disp-1, molecule after drying Measure test result and be shown in Table 1;
(2) preparation of CAPM aqueous emulsion Hyem-1
The above-mentioned response type of the acrylamide of 50kg, the acrylyl oxy-ethyl-trimethyl salmiac of 18kg, 2.5kg is disperseed The ammonium sulfate of agent Disp-1,185kg and 3.6kg polyethylene glycol (molecular weight 20000) join in reactor, add 0.3kg's N, N-dimethylethanolamine and the EDTA of 0.2kg, add 190kg deionized water, stirring and dissolving, adjust with NaOH solution and dilute sulfuric acid Joint pH is 6, after logical nitrogen deoxygenation 30min, is warming up to 30 DEG C of ammonium persulfates adding 2.25g and the ammonium bisulfite of 2.25g, Stir polymer under 200rpm, after system becomes milky, add the 2 of 5.12g, 2 '-azo (2-amidine propane) disalt Hydrochlorate.After being warming up to 50 DEG C of continuation reaction 8h, add the ammonium sulfate of 21kg, after cooling, i.e. obtain the stable of favorable dispersibility CPAM aqueous emulsion product Hyem-1, its performance test results is shown in Table 2.
Embodiment 2
With embodiment 1, except for the difference that change the amount of N-vinylpyrrolidone in step (1) into 5 kilograms, the acid of sulfydryl b ammonium salt The amount of salt changes 2.0kg into, obtains corresponding product dispersant Disp-2, and molecule measuring test result is shown in Table 1;Anti-in step (2) Answering type dispersant Disp-1 to change Disp-2 into, obtain CPAM aqueous emulsion product Hyem-2, its performance test results is shown in Table 2.
Embodiment 3
(1) synthesis of response type dispersant Disp-3
The MethacryloyloxyethylTrimethyl Trimethyl Ammonium Chloride of 140kg and the N-vinylpyrrolidone of 15kg are joined two and stand In side's reactor, add 550kg ethanol and dissolve;Nitrogen deoxygenation it is passed through 20 minutes in reactor;3.8kg is added in reactor Sulfydryl b ammonium salt hydrochlorate and the azodiisobutyronitrile of 280g.Stirring reaction 4 hours at 70 DEG C.Add sodium hydroxide solution to adjust Joint pH value is to 7.0, and decompression pumps most solvent, with each 60kg ether sedimentation three times, centrifugation, is dried to obtain white and consolidates Body polymeric monomer precursor;
In reactor, add above-mentioned polymeric monomer precursor and the 460kg oxolane of aforementioned 100kg, be uniformly dissolved;Will 20.1kg acryloyl chloride is dissolved in 80kg oxolane, joins in above-mentioned solution under stirring, is simultaneously added dropwise the carbon of 55kg 30% Acid sodium aqueous solution, controls reaction temperature at 3 DEG C with the jacket reactor of band refrigerant;After reacting 8 hours, it is warming up to room temperature;Decompression Pump major part solvent, precipitate three times in 60kg ether, obtain white solid response type dispersant Disp-3, molecule after drying Measure test result and be shown in Table 1;
(2) preparation of CAPM aqueous emulsion Hyem-3
The above-mentioned response type of the acrylamide of 50kg, the acrylyl oxy-ethyl-trimethyl salmiac of 18kg, 2.2kg is disperseed The ammonium sulfate of agent Disp-3,180kg and 3.5kg polyethylene glycol (molecular weight 20000) join in reactor, add 0.3kg's N, N-dimethylethanolamine and the EDTA of 0.2kg, add 190kg deionized water, stirring and dissolving, adjust with NaOH solution and dilute sulfuric acid Joint pH is 6, after logical nitrogen deoxygenation 30min, is warming up to 30 DEG C of ammonium persulfates adding 2.10g and the ammonium bisulfite of 2.10g, Stir polymer under 200rpm, after system becomes milky, add the 2 of 5.10g, 2 '-azo (2-amidine propane) disalt Hydrochlorate.After being warming up to 50 DEG C of continuation reaction 4h, add the ammonium sulfate of 20kg, after cooling, i.e. obtain the stable of favorable dispersibility CPAM aqueous emulsion product Hyem-3, its performance test results is shown in Table 2.
Embodiment 4
With embodiment 3, except for the difference that change the amount of N-vinylpyrrolidone in step (1) into 2 kilograms, the acid of sulfydryl b ammonium salt The amount of salt changes 3.2kg into, obtains corresponding product dispersant Disp-4, and molecule measuring test result is shown in Table 1;Anti-in step (2) Answering type dispersant Disp-3 to change Disp-4 into, obtain CPAM aqueous emulsion product Hyem-4, its performance test results is shown in Table 2.
Embodiment 5
(1) synthesis of response type dispersant Disp-5
The N-vinylpyrrolidone of 140kg 3-acrylamide propyl-trimethyl ammonium chloride and 20kg is joined two cubes In reactor, add 580kg ethanol and dissolve;Nitrogen deoxygenation it is passed through 20 minutes in reactor;In reactor, add 3.6kg's Sulfydryl b ammonium salt hydrochlorate and the azodiisobutyronitrile of 270g.Stirring reaction 4 hours at 70 DEG C.Add sodium hydroxide solution regulation PH value is to 7.0, and decompression pumps most solvent, with each 60kg ether sedimentation three times, centrifugation, is dried to obtain white solid Polymeric monomer precursor;
In reactor, add above-mentioned polymeric monomer precursor and the 460kg oxolane of aforementioned 100kg, be uniformly dissolved;Will 18.5kg acryloyl chloride is dissolved in 80kg oxolane, joins in above-mentioned solution under stirring, is simultaneously added dropwise the carbon of 52kg 30% Acid sodium aqueous solution, controls reaction temperature at 3 DEG C with the jacket reactor of band refrigerant;After reacting 5 hours, it is warming up to room temperature;Decompression Pump major part solvent, precipitate three times in 60kg ether, obtain white solid response type dispersant Disp-5, molecule after drying Measure test result and be shown in Table 1;
(2) preparation of CAPM aqueous emulsion Hyem-3
By 50kg acrylamide, 18kg 3-acrylamide propyl-trimethyl ammonium chloride, 2.5kg above-mentioned response type dispersant Disp-5,180kg ammonium sulfate and 3.3kg polyethylene glycol (molecular weight 20000) join in reactor, add the N, N-of 0.3kg Dimethylethanolamine and 0.2kg EDTA, add 190kg deionized water, stirring and dissolving, regulate pH with NaOH solution and dilute sulfuric acid It is 6, after logical nitrogen deoxygenation 30min, is warming up to 30 DEG C of ammonium persulfates adding 2.20g and the ammonium bisulfite of 2.20g, 200rpm Lower stirring polymer, after system becomes milky, adds the 2 of 5.10g, 2 '-azo (2-amidine propane) dihydrochloride.Rise After temperature continues reaction 8h to 50 DEG C, add the ammonium sulfate of 20kg, after cooling, i.e. obtain the stable CPAM water of favorable dispersibility Product emulsion Hyem-5, its performance test results is shown in Table 2.
Embodiment 6
With embodiment 5, except for the difference that change the amount of N-vinylpyrrolidone in step (1) into 2 kilograms, the acid of sulfydryl b ammonium salt The amount of salt changes 3.2kg into, obtains corresponding product dispersant Disp-6, and molecule measuring test result is shown in Table 1;Anti-in step (2) Answering type dispersant Disp-5 to change Disp-6 into, obtain CPAM aqueous emulsion product Hyem-6, its performance test results is shown in Table 2.
Embodiment 7
(1) synthesis of response type dispersant Disp-7
By 80kg acrylyl oxy-ethyl-trimethyl salmiac, the 3-acrylamide propyl-trimethyl ammonium chloride of 60kg and The N-vinylpyrrolidone of 10kg joins in two cubes of reactors, adds 580kg ethanol and dissolves;Nitrogen it is passed through in reactor Deoxygenation 20 minutes;The chain-transferring agent of 3.6kg and the azodiisobutyronitrile of 270g is added in reactor.Stirring reaction at 70 DEG C 4 hours.Addition sodium hydroxide solution regulation pH value is to 7.0, and decompression pumps most solvent, with each 60kg ether sedimentation three Secondary, centrifugation, it is dried to obtain white solid polymeric monomer precursor;
In reactor, add above-mentioned polymeric monomer precursor and the 460kg oxolane of aforementioned 100kg, be uniformly dissolved;Will 18.5kg acryloyl chloride is dissolved in 80kg oxolane, joins in above-mentioned solution under stirring, is simultaneously added dropwise the carbon of 52kg 30% Acid sodium aqueous solution, controls reaction temperature at 3 DEG C with the jacket reactor of band refrigerant;After reacting 5 hours, it is warming up to room temperature;Decompression Pump major part solvent, precipitate three times in 60kg ether, obtain white solid response type dispersant Disp-7, molecule after drying Measure test result and be shown in Table 1;
(2) preparation of CAPM aqueous emulsion Hyem-7
By the acrylamide of 50kg, the 3-acrylamide propyl-trimethyl ammonium chloride of 18kg, the above-mentioned response type of 2.5kg The ammonium sulfate of dispersant Disp-7,180kg and 3.3kg polyethylene glycol (molecular weight 20000) join in reactor, add The N of 0.3kg, N-dimethylethanolamine and the EDTA of 0.2kg, add 190kg deionized water, stirring and dissolving, by NaOH solution and Dilute sulfuric acid regulation pH is 6, after logical nitrogen deoxygenation 30min, is warming up to 30 DEG C of ammonium persulfates adding 2.20g and the sulfurous of 2.20g Acid hydrogen ammonium, stirs polymer, after system becomes milky, adds the 2 of 5.10g, 2 '-azo (2-amidino groups third under 200rpm Alkane) dihydrochloride.After being warming up to 50 DEG C of continuation reaction 8h, add the ammonium sulfate of 20kg, after cooling, i.e. obtain favorable dispersibility Stable CPAM aqueous emulsion product Hyem-7, its performance test results is shown in Table 2.
Embodiment 8
(1) synthesis of response type dispersant Disp-8
By the acrylyl oxy-ethyl-trimethyl salmiac of 140kg, 10kg acryloxyethyldimethyl benzyl ammonium chloride and The N-vinylpyrrolidone of 12kg joins in two cubes of reactors, adds 550kg ethanol and dissolves;Nitrogen it is passed through in reactor Deoxygenation 20 minutes;The chain-transferring agent of 3.0kg and the azodiisobutyronitrile of 270g is added in reactor.Stirring reaction at 70 DEG C 4 hours.Addition sodium hydroxide solution regulation pH value is to 7.0, and decompression pumps most solvent, with each 60kg ether sedimentation three Secondary, centrifugation, it is dried to obtain white solid polymeric monomer precursor;
In reactor, add above-mentioned polymeric monomer precursor and the 460kg oxolane of aforementioned 100kg, be uniformly dissolved;Will 18.5kg acryloyl chloride is dissolved in 80kg oxolane, joins in above-mentioned solution under stirring, is simultaneously added dropwise the carbon of 50kg 30% Acid sodium aqueous solution, controls reaction temperature at 3 DEG C with the jacket reactor of band refrigerant;After reacting 5 hours, it is warming up to room temperature;Decompression Pump major part solvent, precipitate three times in 60kg ether, obtain white solid response type dispersant Disp-8, molecule after drying Measure test result and be shown in Table 1;
(2) preparation of CAPM aqueous emulsion Hyem-8
By the acrylamide of 50kg, the 3-acrylamide propyl-trimethyl ammonium chloride of 18kg, the above-mentioned response type of 3.2 kg The ammonium sulfate of dispersant Disp-4,180kg and 3.0kg polyethylene glycol (molecular weight 20000) join in reactor, add The N of 0.3kg, N-dimethylethanolamine and the EDTA of 0.2kg, add 190kg deionized water, stirring and dissolving, by NaOH solution and Dilute sulfuric acid regulation pH is 6, after logical nitrogen deoxygenation 30min, is warming up to 30 DEG C of ammonium persulfates adding 2.10g and the sulfurous of 2.10g Acid hydrogen ammonium, stirs polymer, after system becomes milky, adds the 2 of 5.10g, 2 '-azo (2-amidino groups third under 200rpm Alkane) dihydrochloride.After being warming up to 50 DEG C of continuation reaction 8h, add the ammonium sulfate of 20kg, after cooling, i.e. obtain favorable dispersibility Stable CPAM aqueous emulsion product Hyem-8, its performance test results is shown in Table 2.
The molecule measuring test result of dispersant in each embodiment of table 1
The performance test results of CPAM aqueous emulsion product in each embodiment of table 2

Claims (7)

1. the preparation method of a PAMC aqueous emulsion product, it is characterised in that: by the response type shown in formula (1) Polymeric monomer, as dispersant, is formed by acrylamide and cationic monomer copolymerization,
Formula (1), in formula (1), m is big point The degree of polymerization of polymer segment cation in sub-monomer;N is the degree of polymerization of vinylpyrrolidone in macromonomer;A is 2~3; A is H or CH3, B is O or atom N.
The preparation method of a kind of PAMC aqueous emulsion product the most according to claim 1, it is characterised in that: The mean molecule quantity of polymeric monomer dispersant is 2 × 105~8 × 105
The preparation method of a kind of PAMC aqueous emulsion product the most according to claim 1, it is characterised in that: Described PAMC aqueous emulsion, its dissolution time is less than 10min.
The preparation method of a kind of PAMC aqueous emulsion product the most according to claim 1, it is characterised in that: Described PAMC aqueous emulsion, its molecular weight is more than 8,000,000.
The preparation method of a kind of PAMC aqueous emulsion product the most according to claim 1, it is characterised in that: Described PAMC aqueous emulsion, its product system viscosity is less than 400 mPa s.
The preparation method of a kind of PAMC aqueous emulsion product the most according to claim 1, it is characterised in that: The preparation method of polymeric monomer dispersant is:
The N-vinylpyrrolidone of the cationic monomer of 20~30 parts and 0~5 part is added in reactor by step 1), add 30~ The solvent of 100 parts dissolves;Nitrogen deoxygenation 15~30 minutes it are passed through in reactor;The chain of 0.01~1 part is added in reactor Transfer agent and the initiator of 0.001~0.05 part;Stirring reaction 4~6 hours at 60~70 DEG C;Add sodium hydroxide solution to adjust Joint pH value is to 7~9, and decompression pumps most solvent, precipitates three times with 10~50 parts of precipitating reagents, centrifugation, is dried to obtain White solid polymeric monomer precursor, its structural formula as the formula (2):
Formula (2)
Step 2) in reactor, add the polymeric monomer precursor of aforementioned 10~20 parts and the oxolane of 50~100 parts, dissolve all Even;1~10 part of acryloyl chloride is dissolved in 20~50 parts of oxolanes, joins in above-mentioned solution under stirring, be simultaneously added dropwise one Quantitative aqueous sodium carbonate, controls reaction temperature at 0~4 DEG C with the jacket reactor of band refrigerant;After reacting 2~4 hours, rise Warm to room temperature;Decompression pumps solvent, precipitates three times in 10~50 parts of ether, obtains the dispersion of white solid response type after drying Agent, its structural formula is as the formula (1).
The preparation method of a kind of PAMC aqueous emulsion product the most according to claim 1, it is characterised in that: Described PAMC aqueous emulsion, preparation method is: by the acrylamides of 5~10 parts, the cation mono of 1~7 part The poly-second that molecular weight is 20000 of body, the above-mentioned response type dispersant of 0.1~2 part, the ammonium sulfate of 20~35 parts and 0.1~4 part Glycol joins in reactor, adds the chain extender of 0.001~0.05 part and the complexing agent of 0.001~0.01 part, add 40~ The deionized water of 60 parts, stirring and dissolving, regulating pH with NaOH solution and dilute sulfuric acid is 5~8, after logical nitrogen deoxygenation 15~40min, Being warming up to 30~35 DEG C of oxidation-reduction initiators adding the Oxidizing and Reducing Agents composition of 0.0001~0.01 part, regulation is stirred Mix speed, after system becomes milky, add the azo initiator of 0.0001~0.01 part, be warming up to 50~55 DEG C of continuation After reaction 4~6h, adding the ammonium sulfate of 2~5 parts, the stable CPAM aqueous emulsion i.e. obtaining favorable dispersibility after cooling is produced Product, in described PAMC aqueous emulsion preparation process, cationic monomer is selected from acrylyl oxy-ethyl-trimethyl chlorine Change ammonium, MethacryloyloxyethylTrimethyl Trimethyl Ammonium Chloride, acryloxyethyldimethyl benzyl ammonium chloride, methacryloxypropyl second One or both in base dimethyl benzyl ammonium chloride, 2-acrylamido-2-trimethoxysilyl propyl methacrylate ammonium chloride;Chain extender selects From N, N-dimethylethanolamine, ethylene glycol, hexylene glycol, N, N-dimethyl-ethylenediamine, N, N-tetramethylethylenediamine, triethylene four One or more in amine, DMPM 3 methylaminopropionitrile;Complexing agent is EDTA;Oxidant is selected from ammonium persulfate, sodium peroxydisulfate, over cure One or more in acid potassium, hydrogen peroxide and 2-methylethyl ketone peroxide;Reducing agent selected from ammonium sulfite, potassium sulfite, sodium sulfite, One or more in ammonium bisulfite, sodium hydrogensulfite, potassium bisulfite and sodium formaldehyde sulphoxylate;Azo series initiators It is that 2,2 '-azo (2-amidine propane) dihydrochloride, 2,2 '-azo (2-imidazoline propane) dihydrochloride and 4,4 '-azo are double One or more in (4-cyanopentanoic acid).
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