CN105330793B - A kind of preparation method of ethers polycarboxylic acid water reducing agent - Google Patents

A kind of preparation method of ethers polycarboxylic acid water reducing agent Download PDF

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CN105330793B
CN105330793B CN201510831545.1A CN201510831545A CN105330793B CN 105330793 B CN105330793 B CN 105330793B CN 201510831545 A CN201510831545 A CN 201510831545A CN 105330793 B CN105330793 B CN 105330793B
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reducing agent
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CN105330793A (en
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方云辉
柯余良
张小芳
曾贤华
吴银财
郑荣平
李格丽
林倩
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Kezhijie New Material Group Guangxi Co ltd
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Abstract

The invention discloses a kind of preparation method of ethers polycarboxylic acid water reducing agent.Comprise the following steps:(1) unsaturated polyether, acrylic acid, unsaturated sulfonic acid salt, paraffin, disodium EDTA and water are added in reactor, stirs lower dissolving, be configured to react bed material, the maintaining nitrogen purge under the liquid level of reaction bed material, while be warming up to 30~40 DEG C;(2) hydrogen peroxide is disposably added in step (1) resulting material, the first mixed solution and the second mixed solution are added dropwise simultaneously, control rate of addition, time for adding is 1~2.5h, after being added dropwise, reaction system is warming up to 50~60 DEG C, the disposable hydrogen peroxide that adds continues to react, (3) SDD is added in step (2) resulting material with terminating reaction, and add sodium hydroxide solution and neutralized, 40~50 DEG C are cooled to, discharging, obtains ethers polycarboxylic acid water reducing agent.The preparation method of the present invention is advantageous to avoid gel from generating, while can greatly improve the bin stability of obtained polycarboxylate water-reducer.

Description

A kind of preparation method of ethers polycarboxylic acid water reducing agent
Technical field
The invention belongs to building material technical field, and in particular to a kind of preparation method of ethers polycarboxylic acid water reducing agent.
Background technology
It is various industry with civil buildings, road and rail bridge, airfield runway, mine construction, hydro-structure, ocean development, The construction of many engineerings such as geothermal engineering and military affairs all be unable to do without concrete.At present, as concrete is to high performance and more The direction of functionalization is developed, it is desirable to which concrete has high workability, high intensity, high-durability, and can meet in many special feelings Application under condition.Polycarboxylate water-reducer with ultra-dispersed performance oneself turn into high performance concrete in indispensable component.
Polycarboxylate water-reducer contains the functional groups such as carboxylic acid group, sulfonic group, ester group, in the molecular binding process of polymer, Different monomers make molecule have comb-type structure with random or regularly condense together, and it is excellent for its special structures shape More performance.Polycarboxylate water-reducer can cut out design principle according to polymer molecule, can be gathered by free radical copolymerization Close construction unit synthesis predetermined structure and performance water reducer, by adjust monomer component and its between proportionate relationship, choose High reaction activity monomer and initiator etc., main chain, the side chain containing preferable molecular structure that can meet specific demand are finally given, And make it have the polymer of certain charge density and molecular conformation molecular structure.
In the correlative study of polycarboxylate water-reducer, numerous enterprises and R&D institution are primarily upon carrying for polycarboxylic acids performance The lifting of liter or cost performance, or the functionalized design of product, and the research for polycarboxylate water-reducer production process is less.It is poly- The synthesis of carboxylic acid water reducer is typically polymerize using aqueous free radical, during the course of the reaction with the consumption of reaction monomers, monomer The raising of conversion ratio, the viscosity of system also increase therewith, i.e. the molecular weight of product gradually steps up, and due to reaction system mass transfer The heterogencity of heat transfer, cause sudden and violent poly- phenomenon may locally occur in system, therefore gelatin phenomenon can be caused to occur, actual production During particularly be very easy to agglomerate gel occur on kettle wall and agitating paddle, often cause reactor discharging opening and product The blocking of pipeline in course of conveying.
The content of the invention
It is an object of the invention to overcome prior art defect, there is provided a kind of preparation method of ethers polycarboxylic acid water reducing agent.
The concrete technical scheme of the present invention is as follows:
A kind of preparation method of ethers polycarboxylic acid water reducing agent, comprises the following steps:
(1) by 100 parts by weight unsaturated polyethers, 2~11 parts by weight of acrylic acid, 1~6 parts by weight unsaturated sulfonic acid salt, 0.01~0.6 parts by weight paraffin, 1~6 parts by wt EDTA-disodium salt and 50 parts by weight water are added in reactor, stirring Lower dissolving, it is configured to react bed material, 12~20min of maintaining nitrogen purge under the liquid level of reaction bed material, while is warming up to 30~40 ℃;Above-mentioned unsaturated polyether is methacrylic polyoxyethylene ether or isopentene group polyoxyethylene ether;
(2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, disposably add 1~6 weight Part hydrogen peroxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding is 1~2.5h, After being added dropwise, reaction system is warming up to 50~60 DEG C, 0.2~1.0 parts by weight hydrogen peroxide is disposably added and continues to react, Reaction time is 0.8~1.2h;Wherein the first mixed solution is by 4~11 parts by weight unsaturated carboxylic acids, 1~6 parts by weight pi-allyl Thiocarbamide, 0.2~1.5 parts by weight chain-transferring agent and 30 parts by weight water are formulated, and the second mixed solution is by 0.05~1.2 parts by weight Reducing agent, 0.05~0.6 parts by weight help reducing agent tetramethylethylenediamine and 30 parts by weight water to be formulated;
(3) 0.01~0.06 parts by weight SDD is added in step (2) resulting material with end Only react, and add the sodium hydroxide solution that 8~22 parts by weight mass concentrations are 30% and neutralized, be cooled to 40~50 DEG C, Discharging, obtains ethers polycarboxylic acid water reducing agent.
In a preferred embodiment of the invention, the step (1) is:By 100 parts by weight unsaturated polyethers, 3~ 10 parts by weight of acrylic acid, 1~5 parts by weight unsaturated sulfonic acid salt, 0.01~0.5 parts by weight paraffin, 1~5 parts by weight ethylenediamine tetraacetic Acetic acid disodium salt and 50 parts by weight water are added in reactor, stir lower dissolving, are configured to react bed material, in the liquid level of reaction bed material Lower maintaining nitrogen purge 15min, while it is warming up to 30~40 DEG C.
In a preferred embodiment of the invention, the step (2) is:Under the liquid level of step (1) resulting material Maintaining nitrogen purge, and continuously stir, 1~5 parts by weight hydrogen peroxide is disposably added, while the first mixed solution and second is added dropwise Mixed solution, rate of addition being controlled, time for adding is 1~2h, and after being added dropwise, reaction system is warming up into 50~60 DEG C, one Secondary property adds 0.2~0.8 parts by weight hydrogen peroxide and continues to react, reaction time 1h.
In a preferred embodiment of the invention, the step (3) is:Added in step (2) resulting material 0.01~0.05 parts by weight SDD is added 10~20 parts by weight mass concentrations and is with terminating reaction 30% sodium hydroxide solution is neutralized, and is cooled to 45 DEG C, discharging, is obtained ethers polycarboxylic acid water reducing agent.
It is further preferred that the unsaturated sulfonic acid salt is 2- hydroxyl -3- allyloxys propanesulfonate, 2- hydroxyl -3- alkene Propoxyl group propane sulfonic acid potassium, 2- hydroxyl -4- alkene butoxy propanesulfonates or 2- hydroxyl -4- alkene butoxy propane sulfonic acid potassium.
It is further preferred that the unsaturated carboxylic acid is acrylic acid, methyl acrylate, ethyl acrylate, acrylic acid hydroxyl first At least one of ester, hydroxy-ethyl acrylate and itaconic acid.
It is further preferred that the chain-transferring agent is mercaptoethanol, TGA or mercaptopropionic acid.
It is further preferred that the reducing agent is 2- hydroxyls -2- sulfinatoacetic acids di-potassium or 2- hydroxyl -2- sulfonic groups Acetic acid di-potassium.
The beneficial effects of the invention are as follows:
1st, preparation method of the invention is advantageous to avoid gel from generating:Before adding reaction monomers, it is passed through nitrogen and removes dereaction Air in kettle, to provide the oxygen-free environment of polymerisation;Paraffin is added in reaction, can reduce or prevent attachment of polymers as far as possible On the reactor part such as kettle wall or agitating paddle;The unsaturated sulfonic acid of introducing, contain three functional groups in its structure, be a kind of high Hydrophilic functional monomer is spent, the hydrophily of polymer can be increased, is advantageous to avoid the generation of gelatinous mass.
2nd, preparation method of the invention can greatly improve the bin stability of obtained polycarboxylate water-reducer, will not produce Raw gel or white gels shape floating object:Introduced allylthiourea, the group with anti-oxidation function, product can be prevented Crosslinking and degraded, can improve the service efficiencies of antioxidant groups, due between antioxidant group and main polymer chain by covalent Key is bonded, and is not in separation effect;The SDD added can be with the chain that is remained in reaction system Radical reaction, chain free radical activity is set to disappear so that reaction terminating.
Embodiment
Technical scheme is further detailed and described below by way of embodiment.
Embodiment 1
(1) by 100 parts by weight methacrylic polyoxyethylene ethers, 5 parts by weight of acrylic acid, 1 parts by weight 2- hydroxyl -3- alkene Propoxyl group propanesulfonate, 0.01 parts by weight paraffin, 1 parts by wt EDTA-disodium salt and 50 parts by weight water add reactor In, lower dissolving is stirred, is configured to react bed material, the maintaining nitrogen purge 15min under the liquid level of reaction bed material, while be warming up to 40 ℃;
(2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, it is disposable to add 4 parts by weight mistakes Hydrogen oxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding 2h, is added dropwise Afterwards, reaction system is warming up to 55 DEG C, the disposable 0.8 parts by weight hydrogen peroxide that adds continues to react, reaction time 1h;Wherein First mixed solution is matched somebody with somebody by 5 parts by weight of acrylic acid, 3 parts by weight allylthioureas, 0.2 parts by weight mercaptoethanol and 30 parts by weight water System forms, and the second mixed solution helps reducing agent tetramethyl by 1 parts by weight 2- hydroxyl -2- sulfinatoacetic acids di-potassium, 0.5 parts by weight Base ethylenediamine and 30 parts by weight water are formulated;
(3) 0.01 parts by weight SDD is added in step (2) resulting material with terminating reaction, And add the sodium hydroxide solution that 13 parts by weight mass concentrations are 30% and neutralized, 45 DEG C are cooled to, discharging, ethers is obtained and gathers Carboxylic acid water reducer.
Embodiment 2
(1) by 100 parts by weight isopentene group polyoxyethylene ethers, 8 parts by weight of acrylic acid, 2 parts by weight 2- hydroxyl -3- allyls Epoxide propane sulfonic acid potassium, 0.01 parts by weight paraffin, 4 parts by wt EDTA-disodium salt and 50 parts by weight water add reactor In, lower dissolving is stirred, is configured to react bed material, the maintaining nitrogen purge 15min under the liquid level of reaction bed material, while be warming up to 30 ℃;
(2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, it is disposable to add 2 parts by weight mistakes Hydrogen oxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding 2h, is added dropwise Afterwards, reaction system is warming up to 55 DEG C, the disposable 0.5 parts by weight hydrogen peroxide that adds continues to react, reaction time 1h;Wherein First mixed solution is by 4 parts by weight of acrylic acid, 1 parts by weight of acrylic acid hydroxyl ethyl ester, 1 parts by weight allylthiourea, 0.4 parts by weight mercapto Base ethanol and 30 parts by weight water are formulated, and the second mixed solution is by 0.4 parts by weight 2- hydroxyl -2- sulfinatoacetic acid dipotassiums Salt, 0.5 parts by weight help reducing agent tetramethylethylenediamine and 30 parts by weight water to be formulated;
(3) 0.04 parts by weight SDD is added in step (2) resulting material with terminating reaction, And add the sodium hydroxide solution that 17 parts by weight mass concentrations are 30% and neutralized, 45 DEG C are cooled to, discharging, ethers is obtained and gathers Carboxylic acid water reducer.
Embodiment 3
(1) by 100 parts by weight isopentene group polyoxyethylene ethers, 3 parts by weight of acrylic acid, 3 parts by weight 2- hydroxyl -4- alkene fourths Epoxide propanesulfonate, 0.5 parts by weight paraffin, 4 parts by wt EDTA-disodium salt and 50 parts by weight water are added in reactor, Stirring is lower to dissolve, and is configured to react bed material, the maintaining nitrogen purge 15min under the liquid level of reaction bed material, while be warming up to 40 DEG C;
(2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, it is disposable to add 1 parts by weight mistake Hydrogen oxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding 1h, is added dropwise Afterwards, reaction system is warming up to 60 DEG C, the disposable 0.5 parts by weight hydrogen peroxide that adds continues to react, reaction time 1h;Wherein First mixed solution is by 3 parts by weight of acrylic acid, 7 parts by weight itaconic acids, 1 parts by weight allylthiourea, 1.2 parts by weight TGAs It is formulated with 30 parts by weight water, the second mixed solution is by 1 parts by weight 2- hydroxyl -2- sulfinatoacetic acids di-potassium, 0.05 weight Amount part helps reducing agent tetramethylethylenediamine and 30 parts by weight water to be formulated;
(3) 0.02 parts by weight SDD is added in step (2) resulting material with terminating reaction, And add the sodium hydroxide solution that 10 parts by weight mass concentrations are 30% and neutralized, 45 DEG C are cooled to, discharging, ethers is obtained and gathers Carboxylic acid water reducer.
Embodiment 4
(1) by 100 parts by weight methacrylic polyoxyethylene ethers, 10 parts by weight of acrylic acid, 5 parts by weight 2- hydroxyls -4- Alkene butoxy propane sulfonic acid potassium, 0.1 parts by weight paraffin, 5 parts by wt EDTA-disodium salt and 50 parts by weight water add reaction In kettle, lower dissolving is stirred, is configured to react bed material, the maintaining nitrogen purge 15min under the liquid level of reaction bed material, while be warming up to 35 ℃;
(2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, it is disposable to add 5 parts by weight mistakes Hydrogen oxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding 1h, is added dropwise Afterwards, reaction system is warming up to 50 DEG C, the disposable 0.2 parts by weight hydrogen peroxide that adds continues to react, reaction time 1h;Wherein First mixed solution is by 2 parts by weight of acrylic acid, 2 parts by weight of acrylic acid hydroxyl ethyl esters, 1 parts by weight itaconic acid, 5 parts by weight allyl sulfides Urea, 0.5 parts by weight mercaptopropionic acid and 30 parts by weight water are formulated, and the second mixed solution is by 0.05 parts by weight 2- hydroxyl -2- sulphurs Acidic group acetic acid di-potassium, 0.1 parts by weight help reducing agent tetramethylethylenediamine and 30 parts by weight water to be formulated;
(3) 0.05 parts by weight SDD is added in step (2) resulting material with terminating reaction, And add the sodium hydroxide solution that 20 parts by weight mass concentrations are 30% and neutralized, 45 DEG C are cooled to, discharging, ethers is obtained and gathers Carboxylic acid water reducer.
Embodiment 1~4 does not find gel on reactor wall and agitating paddle after the completion of reaction;Gained polycarboxylic acids diminishing Agent is stored 12 months at normal temperatures, is not also found gel or white gels shape floating object, is had no hydraulic performance decline.
The product of the gained of embodiment 1~4 use into reference cement P.I 42.5, sand is the river sand of modulus of fineness 2.8, stone For particle diameter 5-20 continuous grading rubbles.According to GB 8076-2008《Concrete admixture》, determine concrete water-reducing ratio, additive Volume is 0.20% (being converted into solid part) of glue material quality, and the concrete water-reducing ratio of the sample of embodiment 1~4 is 30% after tested More than.
Those of ordinary skill in the art understand, when constituent content of the invention changes in following ranges, remain to access Same as the previously described embodiments or similar technique effect, still falls within protection scope of the present invention:
(1) by 100 parts by weight unsaturated polyethers, 2~11 parts by weight of acrylic acid, 1~6 parts by weight unsaturated sulfonic acid salt, 0.01~0.6 parts by weight paraffin, 1~6 parts by wt EDTA-disodium salt and 50 parts by weight water are added in reactor, stirring Lower dissolving, it is configured to react bed material, 12~20min of maintaining nitrogen purge under the liquid level of reaction bed material, while is warming up to 30~40 ℃;Above-mentioned unsaturated polyether is methacrylic polyoxyethylene ether or isopentene group polyoxyethylene ether;
(2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, disposably add 1~6 weight Part hydrogen peroxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding is 1~2.5h, After being added dropwise, reaction system is warming up to 50~60 DEG C, 0.2~1.0 parts by weight hydrogen peroxide is disposably added and continues to react, Reaction time is 0.8~1.2h;Wherein the first mixed solution is by 4~11 parts by weight unsaturated carboxylic acids, 1~6 parts by weight pi-allyl Thiocarbamide, 0.2~1.5 parts by weight chain-transferring agent and 30 parts by weight water are formulated, and the second mixed solution is by 0.05~1.2 parts by weight Reducing agent, 0.05~0.6 parts by weight help reducing agent tetramethylethylenediamine and 30 parts by weight water to be formulated;
(3) 0.01~0.06 parts by weight SDD is added in step (2) resulting material with end Only react, and add the sodium hydroxide solution that 8~22 parts by weight mass concentrations are 30% and neutralized, be cooled to 40~50 DEG C, Discharging, obtains ethers polycarboxylic acid water reducing agent.
The unsaturated sulfonic acid salt is 2- hydroxyl -3- allyloxys propanesulfonate, 2- hydroxyl -3- allyloxy propane sulfonic acid Potassium, 2- hydroxyl -4- alkene butoxy propanesulfonates or 2- hydroxyl -4- alkene butoxy propane sulfonic acid potassium.
The unsaturated carboxylic acid is acrylic acid, methyl acrylate, ethyl acrylate, acrylate, acrylic acid hydroxyl second At least one of ester and itaconic acid.
The chain-transferring agent is mercaptoethanol, TGA or mercaptopropionic acid.
The reducing agent is 2- hydroxyls -2- sulfinatoacetic acids di-potassium or 2- hydroxyl -2- sulfonatoacetic acid di-potassiums.
The foregoing is only a preferred embodiment of the present invention, therefore can not limit the scope that the present invention is implemented according to this, i.e., The equivalent changes and modifications made according to the scope of the claims of the present invention and description, all should still it belong in the range of the present invention covers.

Claims (7)

  1. A kind of 1. preparation method of ethers polycarboxylic acid water reducing agent, it is characterised in that:Comprise the following steps:
    (1) by 100 parts by weight unsaturated polyethers, 2~11 parts by weight of acrylic acid, 1~6 parts by weight unsaturated sulfonic acid salt, 0.01~ 0.6 parts by weight paraffin, 1~6 parts by wt EDTA-disodium salt and 50 parts by weight water are added in reactor, molten under stirring Solution, it is configured to react bed material, 12~20min of maintaining nitrogen purge under the liquid level of reaction bed material, while is warming up to 30~40 DEG C;On It is methacrylic polyoxyethylene ether or isopentene group polyoxyethylene ether to state unsaturated polyether;
    (2) maintaining nitrogen purge under the liquid level of step (1) resulting material, and continuously stir, disposably add 1~6 parts by weight mistake Hydrogen oxide, while the first mixed solution and the second mixed solution is added dropwise, rate of addition is controlled, time for adding is 1~2.5h, is added dropwise After, reaction system is warming up to 50~60 DEG C, 0.2~1.0 parts by weight hydrogen peroxide is disposably added and continues to react, react Time is 0.8~1.2h;Wherein the first mixed solution is by 4~11 parts by weight of acrylic acid, methyl acrylate, ethyl acrylate, third At least one of olefin(e) acid hydroxyl methyl esters, hydroxy-ethyl acrylate and itaconic acid, 1~6 parts by weight allylthiourea, 0.2~1.5 weight Part chain-transferring agent and 30 parts by weight water are formulated, and the second mixed solution is by 0.05~1.2 parts by weight reducing agent, 0.05~0.6 Parts by weight help reducing agent tetramethylethylenediamine and 30 parts by weight water to be formulated;
    (3) it is anti-to terminate that 0.01~0.06 parts by weight SDD is added in step (2) resulting material Should, and add the sodium hydroxide solution that 8~22 parts by weight mass concentrations are 30% and neutralized, 40~50 DEG C are cooled to, is discharged, Obtain ethers polycarboxylic acid water reducing agent.
  2. A kind of 2. preparation method of ethers polycarboxylic acid water reducing agent as claimed in claim 1, it is characterised in that:The step (1) For:By 100 parts by weight unsaturated polyethers, 3~10 parts by weight of acrylic acid, 1~5 parts by weight unsaturated sulfonic acid salt, 0.01~0.5 weight Measure part paraffin, 1~5 parts by wt EDTA-disodium salt and 50 parts by weight water to add in reactor, stir lower dissolving, prepare Into reaction bed material, the maintaining nitrogen purge 15min under the liquid level of reaction bed material, while it is warming up to 30~40 DEG C.
  3. 3. preparation method as claimed in claim 1, it is characterised in that:The step (2) is:In step (1) resulting material Maintaining nitrogen purge under liquid level, and continuously stir, 1~5 parts by weight hydrogen peroxide is disposably added, while the first mixed solution is added dropwise With the second mixed solution, rate of addition is controlled, time for adding is 1~2h, and after being added dropwise, reaction system is warming up into 50~60 DEG C, disposably add 0.2~0.8 parts by weight hydrogen peroxide and continue to react, reaction time 1h.
  4. 4. preparation method as claimed in claim 1, it is characterised in that:The step (3) is:In step (2) resulting material 0.01~0.05 parts by weight SDD is added with terminating reaction, and it is dense to add 10~20 parts by weight quality Spend and neutralized for 30% sodium hydroxide solution, be cooled to 45 DEG C, discharging, obtain ethers polycarboxylic acid water reducing agent.
  5. 5. the preparation method as described in any claim in Claims 1-4, it is characterised in that:The unsaturated sulfonic acid salt For 2- hydroxyl -3- allyloxys propanesulfonate, 2- hydroxyl -3- allyloxy propane sulfonic acid potassium, 2- hydroxyl -4- alkene butoxy propane sulfonic acid Sodium or 2- hydroxyl -4- alkene butoxy propane sulfonic acid potassium.
  6. 6. the preparation method as described in any claim in Claims 1-4, it is characterised in that:The chain-transferring agent is mercapto Base ethanol, TGA or mercaptopropionic acid.
  7. 7. the preparation method as described in any claim in Claims 1-4, it is characterised in that:The reducing agent is 2- hydroxyls Base -2- sulfinatoacetic acids di-potassium or 2- hydroxyl -2- sulfonatoacetic acid di-potassiums.
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JPH09295846A (en) * 1996-05-07 1997-11-18 Nof Corp Resin composition for resin concrete
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