CN103865005A - Water-soluble comb-like polymer and synthesis method thereof - Google Patents

Water-soluble comb-like polymer and synthesis method thereof Download PDF

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CN103865005A
CN103865005A CN201410024128.1A CN201410024128A CN103865005A CN 103865005 A CN103865005 A CN 103865005A CN 201410024128 A CN201410024128 A CN 201410024128A CN 103865005 A CN103865005 A CN 103865005A
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water
soluble comb
aqueous solution
acid
soluble
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CN103865005B (en
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陈杰
杨国武
方世昌
皮永奇
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Guizhou shiboshi Technology Co.,Ltd.
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GUIZHOU DRSHI TECHNOLOGY Ltd
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Abstract

The invention relates to a water reducing agent for concrete and a synthesis method thereof, and specifically relates to a water-soluble comb-like polymer and a synthesis method thereof. The synthesis method of the water-soluble comb-like polymer comprises the following steps: preparing materials, blending materials, dropwise adding, curing and neutralizing. The water-soluble comb-like polymer prepared by the synthesis method is characterized in that the main chain of the polymer is polymerized from vinyl carboxylic acids such as acrylic acid and methylacrylic acid, while the side chain of the same is constructed by a water-soluble linear urea resin; the polymer is simple in synthesis process, has excellent cement dispersibility and can be taken as a novel concrete water reducing agent.

Description

A kind of water-soluble comb-shaped polymer and synthetic method
Technical field
The present invention relates to the reinforcement of concrete water reducer and synthetic method, specifically, relate to a kind of water-soluble comb-shaped polymer and synthetic method.
Background technology
Concrete admixture refers to and mixes in concrete, is not more than cement quality 5%, and can improve on request or improve the additive of concrete mixture characteristic or properties of hardened concrete.In concrete admixture, usage quantity maximum be water reducer, it can be in the water consumption that ensures significantly reduce under the prerequisite of normal construction concrete mix, thereby improves concrete strength, reduces folk prescription concrete cement consumption, reduces costs.According to market statistics, water reducer accounts for 70%~80% of concrete admixture total amount on market.
According to size and the raw material sources etc. of the development course of water reducer, water-reducing rate, generally water reducer product is divided into three generations: first-generation called after ordinary water-reducing agent, taking calcium lignin sulphonate, sodium lignosulfonate as representative, comprise Weibull, brown coal etc., water-reducing rate is less than 10%; The s-generation is referred to as high efficiency water reducing agent, and water-reducing rate is greater than 18%, taking naphthalene series high-efficiency water-reducing agent as representative, comprises sulfamate water reducer, melmac water reducer, aliphatic water reducing agent etc.; Third generation water reducer is called after high-performance water reducing agent in GB8076-2008, and water-reducing rate is greater than 25%, because its currently available products is polycarboxylate series products, is called again high performance water reducing agent of polyocarboxy acid.This three generations's water reducer respectively has performance characteristics, has application in the market.
Compared with the first-generation, s-generation water reducer, polycarboxylic acid series high efficiency water reducing agent has advantages of following outstanding: to the dispersed ability of cement is stronger, higher, the concrete Slump Time losing of Large of water-reducing rate is less, concrete wraps, workability good, high-grade concrete viscosity is little; Concrete gain in strength is large, shrink little, impervious good, resistance to corrosion is strong.In addition, polycarboxylate water-reducer itself not contains sodium sulfate, containing ammonia, containing formaldehyde, without chlorine, alkali-free almost.Therefore, can say, polycarboxylate water-reducer is high performance modern water reducer product truly.At present, high-grade concrete on market, self-leveling concrete, overlength pump concrete, maritime concrete, concrete for railway, concrete for airport, for highway, concrete, water resources dam, water power all use polycarboxylate water-reducer configuration with concrete etc., by statistics in 2013, normal concrete used poly carboxylic acid to exceed 50%.
The large monomer difference using according to polycarboxylate water-reducer, high performance water reducing agent of polyocarboxy acid can be subdivided into again: 1, ester class high performance water reducing agent of polyocarboxy acid, the large monomer of use is methacrylic acid, polyalkylene glycol acrylate monomethyl ether ester); 2, ethers high performance water reducing agent of polyocarboxy acid, the large monomer of use is vinyl carbinol polyglycol ether, methallyl alcohol polyglycol ether, prenol polyglycol ether etc.By these large monomers, we can find out, existing polycarboxylic acid series high efficiency water reducing agent side chain is polyoxyethylene, and different is only the on-link mode (OLM) of polyoxyethylene and main chain.
Abroad Japan to high performance water reducing agent of polyocarboxy acid research and application country the earliest.As catalyst company, flower king, wheat think of top grade have had polycarboxylate water-reducer product very early.The Chinese patent that relates to polycarboxylate water-reducer of Nippon Shokubai Co., Ltd's application has CN97126334, CN97126334, CN99127479, CN200580023517, CN200410033714, CN200610071910, CN200610071910, CN200980117278 etc., and these patents have comprised many poly carboxylic acid and synthesized and compounded technology.Korea S is also polycarboxylate water-reducer research and application country early, as LG chemistry, Qing Dou Co., Ltd. etc., almost all uses polycarboxylate water-reducer to Korea S in 2006 except solid water reducer.The ground recent two decades such as America and Europe come the research of carboxylic acid water reducing agent aspect always more deep, and the use of poly carboxylic acid is more extensive, and the Chinese patent of application has the CN200880111132 of BASF AG, the CN201080005070 of W. R. Grace & Co etc.
The middle and later periods nineties 20th century, the novel water reducer that more domestic colleges and universities, institute etc. at the non-naphthalene of research are all.Although the actual quantity that domestic relevant article is delivered is many, few in aspect researchs such as the impacts of the mechanism of action, Water-reducing Admixtures To Cements aquation and slurry microstructure, only in the academic dissertation of some colleges and universities, slightly inquire into.Synthetic product also mainly rests on laboratory stage, also has suitable distance from suitability for industrialized production.After 2005, the domestic research boom that rises polycarboxylate water-reducer, many investigators constantly explore the synthetic method of high-performance water reducing agent by molecular designing approach, the development research of polycarboxylate high performance water-reducing agent makes great progress, in Beijing, Shanghai, suitability for industrialized production has been realized on the ground such as Jiangsu and Zhejiang Provinces, as Shanghai architecture science research institute, Architecture Science Inst. of Jiangsu Prov., Shandong architecture science research institute, Chinese Research Institute for Building Sciences etc., the patent of application has China Building Material Scientific Research General Institute CN200910077550 in recent years, CN200910077550, Beijing Architectural Engineering Inst CN200810134808, the CN200810134808 of Architecture Science Inst. of Jiangsu Prov., CN200710190296, CN200710190295, CN200710190297, CN200710190297, CN200710190296, CN200710131423, CN200710131423, CN200710024393, CN200710024393 etc.
Summary of the invention
The object of the invention is to, it is to be polymerized by the vinyl carboxylic acid such as vinylformic acid, methacrylic acid that a kind of main chain is provided, and side chain is water-soluble comb-shaped polymer and the synthetic method of water-soluble linear urea-formaldehyde resin.
The present invention is achieved through the following technical solutions:
A kind of water-soluble comb-shaped polymer, is characterized in that: this polymer repeat unit and molecular formula can be represented by following general formula:
Figure 309489DEST_PATH_IMAGE001
Wherein R 1for H or CH 3, m=40~45, n=15~20, L=10~15.
The synthetic method of described water-soluble comb-shaped polymer, comprises the steps:
1, get the raw materials ready: liquid caustic soda and water that the macromonomer aqueous solution, initiator, chain-transfer agent, minor comonomer, the concentration that concentration is 50% is 30%, the mass percent of above-mentioned various raw materials is respectively: the macromonomer aqueous solution 62%, initiator 0.25%-0.3%, chain-transfer agent 0.2%-0.42%, minor comonomer 3.4%-4%, liquid caustic soda 6%, surplus are water;
2, batching
2A, in conversion unit, add the macromonomer aqueous solution, open and stir, and be warming up to 60 DEG C-85 DEG C, stand-by;
2B, be equivalent by moisture two parts, a copy of it and initiator fully dissolve, and the solution of making adds in a dropping equipment; Another part fully dissolves with chain-transfer agent and minor comonomer, and the solution of making joins in No. two dropping equipment;
It should be noted that: in blending process, accurate measurement, the solution in the solution in a dropping equipment and No. two dropping equipment can not be in contact with one another, if be in contact with one another, also can react even if temperature is very low, causes end product quality variation; In addition, temperature will be controlled at design temperature ± 2 DEG C;
3, drip
Solution in solution in a dropping equipment and No. two dropping equipment is at the uniform velocity added drop-wise in conversion unit simultaneously, time for adding is 3 hours, ensure that, after 3 hours, the material in the material in a dropping equipment and No. two dropping equipment is all added drop-wise in conversion unit; In dropping process, temperature maintains 60 DEG C-85 DEG C;
4, slaking: after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
5, neutralization: be cooled to 45 DEG C, to conversion unit, time for adding 20 minutes, ensures that after 20 minutes, liquid caustic soda is all added drop-wise in conversion unit by slow liquid caustic soda underframe.
say further:
The described macromonomer aqueous solution is the double bond containing water-soluble linear urea-formaldehyde resin of the end group oligopolymer aqueous solution, and the repeating unit of this oligopolymer and molecular formula are:
Figure 570706DEST_PATH_IMAGE002
, wherein, n=10-15.
Described initiator is ammonium persulphate, Sodium Persulfate or Potassium Persulphate, and wherein, ammonium persulphate decomposition temperature is minimum, decomposition rate is the fastest, and Sodium Persulfate takes second place, and Potassium Persulphate decomposition temperature is the highest, decomposition rate is the slowest.
Described chain-transfer agent is sodium allyl sulfonate, methallylsulfonic acid sodium, Thiovanic acid or thiohydracrylic acid, and their chain transfer activity raises according to above-mentioned order, and consumption successively reduces.
Described minor comonomer is acrylic or methacrylic acid.
beneficial effect:the water-soluble comb-shaped polymer that adopts the present invention to prepare, main chain is to be polymerized by the vinyl carboxylic acid such as vinylformic acid, methacrylic acid, and side chain is water-soluble linear urea-formaldehyde resin, and the synthesis technique of this polymkeric substance is simple, there is good cement dispersiveness, can be as a kind of novel cement water reducing agent.
Embodiment
Below with reference to specific embodiment, the present invention is described further.
embodiment 1
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.5g ammonium persulphate and 140g water, stirring and dissolving; B expects configuration: in another 250ml beaker, add 2g thiohydracrylic acid, 34g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 2
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.5g ammonium persulphate and 140g water, stirring and dissolving.B expects configuration: in another 250ml beaker, add 2.5g Thiovanic acid, 34g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 3
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.5g ammonium persulphate and 140g water, stirring and dissolving; B expects configuration: in another 250ml beaker, add 3.66g methallylsulfonic acid sodium, 34g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 4
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.5g ammonium persulphate and 140g water, stirring and dissolving.B expects configuration: in another 250ml beaker, add 4.2g sodium allyl sulfonate, 36g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 5
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 70~75 DEG C;
A expects configuration: in a 250ml beaker, add 2.7g Sodium Persulfate and 140g water, stirring and dissolving.B expects configuration: in another 250ml beaker, add 3.89g methallylsulfonic acid sodium, 40g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 6
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 70~75 DEG C;
A expects configuration: in a 250ml beaker, add 2.7g Sodium Persulfate and 140g water, stirring and dissolving.B expects configuration: in another 250ml beaker, add 4.2g sodium allyl sulfonate, 40g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 7
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 80~85 DEG C;
A expects configuration: in a 250ml beaker, add 3.0g Potassium Persulphate and 140g water, stirring and dissolving; B expects configuration: in another 250ml beaker, add 4.2g sodium allyl sulfonate, 40g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 4.5 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
embodiment 8
1, in the there-necked flask that is 1000ml at capacity, adding 620g concentration is the urea-formaldehyde resin oligopolymer aqueous solution of 50% acrylamide end-blocking, opens and stirs, and is warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.5g ammonium persulphate and 140g water, stirring and dissolving; B expects configuration: in another 250ml beaker, add 2g thiohydracrylic acid, 30g vinylformic acid, 10g methyl-prop diluted acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
comparative example 1
1, in the there-necked flask that is 1000ml at capacity, add 310g methacrylic Soxylat A 25-7 (molecular weight 2400) and water 310g, open and stir, dissolve, be warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.8g ammonium persulphate and 140g water, stirring and dissolving; B expects configuration: in another 250ml beaker, add 4.0g methallylsulfonic acid sodium, 40g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
comparative example 2
1, in the there-necked flask that is 1000ml at capacity, add 310g isopentene group Soxylat A 25-7 (molecular weight 2400) and water 310g, open and stir, dissolve, be warming up to 60~65 DEG C;
A expects configuration: in a 250ml beaker, add 2.8g ammonium persulphate and 140g water, stirring and dissolving; B expects configuration: in another 250ml beaker, add 2.4g thiohydracrylic acid, 40g vinylformic acid and 140g water, stirring and dissolving;
2, in there-necked flask, drip A material and B material simultaneously, within 3 hours, drip off, in dropping process, holding temperature is constant;
3, after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
4, be cooled to 45 DEG C, adding concentration is 30% sodium hydroxide 60g, slowly drips, and within 20 minutes, drips off.
[the dispersed experiment of cement]
The product of embodiment 1~7 product and comparative example 1~2 is configured to respectively to 10% solution, by 2% of cement mixing content, only starches experiment according to GB8076-2008 making cement.
Cement: standard cement, consumption 300g;
Water: deionized water, consumption 81g;
Admixture: 6g.
Dispersed experimental result is as shown in the table:
Flowing degree of net paste of cement
Sample Comparative example 1 Comparative example 2 Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4 Embodiment 5 Embodiment 6 Embodiment 7 Embodiment 8
Degree of mobilization/mm 240 260 255 250 255 220 230 210 200 210

Claims (6)

1. a water-soluble comb-shaped polymer, is characterized in that: this polymer repeat unit and molecular formula can be represented by following general formula:
Figure 158821DEST_PATH_IMAGE001
Wherein R 1for H or CH 3, m=40~45, n=15~20, L=10~15.
2. the synthetic method of water-soluble comb-shaped polymer as claimed in claim 1, is characterized in that: comprise the steps:
(1) get the raw materials ready: liquid caustic soda and water that the macromonomer aqueous solution, initiator, chain-transfer agent, minor comonomer, the concentration that concentration is 50% is 30%, the mass percent of above-mentioned various raw materials is respectively: the macromonomer aqueous solution 62%, initiator 0.25%-0.3%, chain-transfer agent 0.2%-0.42%, minor comonomer 3.4%-4%, liquid caustic soda 6%, surplus are water;
(2) batching
(2A) in conversion unit, add the macromonomer aqueous solution, open and stir, and be warming up to 60 DEG C-85 DEG C, stand-by;
(2B) be equivalent by moisture two parts, a copy of it and initiator fully dissolve, and the solution of making adds in a dropping equipment; Another part fully dissolves with chain-transfer agent and minor comonomer, and the solution of making joins in No. two dropping equipment;
(3) drip
Solution in solution in a dropping equipment and No. two dropping equipment is at the uniform velocity added drop-wise in conversion unit simultaneously, time for adding is 3 hours, ensure that, after 3 hours, the material in the material in a dropping equipment and No. two dropping equipment is all added drop-wise in conversion unit; In dropping process, temperature maintains 60 DEG C-85 DEG C;
(4) slaking: after being added dropwise to complete, holding temperature is constant, insulation slaking 1 hour;
(5) neutralization: be cooled to 45 DEG C, to conversion unit, time for adding 20 minutes, ensures that after 20 minutes, liquid caustic soda is all added drop-wise in conversion unit by slow liquid caustic soda underframe.
3. the synthetic method of water-soluble comb-shaped polymer according to claim 2, is characterized in that: the described macromonomer aqueous solution is the double bond containing water-soluble linear urea-formaldehyde resin of the end group oligopolymer aqueous solution, and the repeating unit of this oligopolymer and molecular formula are:
Figure 981283DEST_PATH_IMAGE002
Wherein, n=10-15.
4. the synthetic method of water-soluble comb-shaped polymer according to claim 2, is characterized in that: described initiator is ammonium persulphate, Sodium Persulfate or Potassium Persulphate.
5. the synthetic method of water-soluble comb-shaped polymer according to claim 2, is characterized in that: described chain-transfer agent is sodium allyl sulfonate, methallylsulfonic acid sodium, Thiovanic acid or thiohydracrylic acid.
6. the synthetic method of water-soluble comb-shaped polymer according to claim 2, is characterized in that: described minor comonomer is acrylic or methacrylic acid.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111019060A (en) * 2019-12-12 2020-04-17 贵州师范学院 Preparation method of tannic acid base star-shaped polycarboxylate superplasticizer
CN116063685A (en) * 2022-12-16 2023-05-05 西南林业大学 Comb-shaped hyperbranched amino copolycondensation resin and preparation method thereof

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CN102199298A (en) * 2011-03-23 2011-09-28 中国日用化学工业研究院 Preparation method for polycarboxylic acid series comb-shaped surface active agent
CN103613306A (en) * 2013-11-18 2014-03-05 济南大学 Hyperbranched poly(amine-ester) structure-containing polycarboxylic water reducer and preparation method thereof

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Publication number Priority date Publication date Assignee Title
CN1702087A (en) * 2005-06-21 2005-11-30 重庆大学 Polyacrylic acid salts shrinkage-reducing-agent and method for making same
CN102199298A (en) * 2011-03-23 2011-09-28 中国日用化学工业研究院 Preparation method for polycarboxylic acid series comb-shaped surface active agent
CN103613306A (en) * 2013-11-18 2014-03-05 济南大学 Hyperbranched poly(amine-ester) structure-containing polycarboxylic water reducer and preparation method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111019060A (en) * 2019-12-12 2020-04-17 贵州师范学院 Preparation method of tannic acid base star-shaped polycarboxylate superplasticizer
CN116063685A (en) * 2022-12-16 2023-05-05 西南林业大学 Comb-shaped hyperbranched amino copolycondensation resin and preparation method thereof
CN116063685B (en) * 2022-12-16 2023-10-20 西南林业大学 Comb-shaped hyperbranched amino copolycondensation resin and preparation method thereof

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