CN1072685C - Method for prepn. of latex for coating paper - Google Patents

Method for prepn. of latex for coating paper Download PDF

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Publication number
CN1072685C
CN1072685C CN97113381A CN97113381A CN1072685C CN 1072685 C CN1072685 C CN 1072685C CN 97113381 A CN97113381 A CN 97113381A CN 97113381 A CN97113381 A CN 97113381A CN 1072685 C CN1072685 C CN 1072685C
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China
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polymerization
conjugated diene
latex
monomer
aromatic ethenyl
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Expired - Fee Related
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CN97113381A
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CN1208736A (en
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米普科
李成贵
杨继刚
刘静平
达世明
严增涛
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CHEMICAL INST LANZHOU CHEMICAL
Lanzhou Chemical Industry Co china National Petroleum Corp
China Petrochemical Corp
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CHEMICAL INST LANZHOU CHEMICAL
Lanzhou Chemical Industry Co china National Petroleum Corp
China Petrochemical Corp
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Abstract

The present invention relates to a method for polymerizing the emulsion of a carboxyl butadienestyrene copolymer used for coating paper. Monomers are respectively composed of vinyl unsaturated carboxylic acid, a fatty group conjugated diene, an aromatic vinyl composition and unsaturated acid amide. The present invention adopts a two section polymerization method, and leads the obtained latex to have good performances by controlling the addition amount of each section of monomer. Paint has stable mechanical performances, and fluidity, binding strength and water resistance meet the requirement of a high coating speed. In addition, the binding strength, the glossiness and the foaming resistance performance reach the optimum balance.

Description

A kind of preparation method of paper latex for coating
The present invention relates to a kind of high molecule emulsion polymerization method, more particularly, relate to the emulsion polymerisation process of a kind of paper coating with the carboxyl butylbenzene copolymer.
On paper, cardboard, be coated with the pigment dispersion (coating) that contains latex and can improve optical properties such as gloss, whiteness, and can improve surface smoothness, ink absorption, improved print gloss.Along with the continuous progress of paper-making technique and the high speed of surface covered, coating performance to coating requires also more and more higher, this mainly comprises having favorable mechanical stability, good flowability and equal voltinism, good cohesive strength and water tolerance, surface of good spreadability etc., in the prior art, the paper latex for coating many improvement have been done, as latex being made the distinct nucleocapsid structure of second-order transition temperature, the stone soft shell, soft nuclear duricrust, to improve sheet gloss etc., U.S.Patent3487032 discloses a kind of tetrapolymer latex, adopt the increment polymerization process, wherein comprise 20~70wt% aromatic vinyl monomer, 30~80wt% aliphatics conjugated diene monomer, 0.5~10wt% vinyl unsaturated carboxylic acid and 0.1~5wt% unsaturated amides.This invention is with aromatic vinyl monomer and aliphatics conjugated diene monomer, vinyl unsaturated carboxylic acid and vinyl unsaturated amides carry out pre-mixing respectively, by increment method mix monomer is joined in the polymerization reactor, in whole polymerization process, monomer ratio is that the ratio of aliphatics conjugated diene and aromatic vinyl monomer is a constant, the ratio of these monomers in the polymkeric substance that forms also is relatively-stationary, therefore still can not solve along with the printing technology high speed, cross the deficiency that decarboxylate butylbenzene copolymer latex exists anti-whipability, or when having satisfied anti-whipability, cohesive strength, the water tolerance this defective that can descend.Therefore latex is under paper machine surface covered condition with higher, and the mechanical stability of coating, flowability, surface strength of paper seem relatively poor, is difficult to form fine and smooth, fine and close coating layer.
The preparation method who the purpose of this invention is to provide a kind of paper latex for coating, make the latex excellent performance that obtains, the mechanical stability of coating, flowability, cohesive strength and water tolerance satisfy the requirement of high surface covered, and cohesive strength and glossiness, anti-whipability reach optimum balance.
The present invention seeks to realize by following method.
Adopt two sections polymerization techniques, first section polymerization single polymerization monomer is by C 3~C 5Vinyl unsaturated carboxylic acid, C 3~C 4Unsaturated amides, C 4~C 5Aliphatics conjugated diene, C 8~C 9Aromatic ethenyl compound form, its consumption is 25~50wt% of one, two section total monomer amount.In one-step polymerization, in the monomer that adds: the total amount of aliphatics conjugated diene (1) and aromatic ethenyl compound (2) is 100wt%, and the one-step polymerization set of monomers becomes accordingly:
(1) the aliphatics conjugated diene has: divinyl, isoprene, its consumption are 35~45wt%, and be relatively poor with quantity not sufficient 35% latex cohesive strength, greater than then water tolerance reduction of 45wt%.
(2) aromatic ethenyl compound has: vinylbenzene, vinyl toluene and their mixture, its consumption are 55~65wt%, not enough 55wt%, its cohesive strength, poor water resistance, also poor greater than the 65wt% cohesive strength.
(3) the vinyl unsaturated carboxylic acid has: methacrylic acid, vinylformic acid, methylene-succinic acid and their mixture.Its consumption is that 5~10wt%[is 100wt% in monomer (1), (2) total amount, and is as follows], not enough 5wt%, latex stability and cohesive strength are relatively poor, and be bigger greater than 10% viscosity of latex, and the coating flowability is bad.
(4) unsaturated amides has: acrylamide, Methacrylamide, n-methylolacrylamide and their mixture, its consumption is 0.5~5.0wt%, and not enough 0.5wt% latex stability is relatively poor, the water tolerance deficiency, too high greater than the 5.0wt% viscosity of latex, the White Board water tolerance is not good enough.
Second section polymerization single polymerization monomer is by C 4~C 5Aliphatics conjugated diene, C 8~C 9Aromatic ethenyl compound form or add again C 3~C 5Vinyl unsaturated carboxylic acid, C 3~C 4Unsaturated amides in one or both compositions.Its consumption is 50~75wt% of one, two section total monomer amount, and in two sections polymerizations, in the monomer that adds: the total amount of aliphatics conjugated diene (1) and aromatic ethenyl compound (2) is 100wt%, and corresponding two sections polymerization single polymerization monomers consist of:
(1) aliphatics conjugated diene: divinyl, isoprene are arranged, and its consumption is 30~45wt%.
(2) aromatic ethenyl compound has: vinylbenzene, vinyl toluene and their mixture, its consumption are 55~70wt%.
(3) the vinyl unsaturated carboxylic acid has: methacrylic acid, vinylformic acid, methylene-succinic acid and their mixture, its consumption is that 0~3.0wt%[is 100wt% in monomer (1), (2) total amount, and is as follows].
(4) unsaturated amides has: acrylamide, Methacrylamide, n-methylolacrylamide, and their mixture, its consumption are 0~2.0wt%.
One section monomer, two sections monomers can adopt once, add polymerization in batches or continuously, can adopt general polymerization starter, emulsifying agent, chain-transfer agent during polymerization, and polymerization temperature is 40~80 ℃, polymerization time 6~12h.
Characteristics of the present invention are that the latex that the preparation method of application paper latex for coating of the present invention obtains is tetrapolymer latex, and monomer is respectively aromatic ethenyl compound, aliphatics conjugated diene, vinyl unsaturated carboxylic acid and unsaturated amides.On the one hand, though adopt two sections polymerizations, but still can not constitute nucleocapsid structure latex, on the other hand owing to adopted two sections polymeric methods, one section monomer is formed with two sections compositions relatively independent, and this can mutually adjust contradiction and reaches optimum balance thereby make the cohesiveness of the latex that the method for application invention obtains and optical property.The preparation method of paper latex for coating of the present invention in addition, control to one section, two sections each monomer compositing range is also quite necessary, thus obtained latex excellent performance, can not only satisfy the optical property of improving paper, improve printing performance and can satisfy the high coating performance that the high speed owing to the paper surface covered brings.
Use the made coating of latex that the preparation method of paper latex for coating of the present invention makes, its mechanical stability, flowability, cohesive strength and water tolerance excellence, and also cohesive strength and glossiness, anti-whipability have obtained optimum balance.
Embodiment 1
(is 100wt% in one, two section total monomer add-on)
In the 10L polymerization reactor, add distilled water 90wt%, 12 carbon sodium alkyl benzene sulfonate 0.2wt%, vinylbenzene 18wt%, divinyl 13wt%, vinylformic acid 2wt%, acrylamide 1.0wt%, n-methylolacrylamide 0.5wt%, and DDM dodecyl mercaptan 0.15wt%, sodium bicarbonate 1.2wt% adds ammonium persulphate 0.8wt% in the time of 80 ℃, polyase 13 hour, add vinylbenzene 39wt% again, divinyl 25wt%, vinylformic acid 1wt%, acrylamide 0.5wt%, DDM dodecyl mercaptan 0.25wt%, 12 carbon sodium alkyl benzene sulfonate 0.2wt%, the mixture of Potassium Persulphate 0.2wt% and water 10wt% finishes until polymerization.After deviating from residual monomer, regulate pH value to 7.0, obtain latex at last with potassium hydroxide, the preparation coating composition, coating composition is pressed following formulation: (wt%)
Proportioning raw materials
China clay 70
Lime carbonate 30
Sumstar 190 13
Latex 17
Dispersion agent 0.3
Coating concentration is 60 ± 2wt%, and the pH value is 8.5.Coating and White Board performance see Table 2.
Embodiment 2,3,4,5,6,7,8
Use the polymerization process identical with embodiment 1, change the add-on of monomer and conditioning agent, concrete component is formed and is seen Table 1, obtain latex after, employing and embodiment 1 identical method is made coating composition again, coating and White Board performance see Table 2.
Comparative example 1,2,3,4,5,6
Use the polymerization process identical with embodiment 1, change the add-on of monomer and conditioning agent, concrete component is formed and is seen Table 1, obtain latex after, employing and embodiment 1 identical method is made coating composition again, coating and White Board performance see Table 2.
Comparative example 7
Adopt the one-step polymerization method, promptly (is 100wt% in one, two section total monomer add-on) adds distilled water 100wt%, 12 carbon sodium alkyl benzene sulfonate 0.2wt% in the 10L polymerization reactor, vinylbenzene 57wt%, divinyl 38wt%, vinylformic acid 3.5wt%, acrylamide 1.5wt%, and DDM dodecyl mercaptan 0.35wt%, sodium bicarbonate 1.2wt% adds ammonium persulphate 0.8wt% in the time of 80 ℃, finish until polymerization.After deviating from residual monomer, regulate pH value to 7.0 with potassium hydroxide.After obtaining latex, adopt the method identical with embodiment 1 to make coating composition again, coating and White Board performance see Table 2.
The performance measurement method all adopts GB:
Whiteness: GB7974, glossiness: GB8941.3, smoothness: GB456, tear strength: GB10341, print gloss: GB8941.3, ink absorption: GB12911, water absorbent surface: GB1540.
Table 1 embodiment and comparative example monomer are formed
Latex is formed (wt%) Embodiment Comparative example
1 2 3 4 5 6 7 8 1 2 3 4 5 6 7
One section Styrene α-vinyltoluene butadiene-isoprene acrylic acid methacrylic acid itaconic acid acrylamide Methacrylamide NMA DDM dodecyl mercaptan 18 - 13 - 2 - - 1 - 0.5 0.15 22 - 18 - - - 3 2 - - 0.15 16 - - 12 - 1 1 0.5 0.5 - 0.2 15 - 12 - 1.5 1 - 1 - - 0.15 13 5 5 - 1.5 - - - - 1 0.15 10 8 13 - 2 - 1.0 0.5 - - 0.2 - 18 13 - 3 - - - 0.5 0.2 18 - 13 - 3 - - 0.5 - 0.2 18 - 13 - 2.5 - - - - - 0.15 17 - 12 - 2 - - 2 - 0.5 0.2 17 - 12 - 1 1 - 1 0.5 - 0.115 17 - 12 - 4.5 - - 1.5 - - 0.15 17 - 13 - 2 - - 1 - - 0.15 17 - 13 - 2.5 - - 1.5 - - 0.15 57 - 38 - 3.5 - - 1.5 - - 0.35
Two sections Styrene butadiene acrylic acid acrylamide n-methylolacrylamide DDM dodecyl mercaptan 39 25 1 0.5 - 0.25 35 20 - - - 0.15 42.5 26 - 0.5 - 0.2 42.5 26 0.5 0.5 - 0.15 49 24 1.0 - 0.5 0.15 44 21 - 0.5 - 0.2 44 21 - - 0.5 0.15 45 20 - 0.5 - 0.15 40.3 25 1 0.2 - 0.2 40 25.5 1 - - 0.15 40 25 1 1.5 - 0.2 40 25 - - - 0.2 46.5 19 1 0.5 - 0.2 35 29.5 1 0.5 - 0.2 - - - - - -
Table 2. White Board rerum natura
Project Embodiment Comparative example
1 2 3 4 5 6 7 8 1 2 3 4 5 6 7
Coating solid content (%) 59.1 58.6 58.6 58.5 58.5 58.7 58.3 58.1 58.9 59.0 58.6 58.6 58.2 58.4 58.6
Dope viscosity (mPas) 1820 2020 2140 1920 1870 2100 2180 2140 1630 2550 2780 2816 2020 2300 2364
Whiteness (%) 80.9 80.9 81.1 81.0 80.1 80.6 81 80.4 80.6 80.0 80.4 80.5 80.2 80.2 80.7
Glossiness (%) 17.2 16.9 16.8 16.7 16.9 17.1 16.8 17.0 17.0 16.7 17.4 17.3 18.0 16.0 17.7
Smoothness (s) 81 85 82 91 79 82 84 89 86 84 83 80 62 86 73
Surface strength (m/s) Tear 2.60 2.43 2.45 2.28 2.65 2.65 2.55 2.57 1.90 1.98 2.00 2.16 1.50 2.40 1.87
Bubble 1.96 1.87 1.95 1.92 1.97 1.93 1.92 1.96 1.85 1.87 1.92 1.96 1.40 1.90 1.62
Print gloss (%) 65.4 62.7 57.7 59.3 58.3 60.0 63.0 62.7 56.3 56.2 59.2 64.3 66.7 55.3 60.3
Ink absorption (%) 23.8 24.1 24.0 24.6 25.1 20.9 22.1 23.7 25.6 24.7 23.7 22.6 30.0 23.0 23.6
Water absorbent surface (g/m 2) 38 44 38 43 39 42 38 39 51 54 48 47 41 54 51

Claims (5)

1. the preparation method of a paper latex for coating, polymerization single polymerization monomer is aliphatics conjugated diene, aromatic ethenyl compound, vinyl unsaturated carboxylic acid, unsaturated amides, adopt two sections polymerization techniques, one section monomer, two sections monomers can adopt once, add polymerization in batches or continuously, can adopt general polymerization starter, emulsifying agent, chain-transfer agent during polymerization, polymerization temperature is 40~80 ℃, polymerization time 6~12h is characterised in that:
(1) first section polymerization single polymerization monomer is by C 3~C 5Vinyl unsaturated carboxylic acid, C 3~C 4Unsaturated amides, C 4~C 5Aliphatics conjugated diene, C 8~C 9Aromatic ethenyl compound form, its consumption is 25~50wt% of one, two section total monomer amount, in one-step polymerization, in the aliphatics conjugated diene of adding and the total amount of aromatic ethenyl compound is 100wt%, corresponding one-step polymerization set of monomers becomes: aliphatics conjugated diene 35~45wt%, aromatic ethenyl compound 55~65wt%, vinyl unsaturated carboxylic acid 5~10wt%, unsaturated amides 0.5~5.0wt%;
(2) second sections polymerization single polymerization monomers are by C 4~C 5Aliphatics conjugated diolefine, C 8~C 9Aromatic ethenyl compound form or add again C 3~C 5Vinyl unsaturated carboxylic acid, C 3~C 4One or both compositions in the unsaturated amides, its consumption is 50~75wt% of one, two section total monomer amount, in two sections polymerizations, in the aliphatics conjugated diene of adding and the total amount of aromatic ethenyl compound is 100wt%, corresponding two sections polymerization single polymerization monomers consist of: aliphatics conjugated diene 30~45wt%, aromatic ethenyl compound 55~70wt%, vinyl unsaturated carboxylic acid 0~3.0wt%, unsaturated amides 0~2.0wt%.
2. the preparation method of latex according to claim 1 is characterized in that the aliphatics conjugated diene is divinyl or isoprene.
3. the preparation method of latex according to claim 1 is characterized in that aromatic ethenyl compound is vinylbenzene or vinyl toluene and their mixture.
According to claim 1 the preparation method of fast latex, it is characterized in that the vinyl unsaturated carboxylic acid is methacrylic acid, vinylformic acid, methylene-succinic acid and their mixture.
5. the preparation method of latex according to claim 1 is characterized in that unsaturated amides is acrylamide, Methacrylamide, n-methylolacrylamide and their mixture.
CN97113381A 1997-08-14 1997-08-14 Method for prepn. of latex for coating paper Expired - Fee Related CN1072685C (en)

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Publication number Priority date Publication date Assignee Title
CN100475887C (en) 2001-11-26 2009-04-08 米其林技术公司 Rubber composition for tread and method for manufacturing same
CN105542079A (en) * 2016-02-19 2016-05-04 莱芜兴业滤材树脂有限公司 Method for preparing styrene-butadiene latex without adding emulsifier
CN110416547B (en) * 2018-04-26 2021-09-21 中国石油化工股份有限公司 Slurry composition, preparation method thereof, battery cathode and lithium ion battery

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6163795A (en) * 1984-09-03 1986-04-01 ジェイエスアール株式会社 Paper coating composition
CN87105487A (en) * 1987-08-06 1988-07-27 中国石油化工总公司 The preparation method of high-stability carboxylic butadiene-styrene latex
JPS63227892A (en) * 1987-03-12 1988-09-22 住友ダウ株式会社 Paper coating composition
JPH02210094A (en) * 1989-02-01 1990-08-21 Japan Synthetic Rubber Co Ltd Copolymer latex and composition for coating paper
JPH04359001A (en) * 1991-06-03 1992-12-11 Sumitomo Dow Ltd Production of copolymer latex and paper-coating composition produced by using the same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6163795A (en) * 1984-09-03 1986-04-01 ジェイエスアール株式会社 Paper coating composition
JPS63227892A (en) * 1987-03-12 1988-09-22 住友ダウ株式会社 Paper coating composition
CN87105487A (en) * 1987-08-06 1988-07-27 中国石油化工总公司 The preparation method of high-stability carboxylic butadiene-styrene latex
JPH02210094A (en) * 1989-02-01 1990-08-21 Japan Synthetic Rubber Co Ltd Copolymer latex and composition for coating paper
JPH04359001A (en) * 1991-06-03 1992-12-11 Sumitomo Dow Ltd Production of copolymer latex and paper-coating composition produced by using the same

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