CN106380553A - Method for preparing maleic anhydride type superplasticizer by utilizing response surface method to optimize microwave radiation - Google Patents

Method for preparing maleic anhydride type superplasticizer by utilizing response surface method to optimize microwave radiation Download PDF

Info

Publication number
CN106380553A
CN106380553A CN201610869618.0A CN201610869618A CN106380553A CN 106380553 A CN106380553 A CN 106380553A CN 201610869618 A CN201610869618 A CN 201610869618A CN 106380553 A CN106380553 A CN 106380553A
Authority
CN
China
Prior art keywords
maleic anhydride
reaction
reducing agent
high efficiency
water reducing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201610869618.0A
Other languages
Chinese (zh)
Other versions
CN106380553B (en
Inventor
罗应
李彦青
程昊
李利军
孔红星
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangxi University of Science and Technology
Lushan College of Guangxi University of Science and Technology
Original Assignee
Guangxi University of Science and Technology
Lushan College of Guangxi University of Science and Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guangxi University of Science and Technology, Lushan College of Guangxi University of Science and Technology filed Critical Guangxi University of Science and Technology
Priority to CN201610869618.0A priority Critical patent/CN106380553B/en
Publication of CN106380553A publication Critical patent/CN106380553A/en
Application granted granted Critical
Publication of CN106380553B publication Critical patent/CN106380553B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F283/00Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C08F283/06Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
    • C08F283/065Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals on to unsaturated polyethers, polyoxymethylenes or polyacetals
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/16Sulfur-containing compounds
    • C04B24/161Macromolecular compounds comprising sulfonate or sulfate groups
    • C04B24/166Macromolecular compounds comprising sulfonate or sulfate groups obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2103/00Function or property of ingredients for mortars, concrete or artificial stone
    • C04B2103/30Water reducers, plasticisers, air-entrainers, flow improvers
    • C04B2103/302Water reducers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

The invention discloses a method for preparing a maleic anhydride type superplasticizer by utilizing a response surface method to optimize microwave radiation. According to the method, allyl polyoxyethylene ether and sodium methallyl sulfonate are used as raw materials and are added with water to be uniformly stirred and mixed; a mixture is heated to a reaction temperature under the microwave radiation condition; then maleic anhydride and ammonium persulfate are added at a constant temperature to perform a reaction for a period of time; variable parameters of the reaction are set by utilizing the response surface method; after the reaction is ended, cooling is carried out; and pH is regulated to obtain the maleic anhydride type superplasticizer. The invention researches a maleic anhydride type superplasticizer synthetic process which is optimized by utilizing the response surface method on the basis of single factor analysis, obtains process conditions relatively suitable for preparing the maleic anhydride type superplasticizer, and aims to provide the scientific test basis for development and popularization of the superplasticizer.

Description

Response phase method optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent
Technical field
The invention belongs to the preparation field of water reducer prepares maleic acid and in particular to a kind of response phase method optimizes microwave The method of anhydride high efficiency water reducing agent.
Background technology
Maleic anhydride contains anhydride group and carbon-carbon double bond, and this molecular configuration is conducive to producing conjugation, makes double bond (- C =C-) easily it is copolymerized with olefin monomer, such as methylpropene sodium sulfonate, acrylic acid, allyl polyethenoxy ether, styrene etc. Monomer, and the maleic anhydride as circulus, because of carbonyl electrophilic inductive effect and disubstituted group in its intramolecule Space steric effect is so as to be difficult to homopolymerization.So compared with the active olefin being susceptible to homopolymerization, the low work of maleic anhydride Property can effectively prevent reaction system cruelly poly-, and it is easily controllable to realize reaction condition, simple production process;In addition, maleic anhydride price Cheap, advantageously reduce product cost, be easy to the popularization and application of high efficiency water reducing agent.
Compared with traditional heating, microwave has fuel factor and the non-thermal effect of uniqueness, not only can achieve to reactant System is quick, uniformly heating, and can be different according to the dielectric constant of reaction system medium, realizes selectively heating, and by pole Change acts on, priming reaction group, improves polymerization rate.
Responds Surface Methodology is a kind of using functional relation between polynary quadratic regression equation data fitting and response A kind of statistical method, the method can solve Multivariable, and draws optimal processing parameter by regression equation analysis.Exist at present In the exploitation of high efficiency water reducing agent, such as CN201210274917.1, be using orthogonal experiment method filter out influence index notable because Element simultaneously provides optimal factor level combination, but exists and cannot find out lacking of the best of breed of factor and response in whole region More, there is deviation with actual conditions in point, and adopt linear model, the problems such as precision is high.
Content of the invention
Present invention aim to address above-mentioned technical problem, provide a kind of response phase method to optimize microwave and prepare maleic acid The method of anhydride high efficiency water reducing agent, research, on the basis of single factor analysis, optimizes maleic acid anhydride using response phase method and efficiently subtracts Aqua synthesis technique, draws relatively to be applied to and prepares maleic anhydride analog high efficiency water reducing agent process conditions it is intended to be high efficiency water reducing agent Exploitation, popularization provide scientific experimentation foundation.
For realizing above-mentioned purpose, the technical scheme is that:
A kind of response phase method optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, and it is to be gathered with pi-allyl Oxygen vinethene and methylpropene sodium sulfonate add water for raw material and are uniformly mixed, and are heated to reaction temperature under the conditions of microwave Degree, then constant temperature addition maleic anhydride and ammonium persulfate reaction a period of time, sets the variable parameter of reaction using response phase method, Reaction cools down after terminating, and adjusts pH, obtains final product maleic anhydride analog high efficiency water reducing agent.
As further technical scheme, the above response phase method sets the variable parameter of reaction, by following secondary Multinomial regression equation:
Y=320.00+0.83A+2.33B+4.92C-0.42D-1.50AB-3.25AC-4.75AD-4. 50CD 10.93A2–5.93B2-8.31C2+1.44D2
In formula:Response Y is flowing degree of net paste of cement, unit mm;A is methylpropene sodium sulfonate and allyl polyethenoxy The mol ratio of ether;B is the mol ratio of maleic anhydride and allyl polyethenoxy ether;C is the reaction time, unit min;D is reaction Temperature, unit DEG C.
As further technical scheme, the mol ratio of the above methylpropene sodium sulfonate and allyl polyethenoxy ether For 0.4-0.6, described maleic anhydride is 2.5-3.5 with the mol ratio of allyl polyethenoxy ether, and the described reaction time is 25- 35min, described reaction temperature is 80-90 DEG C.
As further technical scheme, the mol ratio of the above methylpropene sodium sulfonate and allyl polyethenoxy ether For 0.52, described maleic anhydride is 3.10 with the mol ratio of allyl polyethenoxy ether, and the described reaction time is 33min, described Reaction temperature is 80 DEG C.
As further technical scheme, the volume of the above ammonium persulfate is allyl polyethenoxy ether and methyl-prop The 1.5%-2.5% of alkene sodium sulfonate gross mass.
As further technical scheme, the power of the above microwave is 250W-350W.
As further technical scheme, the above adjusts pH, is to be adjusted to the reaction solution pH after cooling down with aqueous slkali 7-8.
As further technical scheme, the above aqueous slkali is NaOH, potassium hydroxide, sodium carbonate, potassium carbonate.
As further technical scheme, the mass fraction of the above NaOH is 20%-40%.
Compared with prior art, beneficial effects of the present invention are:
(1) response phase method of the present invention be suitable for solve nonlinear transportation relevant issues, it enumerate experimental design, Modeling, the well-formedness of testing model, seek optimum combination condition etc.;By to the regression fit of process and response surface, contour Draw it is convenient to obtain the response corresponding to each factor level;And find out the response optimal value of prediction based on this And the experiment condition of response.Compared with orthogonal test, its advantage is:In experimental condition searching process, can be continuously right Each level of test is analyzed, and the forecast model of gained is continuously, and orthogonal test can only be to the examination isolated one by one Test and be a little analyzed;Response phase method considers test random error, simultaneously response phase method complicated unknown function is closed tie up to little In region with simple once or quadratic polynomial model is come matching, calculate easier, be effective hand of solving practical problems Section.
(2) present invention establishes the secondary multinomial regression equation model of flowing degree of net paste of cement and dependent variable, employing Design-Expert 8.0 software, with five changed factors, only with four levels, compared with Orthogonal Method, with a small amount of test group Just can obtain a result, and obtained optimum condition is not the value setting but within the scope of imposing a condition.Pass through Using response phase method to the mol ratio of methylpropene sodium sulfonate and allyl polyethenoxy ether, maleic anhydride and pi-allyl polyoxy second The mol ratio of alkene ether, reaction time and reaction temperature are optimized, and the condition obtaining optimizing is:Methylpropene sodium sulfonate and allyl The mol ratio of base APEO is 0.52, and maleic anhydride is 3.10 with the mol ratio of allyl polyethenoxy ether, the reaction time For 33min, reaction temperature is 80 DEG C, and the product flowing degree of net paste of cement obtaining is 325.24mm, is that maleic acid anhydride efficiently subtracts Aqua industrialized production provides a scientific basis.
(3) the inventive method is accurately and reliably.For verifying the validity of model, efficient diminishing is prepared using the inventive method Agent, and carry out properties of product test.By actual 3 parallel testings, with the ratio of mud for 0.29, it is water in water reducer solid volume Under the conditions of the 0.5% of shale amount, flowing degree of net paste of cement mean value is 326mm, substantially identical with theoretical expectation values, shows to be based on Response phase method optimum synthesis technique is accurately and reliably.
(4) product of the present invention has good dispersion retentivity.In the present invention, when product volume is 0.15%, just Beginning flowing degree of net paste of cement is 287mm, and is gradually increased and tends towards stability with the volume initial flowing degree of net paste of cement of increase, its The corresponding initial flowing degree of net paste of cement of middle volume 0.5% reaches 328mm;In addition, extending with the testing time, four kinds of different diminishings Flowing degree of net paste of cement under agent volume is declined slightly, and wherein volume is corresponding to 0.15%, 0.30%, 0.50%, 0.70% 60min flowing degree of net paste of cement gradual loss rate be respectively 5.9%, 4.5%, 5.2% and 4.9%, this efficient diminishing is described Agent has good dispersion retentivity, is suitable for concrete long-distance transportation, construction.
(5) product of the present invention has preferable actual application value.The present invention is probing into maleic anhydride analog high efficiency water reducing agent On the basis of dispersive property, experiment investigation water reducer application performance.When water reducer solid volume is for the 0.3% of cement quality, Its corresponding water reducing ratio of cement mortar reaches 35.4%, shows that the high efficiency water reducing agent of preparation under this process conditions can meet high property well Energy concrete application requirement, has preferable actual application value.
(6) microwave of the present invention effectively increases process efficiency, and energy-conserving and environment-protective, easy to operate, easy to control.
Brief description
Fig. 1 is methylpropene sodium sulfonate of the present invention and the impact to flowing degree of net paste of cement for the allyl polyethenoxy ether mole Figure;
Fig. 2 is maleic anhydride of the present invention and the impact figure to flowing degree of net paste of cement for the allyl polyethenoxy ether mol ratio;
Fig. 3 is the impact figure to flowing degree of net paste of cement for the ammonium persulfate consumption of the present invention;
Fig. 4 is the impact figure to flowing degree of net paste of cement for the reaction temperature of the present invention;
Fig. 5 is the impact figure to flowing degree of net paste of cement for the present invention reaction time;
Fig. 6 is mol ratio and maleic anhydride and the pi-allyl of methylpropene sodium sulfonate of the present invention and allyl polyethenoxy ether The response surface figure to flowing degree of net paste of cement for the reciprocation of the mol ratio of APEO;
Fig. 7 be the mol ratio of methylpropene sodium sulfonate of the present invention and allyl polyethenoxy ether and reaction time interact work With the response surface figure to flowing degree of net paste of cement;
Fig. 8 be the mol ratio of methylpropene sodium sulfonate of the present invention and allyl polyethenoxy ether and reaction temperature interact work With the response surface figure to flowing degree of net paste of cement;
Fig. 9 is the mol ratio of maleic anhydride of the present invention and allyl polyethenoxy ether and the reciprocation in reaction time to water The response surface figure of cement paste fluidity;
Figure 10 is maleic anhydride of the present invention and the mol ratio of allyl polyethenoxy ether and the reciprocation pair of reaction temperature The response surface figure of flowing degree of net paste of cement;
Figure 11 is reaction temperature of the present invention and the reciprocation in the reaction time response surface figure to flowing degree of net paste of cement;
Figure 12 is flowing degree of net paste of cement gradual loss figure under maleic anhydride analog high efficiency water reducing agent different addition quantity of the present invention.
Specific embodiment
With reference to embodiment, the present invention is described in further detail, but embodiments of the present invention are not limited to The scope that embodiment represents.
Embodiment 1:
A kind of response phase method optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, and it is to be gathered with pi-allyl Oxygen vinethene and methylpropene sodium sulfonate add water for raw material and are uniformly mixed, and are heated to reaction temperature under the conditions of microwave Degree, then constant temperature addition maleic anhydride and ammonium persulfate reaction a period of time, sets the variable parameter of reaction using response phase method, Reaction cools down after terminating, and adjusts pH, obtains final product maleic anhydride analog high efficiency water reducing agent.Specifically include following steps:
1st, the preparation of sample
Accurately weigh a certain amount of allyl polyethenoxy ether and methylpropene sodium sulfonate, put into tetra- mouthfuls of the 500mL of cleaning In reaction flask, put into microwave reactor, and install reflux condensing tube, thermometer, agitator, add water after sealing 50mL, and Mixture solution is stirred.Start microwave reactor, using microwave power 300W, solution is heated, treat that temperature reaches instead After answering temperature, under constant temperature, it is simultaneously added dropwise maleic anhydride and initiator ammonium persulfate solution respectively, drips and finish, isothermal reaction is extremely required Time.Close microwave emitter, after question response solution is cooled to room temperature, the sodium hydroxide solution of dropping mass fraction 30%, adjust Section mixed solution pH value is 7~8, obtains glassy yellow transparent maleic anhydride analog high efficiency water reducing agent.
2nd, performance test and sign
(1) mensure of solid content:By GB/T 8077-2012《Methods for testing uniformity of concrete admixture》Tested.
(2) mensure of flowing degree of net paste of cement:By GB/T 8077-2012《Methods for testing uniformity of concrete admixture》 Tested, wherein the ratio of mud adopts 0.29, in process optimization, water reducer solid volume is the 0.5% of cement weight.
(3) mensure of water reducing ratio of cement mortar:By GB/T 8077-2012《Methods for testing uniformity of concrete admixture》Carry out Test.
(4) flowing degree of net paste of cement gradual loss:The ratio of mud is 0.29, after testing initial paste flowing degree, rapidly will be net Slurry leaves (20 ± 2) DEG C in, relative humidity is in 60%~80% curing box, measures a cement paste stream every 30min Dynamic degree.
3rd, experiment of single factor
(1) SMAS (i.e. methylpropene sodium sulfonate) and APEG (i.e. allyl polyethenoxy ether) mol ratio are disperseed to water reducer The impact of performance
In high efficiency water reducing agent molecular structure, methylpropene sodium sulfonate and allyl polyethenoxy ether are respectively configured to provide the moon Ionic group-SO3 -And long side base-(CH2CH2O)-, wherein-SO3 -Can effectively adsorb in cement particle surface, be conducive in cement Particle surface forms electric double layer;And polyethoxy-(CH2CH2O)-effective space steric effect can be provided, so electrostatic repulsion and The cooperative effect of sterically hindered, directly affects Cement Hydration Process.In nMAH:nAPEG=3, initiator ammonium persulfate consumption Under the conditions of the 2% of total addition level, microwave power 300W, reaction time 30min, 85 DEG C of reaction temperature, methylpropene sodium sulfonate As shown in Figure 1 with the impact to water reducer dispersive property for the allyl polyethenoxy ether mol ratio.
Fig. 1 shows, flowing degree of net paste of cement is with the increase of methylpropene sodium sulfonate and allyl polyethenoxy ether mol ratio First increases and then decreases, works as nSMAS:nAPEGWhen=0.5, paste flowing degree reaches maximum 328mm.This is because with SMAS volume Increase ,-SO in polymer molecule3 -Increase, anionic charge density increases and is conducive to water reducer in the absorption of cement particle surface; But when SMAS addition is excessive, because SMAS has chain-transferring agent effect, so that polymer molecular weight is reduced, product dispersive property Decline.
(2) MAH (i.e. maleic anhydride) and APEG (i.e. allyl polyethenoxy ether) mol ratio are to water reducer dispersive property Impact
According to maleic anhydride molecule configuration, after its hydrolysis, a molecule maleic anhydride will produce two-COO-Functional group, with- SO3 -Efficiency is the same, the Ca of this group and cement particle surface2+And the Ca in solution2+There is complex reaction, suppress hydrated cementitious, Improve water reducer dispersive property.In nSMAS:nAPEG=0.5, initiator ammonium persulfate consumption be total addition level 2%, microwave power Under the conditions of 300W, reaction time 30min, 85 DEG C of reaction temperature, maleic anhydride and allyl polyethenoxy ether mol ratio are to diminishing The impact of agent dispersive property is as shown in Figure 2.
As shown in Figure 2, work as nMAH:nAPEGWhen 2~3, flowing degree of net paste of cement gradually increases with maleic anhydride volume increase Greatly, show-COO-The increase of group is conducive to enhancing product performance;And work as nMAH:nAPEGDuring more than 3, due to maleic anhydride volume Excessive, on main chain, long side chain density reduces, and space steric effect reduces, and electrostatic repulsion is declined with sterically hindered synergy, Properties of product weaken.
(3) APS (i.e. ammonium persulfate) impact to water reducer dispersive property for the consumption
In nSMAS:nMAH:nAPEG=0.5:3:1st, microwave power 300W, reaction time 30min, 85 DEG C of conditions of reaction temperature Under, investigate the impact to water reducer dispersive property for the initiator ammonium persulfate consumption, as shown in Figure 3.Fig. 3 shows, works as persulfuric acid When ammonium volume is always add quality 2%, water reducer dispersive property is optimal.This is because when initiator amount is less, freely Base polymerization activity center is less, and reaction rate is slower, and within the short time in reaction time 30min, polymerisation is insufficient, water Cement paste fluidity is relatively low;When ammonium persulfate volume is larger, the degree of polymerization is not high, and polymer molecular weight is low, leads to water reducer Can reduce.
(4) impact to water reducer dispersive property for the reaction temperature
In nSMAS:nMAH:nAPEG=0.5:3:1st, ammonium persulfate consumption be total addition level 2%, microwave power 300W, reaction Under the conditions of time 30min, reaction temperature is obvious on pulp flowage impact, as shown in Figure 4.Fig. 4 shows when temperature is by 65 DEG C When increasing to 85 DEG C, flowing degree of net paste of cement increases to 328mm from 183mm, and water reducer performance temperature influence is larger;Followed by of continuing rising When high polymerization temperature is to 90 DEG C, flowing degree of net paste of cement is declined slightly, therefore optimal reaction temperature is 85 DEG C.
(5) impact to water reducer dispersive property for the reaction time
In nSMAS:nMAH:nAPEG=0.5:3:1st, ammonium persulfate consumption be total addition level 2%, microwave power 300W, reaction Under the conditions of 85 DEG C of temperature, as shown in Figure 5, in the range of polymerization time 20min~50min, flowing degree of net paste of cement is with during reaction Between change less, so under the premise of guaranteeing that starting monomer fully reacts and avoids gelatin phenomenon, being optimal polymerization using 30min Reaction time.
4th, maleic anhydride analog high efficiency water reducing agent prepares response surface optimization analysis
(1) model is set up and significance test
Each factor due to affecting water reducer dispersive property does not isolate, and tests on the basis of single factor test optimizes, using sound Surface analysis technology is answered to determine the reciprocation between each factor to water reducer performance impact rule, according to test data analyzer result, Carry out multiple regression matching, draw quadratic regression equation model, determine optimum process condition.Research and utilization Design-Expert 8.0.6 software, with nSMAS:nAPEG(A)、nMAH:nAPEG(B), reaction time (C), reaction temperature (D) are independent variable, take cement net Slurry fluidity is response, and each factor level and result of the test are shown in Table 1, table 2 respectively.
Table 1 factor level table
Table 2 response surface experiments result
Using Design-Expert 8.0 software, it is carried out with multiple matching, obtain response flowing degree of net paste of cement Encoding equtions is as follows:Flowing degree of net paste of cement (mm)=320.00+0.83A+2.33B+4.92C-0.42D-1.50AB- 3.25AC-4.75AD-4.50CD–10.93A2–5.93B2-8.31C2+1.44D2, in formula:A—nSMAS:nAPEG;B—nMAH: nAPEG;The C reaction time;D reaction temperature, variance analysis is shown in Table 3.
Table 3 analysis of variance table
Note:Prob<0.001 is that difference is extremely notable;Prob<0.01 is difference highly significant;Prob<0.05 shows for difference Write.
From table 3 it can be seen that C (reaction time), AD (nMAH:nAPEGReciprocation with reaction temperature), A2、B2、C2Right The impact of flowing degree of net paste of cement is significant.Meanwhile, model P=0.0005 (notable), shows that quadratic equation model is notable 's;Lose and intend item P=0.9538 (not notable), illustrate that this regression equation is meaningful, can be used for speculating result of the test.
(2) response surface interactive analysis and optimization
Carry out response phase method analysis using reciprocation between each factor for the Design-Expert 8.0, draw out with water Cement paste fluidity is the response surface 3D curve map of response, such as Fig. 6-11.Each factor interaction can intuitively be reflected by Fig. 6-11 The impact to flowing degree of net paste of cement for the effect, wherein curve is more precipitous, illustrates that this factor affects on flowing degree of net paste of cement bigger. From Fig. 6-11 it can be seen that the reaction time affects maximum to water reducer dispersive property, according to its corresponding P=0.0017<0.05, The impact to flowing degree of net paste of cement for the reaction time reaches the level of signifiance;Meanwhile, within the specific limits flowing degree of net paste of cement with Reaction temperature and nSMAS:nAPEGIncrease in rising trend, two factor significant interaction.
From Fig. 6-11, there is maximum in response.Obtain microwave by Design-Expert 8.0 software optimization to make With the lower most preferably theoretical technique preparing high efficiency water reducing agent it is:nSMAS:nAPEG=0.52;nMAH:nAPEG=3.09;Reaction time is 32.67min;Reaction temperature is 80.00 DEG C, and under the conditions of being somebody's turn to do, flowing degree of net paste of cement is 325.24mm.
(3) reliability of response phase method
For verifying the validity of model, high efficiency water reducing agent is prepared using above-mentioned optimize technique, and carries out properties of product test. In view of the operability of technological parameter, each technological parameter is modified to n respectivelySMAS:nAPEG=0.52, nMAH:nAPEG=3.10, react Time be 33min, reaction temperature be 80 DEG C.By actual 3 parallel testings, with the ratio of mud for 0.29, mix in water reducer solid Measure as under the conditions of the 0.5% of cement quality, flowing degree of net paste of cement mean value is 326mm, table substantially identical with theoretical expectation values Bright based on response phase method optimum synthesis technique accurately and reliably.
5th, maleic anhydride analog high efficiency water reducing agent performance test
For probing into the maleic anhydride analog high efficiency water reducing agent application performance of preparation under this process conditions, check molecular structure function Change design rationality, test further study the impact (Figure 12) to cement dispersive property for this high efficiency water reducing agent and diminishing effect Really.
Figure 12 shows, when water reducer volume is 0.15%, initial flowing degree of net paste of cement is 287mm, and with volume Increase initial flowing degree of net paste of cement to be gradually increased and tend towards stability, wherein the corresponding initial pulp flowage of volume 0.5% Degree reaches 328mm;In addition, extending with the testing time, the flowing degree of net paste of cement under four kinds of different water reducer volumes is declined slightly, Wherein volume is 0.15%, the 60min flowing degree of net paste of cement gradual loss rate corresponding to 0.30%, 0.50%, 0.70% divides Not Wei 5.9%, 4.5%, 5.2% and 4.9%, illustrate that this high efficiency water reducing agent has good dispersion retentivity, be suitable for coagulation Native long-distance transportation, construction.
On the basis of probe into maleic anhydride analog high efficiency water reducing agent dispersive property, experiment investigation water reducer application performance.When When water reducer solid volume is the 0.3% of cement quality, its corresponding water reducing ratio of cement mortar reaches 35.4%, shows under this process conditions The high efficiency water reducing agent of preparation can meet high performance concrete application requirement well, has preferable actual application value.
After obtaining optimum process condition, in the present embodiment, the volume of ammonium persulfate can be replaced allyl polyethenoxy Ether and the 1.8% or 3.0% of methylpropene sodium sulfonate gross mass, the power of microwave can be replaced 250W or 350W, alkali soluble Liquid can be replaced potassium hydroxide, sodium carbonate or potassium carbonate, and the mass fraction of aqueous slkali can be replaced 20% or 40%.
Above-described embodiment, only the purpose of the present invention, technical scheme and beneficial effect are further described is concrete Individual example, the present invention is not limited to this.All any modification, equivalent substitution and improvement done within the scope of disclosed by the invention Deng being all contained within protection scope of the present invention.

Claims (9)

1. a kind of response phase method optimize microwave prepare maleic anhydride analog high efficiency water reducing agent method it is characterised in that:It is Added water for raw material with allyl polyethenoxy ether and methylpropene sodium sulfonate and be uniformly mixed, heat under the conditions of microwave To reaction temperature, then constant temperature addition maleic anhydride and ammonium persulfate reaction a period of time, set reaction using response phase method Variable parameter, reaction cools down after terminating, and adjusts pH, obtains final product maleic anhydride analog high efficiency water reducing agent.
2. response phase method according to claim 1 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:Described response phase method sets the variable parameter of reaction, by following secondary multinomial regression equation:
Y=320.00 + 0.83A+ 2.33B+ 4.92C- 0.42D- 1.50AB- 3.25AC- 4.75AD - 4.50CD– 10.93A 2– 5.93B 2- 8.31C 2+ 1.44D 2
In formula:ResponseYFor flowing degree of net paste of cement, unit mm;AFor methylpropene sodium sulfonate and allyl polyethenoxy ether Mol ratio;BMol ratio for maleic anhydride and allyl polyethenoxy ether;CFor reaction time, unit min;DFor reaction Temperature, unit DEG C.
3. response phase method according to claim 2 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:Described methylpropene sodium sulfonate is 0.4-0.6 with the mol ratio of allyl polyethenoxy ether, described maleic anhydride Mol ratio with allyl polyethenoxy ether is 2.5-3.5, and the described reaction time is 25-35 min, and described reaction temperature is 80- 90 ℃.
4. response phase method according to claim 3 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:The mol ratio of described methylpropene sodium sulfonate and allyl polyethenoxy ether is 0.52, described maleic anhydride with The mol ratio of allyl polyethenoxy ether is 3.10, and the described reaction time is 33 min, and described reaction temperature is 80 DEG C.
5. response phase method according to claim 1 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:The volume of described ammonium persulfate is the 1.5%- of allyl polyethenoxy ether and methylpropene sodium sulfonate gross mass 2.5%.
6. response phase method according to claim 1 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:The power of described microwave is 250 W-350 W.
7. response phase method according to claim 1 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:Described tune pH, is, with aqueous slkali, the reaction solution pH after cooling down is adjusted to 7-8.
8. response phase method according to claim 7 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:Described aqueous slkali is NaOH, potassium hydroxide, sodium carbonate, potassium carbonate.
9. response phase method according to claim 8 optimizes the method that microwave prepares maleic anhydride analog high efficiency water reducing agent, It is characterized in that:The mass fraction of described NaOH is 20%-40%.
CN201610869618.0A 2016-09-30 2016-09-30 The method that response phase method optimization microwave radiation prepares maleic anhydride analog high efficiency water reducing agent Active CN106380553B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610869618.0A CN106380553B (en) 2016-09-30 2016-09-30 The method that response phase method optimization microwave radiation prepares maleic anhydride analog high efficiency water reducing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610869618.0A CN106380553B (en) 2016-09-30 2016-09-30 The method that response phase method optimization microwave radiation prepares maleic anhydride analog high efficiency water reducing agent

Publications (2)

Publication Number Publication Date
CN106380553A true CN106380553A (en) 2017-02-08
CN106380553B CN106380553B (en) 2018-12-18

Family

ID=57937054

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610869618.0A Active CN106380553B (en) 2016-09-30 2016-09-30 The method that response phase method optimization microwave radiation prepares maleic anhydride analog high efficiency water reducing agent

Country Status (1)

Country Link
CN (1) CN106380553B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112908430A (en) * 2019-12-03 2021-06-04 中国科学院大连化学物理研究所 Experimental method for optimizing normal olefin prepared by high-carbon alcohol dehydration by using response surface method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101538134A (en) * 2009-04-14 2009-09-23 大连市建筑科学研究设计院股份有限公司 Polyether class polycarboxylic acid high-efficiency water reducing agent and preparation method thereof
CN105061691A (en) * 2015-07-31 2015-11-18 广西科技大学 Method for efficiently preparing amide type polycarboxylate water reducer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101538134A (en) * 2009-04-14 2009-09-23 大连市建筑科学研究设计院股份有限公司 Polyether class polycarboxylic acid high-efficiency water reducing agent and preparation method thereof
CN105061691A (en) * 2015-07-31 2015-11-18 广西科技大学 Method for efficiently preparing amide type polycarboxylate water reducer

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
葛宜元 等: "《试验设计方法与Design-Expert软件应用》", 31 January 2015, 哈尔滨工业大学出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112908430A (en) * 2019-12-03 2021-06-04 中国科学院大连化学物理研究所 Experimental method for optimizing normal olefin prepared by high-carbon alcohol dehydration by using response surface method

Also Published As

Publication number Publication date
CN106380553B (en) 2018-12-18

Similar Documents

Publication Publication Date Title
CN100591704C (en) Method for synthesizing allyl polyether-type high-performance water reducing agent
CN102504238B (en) Unsaturated polyether monomer, comb-like branched copolymer cement dispersant prepared by the same, and preparation method thereof
CN107129177B (en) A kind of anti-chamotte mould polycarboxylate water-reducer and preparation method and the application in concrete
CN101805146A (en) Polycarboxylic acid water reducer and preparation method thereof
CN104788629A (en) Polycarboxylate water-reducing agent and normal-temperature preparation method thereof
CN104649608A (en) Additive for improving early strength of cement based material as well as preparation method and application of additive
CN103641361A (en) Polycarboxylic slump retaining agent and its preparation method
CN106046276A (en) Preparation method and product of polycarboxylate superplasticizer comprising amido groups
CN103497285B (en) A kind of method adopting microwave assisting method to prepare the efficient superplasticizer of poly carboxylic acid graft copolymer class
CN103664040B (en) A kind of multiple copolymer cement grinding aid and preparation method
CN112851889A (en) Preparation method of graphene oxide modified TPEG type polycarboxylate superplasticizer
CN104628959A (en) Method for synthesizing cement dispersing agent by using terminated functional polyethylene fatty acid ester macromonomer
CN105693946A (en) Anti-crack high slump loss resistance concrete polycarboxylate superplasticizer
CN106380553A (en) Method for preparing maleic anhydride type superplasticizer by utilizing response surface method to optimize microwave radiation
CN102250296B (en) Water reducing agent as well as preparation method and application thereof
CN106317343A (en) Water-reducing agent for polycarboxylate concrete and preparation and application thereof
CN102786613B (en) Emulsion polymerized syndiotactic polystyrene and its preparation method
CN103804611B (en) The preparation method of polycarboxylate high-efficiency water reducing agent
CN102319585B (en) High-temperature-resistant maleic anhydride (MAH) resin catalyst and preparation method thereof
CN109096449A (en) Concrete slump retaining agent and preparation method thereof with high-adaptability
CN103923258A (en) IAEO-AA-SMAS terpolymer surfactant as well as preparation method and application thereof
CN107793538A (en) A kind of preparation method and application of polycarboxylate water-reducer
CN105293976B (en) A kind of pile tube and preparation method thereof
CN105622864A (en) Method for rapidly preparing high-water reduction polycarboxylate water reducing agent at low temperature
CN104892856B (en) A kind of preparation method of polycarboxylate water-reducer

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant