CN104609759B - Additive capable of improving bending strength and tensile strength of cement base material and its preparation method - Google Patents
Additive capable of improving bending strength and tensile strength of cement base material and its preparation method Download PDFInfo
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- CN104609759B CN104609759B CN201410690674.9A CN201410690674A CN104609759B CN 104609759 B CN104609759 B CN 104609759B CN 201410690674 A CN201410690674 A CN 201410690674A CN 104609759 B CN104609759 B CN 104609759B
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Abstract
The invention discloses an additive capable of improving bending strength and tensile strength of a cement base material. The additive is an aqueous dispersion of organic-inorganic hybrid particles with core-shell structures. Each organic-inorganic hybrid particle is composed of inner and outer layers, wherein the inner layer is an organic polymer core; the outer layer is an inorganic composite oxide or an inorganic composite oxide covalently connected with an organic functional group; the inorganic composite oxide is a silicon-calcium composite oxide or a silicon-magnesium composite oxide or a silicon-calcium-magnesium composite oxide; and the outer layer is in covalent connection with an electronegative organic polyelectrolyte internally. Compared to the mixing amount of a polymer or polymer fiber in a pure polymer-modified cement base material or a polymer fiber-modified cement base material, the mixing amount of the additive in the cement base material can be greatly reduced; and the additive can more obviously improve the splitting tensile and bending resistant performances of the cement base material in comparison with a traditional polymer emulsion in the same mixing amount. Therefore, the additive overcomes the disadvantage that the high polymer mixing amount of the traditional polymer modified cement base material affects the compressive strength of the cement base material, and can effectively improve the bending strength and tensile strength (or splitting tensile strength) of the cement base material.
Description
Technical field
The present invention relates to be used for the modified additive field of cement-based material, and in particular to one kind can improve cement-based material
The additive of anti-folding and tensile strength.
Background technology
The cement matrixs such as concrete, mortar or slip casting are represented used in term " concrete " herein is generally indiscriminate
Material, this is also suitable in elsewhere herein.
Portland cement concrete is a kind of typical fragile material, and its comprcssive strength is high, and bend resistance, tensile strength are substantially not
Foot, in actual use, easily because stress concentration or unbalance stress produce various crackles or damage so that durability declines,
So as to limit its application, for example, it is applied to cement pavement surface layer and easily occurs the disease such as disconnected plate and surface texture destruction too early, because
And limit its application in high-grade highway.
People have carried out substantial amounts of research in terms of Brittleness of Concrete is improved, especially by addition modified component so as to carrying
The method of high concrete bend resistance, tensile strength, existing main modified component includes fiber (organic polymer, steel fibre and glass
Glass fiber) and polymer particle (emulsion or dry powder) etc..
Fiber reinforced principle is:(1) microcrack development is limited.When fiber is evenly distributed among concrete substrate,
It is assumed that there are the tendency that microcrack occurs inside concrete substrate, when any microcrack occurs and may be to any
When direction is developed, it is farthest less than fiber in concrete substrate fiber mean center away from distance within, the crack will meet
To the fiber lain across in front of it.After crack produces, due to the high-moduluss and single high-tensile of fiber, can hinder
Crack arrest seam further development, can only be formed in concrete substrate similar to harmless hole closed cavity or internal diameter very
Tiny hole.(2) high strength fibre toughness itself is far above concrete, the intensity of fibre modification concrete be concrete phase and
The superposition of fiber phase performance, thus its toughness is higher than normal concrete.
Polymer particle can improve the combination between concrete component as additive.The dispersion of polymer particle and
Film forming is their ability to modified main cause.Due to the presence of polymeric film, make the mechanical property of concrete material (especially tough
Property) more excellent.Physical action or the effect of part chemical bonding are generated between polymer and inorganic material, i.e., polymer is with grain
The form of son or film is modified to cement mortar, it is also possible to formed with the more fine and close chelating of the structure of coordination combination
Body, so as to improve the performance of polymer cement concrete.Active group such as-OH ,-COOH ,-COOR are introduced in polymer
Coordination can be produced with hydrolysis product of cement, change of bonding of the cement material based on siliconoxygen bond, add organic C-H bond
Of bonding, be remarkably reinforced structure, form folded double set network structures repeatedly staggeredly, improve the combination between interface, raising
Interphase fracture energy and toughness (Bulletin of the Chinese Ceramic Society, 2014,33,365).
But all there is obvious deficiency in above technology:
(1) fiber easy conglomeration in concrete-agitating, it is difficult to disperse, it is impossible in being uniformly distributed in concrete.Fiber changes
Property the performance of concrete and the dispersion of fiber and orientation have substantial connection, thus concrete preparation technology affects on concrete performance
Larger, its preparation is more increasingly difficult than conventional concrete.Conglomeration makes concrete workability poor, pumping difficulties, is difficult to construct.Steel fibre
In use damage -form is mainly pulled out, without being pulled off, the adhesiveness with concrete of this explanation steel fibre
Deficiency, this can affect the effect for improving concrete tensile strength.Synthetic fibers density is little, and filament diameter is less, there is thickening effect
Should, it is unfavorable for that the vibrations of concrete are closely knit.Glass fibre is poor due to alkali resistance, and the application of glass concrete is limited
System.
The toughening cement-based materials method that patent CN101891417B is disclosed needs (to wrap its formula each component by stirring
Include fiber) it is uniformly dispersed, mixing time longer (25-35min).Patent CN101913188B adds magnetic field to make the single-phase distribution of steel fibre
Flexural Strength of Steel Fibers Concrete is improved, this undoubtedly causes the preparation of concrete to complicate.Patent US7192643 passes through special side
Method prepares easily scattered organic fiber film is used for toughening cement-based materials.Patent EP0488577, US5993537, US4524101
It is both needed to add the limited means such as so-called wetting agent or inorganic coupling reagent (binding agent) and fiber is disperseed.These
Patent generally needs to prepare required fibrous material or corresponding modified concrete by specific means or equipment.
(2) polymer volume is too high in polymer modification concrete.Because polymer modification concrete is more formed
Polymer network, equivalent to the form being blended by material concrete performance, polymer network itself and cement-based material are improved
Cohesive force is limited, thus the performance that is modified in low-dosage is not obvious, it is necessary to which compared with high additive, this causes its relatively costly for addition.
Polymer emulsion is also possible to coagulation in the environment of concrete highly basic high salt, affects its effect to play (anionic emulsifying
The easy coagulation of emulsion of agent synthesis, Journal of Materials in Civil Engineering 2011,23,1412).Specially
Sharp CN102276764B provides the chemical modification method that a kind of polymer powder is modified, on polymer powder surface by being coupled
Agent carries out chemical graft, and to improve the interaction of powder and matrix, so as to improve the shock resistance of modified mortar, but it is originally
Body does not solve the scattering problem of polymer powder.
Although polymer increased rupture strength and toughness, the comprcssive strength of high additive polymer modification concrete is obvious
Reduce.Even if (with ratio of mud condition, or even in view of polymer breast under conditions of polymer volume relatively low (5wt%)
The water-reduction of liquid, also has slight intensity and declines using the lower ratio of mud), concrete crushing strength also has in various degree
Decline, its amplitude even up to~15-50% (Journal of Jilin Institute of Architecture&
Civil Engineering2012,29,7;Cement and Concrete Research 2005,35,900 etc.).
Polymer emulsion (Handbook of polymer-modified concrete and mortars, 1995,55)
The setting time of cement-based material is affected, the polymer emulsion species by using is relevant with consumption, typically can postpone
Setting time (several tens minutes-a few hours).
In addition, patent CN103130436A and CN101239800B report respectively using Graphene (graphene oxide) and
Carbon nano-tube modification cement-based material, is lifted to resistance to compression tension rupture strength, but its high cost.EP2695850A1 is disclosed
A kind of method in cement-based material situ nucleating growth calcium silicates (wollastonite) nanocrystal is used for toughness reinforcing, needs
The conditions such as specific temperature, pressure, to preparation difficulty is brought.
The content of the invention
Goal of the invention:The invention aims to solve the above problems, there is provided one kind can improve the anti-folding of cement-based material
With the additive of tensile strength.
Technical scheme:The additive for improving the anti-folding of cement-based material and tensile strength of the present invention, the additive
It is a kind of aqueous dispersions of the hybrid inorganic-organic particle with nucleocapsid structure, the hybrid inorganic-organic particle is by inside and outside
Two-layer is constituted, and internal layer is the inorganic compounding of organic polymer core, outer layer inorganic composite oxide or organo-functional group covalent attachment
Oxide, affiliated inorganic composite oxide is silicon-calcium composite oxides or silicon-Magnesium coumpoud oxide or silicon-calcium-magnesium combined oxidation
Thing, being covalently attached in the layer of the outer layer has elecrtonegativity organic polyelectrolyte.
The effect of the inside and outside materials at two layers of the hybrid inorganic-organic particle is respectively:
When hybrid inorganic-organic particle incorporation cement-based material is modified, internal layer plays a part of to be crosslinked node, due to
Organic substance has excellent tensile property, can undertake part external force, to lift the rupture strength of cement-based material and split drawing by force
Degree;
It is connected with each other with covalent bond between outer layer and internal layer Organic substance core, outer layer has triple role, strong in cement-based material
In the environment of alkalescence, the mineral shell can induce the main bonding component hydrated calcium silicate gel (CSH) of cement-based material
In particle surface crystallization, on the one hand, greatly accelerate heat evolution velocity, the development of cement-based material early strength is promoted (but not affect material
The final mechanical property of material), on the other hand (it is covalent that-OH alkaline reactions generate silica with CSH gels generation ionic bond and covalent bond
Key) connection, whole organic polymers are coupled together with CSH granules so as to pass through chemical bond, because monodispersed particle is in water
It is significantly increased compared to polymeric film with the bond area of Binder Materials in mud system, thus internal layer Organic substance can be given full play to
Improve the effect of Mechanical Properties of Cement-based Materials, such that it is able to lift the rupture strength and tension of cement-based material in low-dosage
(or splitting drawing) intensity.
The present invention also provides the preparation method of the additive, and step is as follows:
(1) polymerisable monomer A, polymerisable monomer B, Part I cross-linking agent C and water are added in reactor, is sufficiently stirred for
Mixing;Lead to N in mixed liquor2Except O2, reactor is risen to into reaction temperature, add initiator to draw in reactor under stirring condition
Polymerization is sent out, starting simultaneously at the mixed liquor of Deca Part II cross-linking agent C and polymerisable monomer D in reactor carries out copolymerization, institute
It is arbitrary proportion to state Part I cross-linking agent C and Part II cross-linking agent C, and reaction end obtains the dispersion of organic polymer nuclear particle
Liquid;
(2) organic polymer nuclear particle dispersion liquid prepared by step (1) is adjusted to temperature required, to having under stirring condition
Organic substance E, organic polymer G and inorganic component F are added in machine polymer core particle dispersion, are reacted in reaction condition,
Volatilizable organic molecule is extracted in decompression out, and cooling is improved the additive of the anti-folding of cement-based material and tensile strength.
The polymerisable monomer A is to meet the one kind in below general formula (1)-(3) Organic substance:
Wherein, R1、R2、R3And R5Separately represent H or CH3, R4Represent the alkyl of 6-30 carbon atom, X1、X2、X3With
X4O or NH is separately represented, a, b are ethyoxyl (- CH2CH2O) chain link average repeat unit number, span is 4-50, c
Span be 6-12.The too small then autoemulsification of a, b and c value is weak, and value is excessive then compared to monomer B and cross-linking agent C
Polymerization activity is too low, so as to cause to residue in a large number in polymerization system because being difficult to copolymerization.Polymerisable monomer A is used to stablize first
The organic polymer nuclear particle of stage synthesis, the polymerisable emulsifier in the similar conventional emulsion polymerizations of its effect.Its consumption is same
There is impact closely to the size of the organic polymer nuclear particle of first stage synthesis, its consumption is higher, and particle size is less.
The polymerisable monomer B and polymerisable monomer D can be gathered by functional group's type monomer and non-functional group type monomer composition
The 0.5-5% that the monomer in monomer B accounts for polymerisable monomer B gross masses is closed, the monomer in polymerisable monomer D accounts for
The 0.5-5% of polymerisable monomer D gross masses, the monomer for hydroxyl, amino or carboxyl polymerisable monomer, be with
Under one kind in all monomers or more than one combination in any:Monomer's (containing amino) includes 3- aminobenzene second
The salt of alkene, 4- aminostyryls, 2- (tert-butylamino) ethyl methacrylate, aminoethyl methacrylate and these monomers
Hydrochlorate or sulfonate;Monomer's (containing carboxyl) includes the acid of acrylic acid, methacrylic acid and acrylic or methacrylic
Univalent metal salt (sodium salt and potassium salt);Monomer's (hydroxyl) is hydroxy acrylate or methacrylate, hydroxyl third
Acrylamide or hydroxymethylacrylamide class monomer, including acrylic acid -2- hydroxyl ethyl esters, 2-hydroxyethyl methacry-late (HEMA),
2-hydroxypropyl acrylate, acrylic acid -4- hydroxybutyls, methacrylic acid -2- hydroxy propyl esters, methacrylic acid -4- hydroxyl fourths
Ester, N hydroxymethyl acrylamide, N- hydroxyethyl acrylamides, N- (2- hydroxypropyls) acrylamide, N- hydroxymethyl, methyl acryloyls
Amine and N- (2- hydroxypropyls) Methacrylamide.
The non-functional group type monomer is the one kind in styrene and monomer shown in formula (4) or more than one any group
Close:
Wherein, R6Represent H or CH3, R7Represent the alkyl of 1-12 carbon atom.
Polymerisable monomer B and polymerisable monomer D is the main composition of organic polymer nuclear particle, its role is to provide
The preferable Organic substance matrix of toughness, for the final rupture strength and split tensile strength for lifting cement-based material.Polymerisable monomer D's
Composition can be identical from polymerisable monomer B, or different.
Organic polymer nuclear particle adds hydroxyl, amino or carboxylic polymerizable list when prepared by polymerization process
Body, so as to introduce hydroxyl, amino or carboxyl functional group on its surface, when intermediate layer covers, these amino or carboxyl official
Can roll into a ball and be reacted so as to play a part of with covalent bonded intermediate layer as reaction site part and outer layer, remaining site is received
Limit to reaction efficiency and do not change.
The cross-linking agent C is one kind or more than one combination in any in following material:Divinylbenzene, vinyl three
Methoxy silane, VTES, methacryloxypropyl trimethoxy silane, methacryloxy third
Ethyl triethoxy silicane alkane, methacryloxymethyl triethoxysilane, acryloyloxymethyl trimethoxy silane, propylene
Acryloxypropylethoxysilane trimethoxy silane.The effect of cross-linking agent C is the mechanical strength for lifting polymer beads daughter nucleus, reduces polymer
Dissolubility of the particle core in water.
The initiator is to thermally decompose initiator system initiator or the one kind in redox initiation system initiator, described
Thermal decomposition initiator system initiator is the isobutyl imidazoline hydrochloride (VA044) of azo two, double (the 2- methyl-prop amidines) two of 2,2'- azos
One kind in hydrochlorate (V50), Ammonium persulfate., potassium peroxydisulfate or sodium peroxydisulfate, in the redox initiation system initiator
Oxidant be H2O2, reducing agent is vitamin C or rongalite.
The redox initiation system initiator is also possible that oxidant is Ammonium persulfate., sodium peroxydisulfate or persulfuric acid
One kind in potassium, reducing agent is the one kind in sodium sulfite, sodium sulfite, sodium pyrosulfite or rongalite.
The oxidant of the redox initiation system initiator is 0.5-2.0 with the consumption mol ratio of reducing agent.
For thermal decomposition initiating, directly can once add, it is also possible to be slowly uniformly added into;For redox initiation
Agent, first adds polymerization system by required quality oxide agent, and then reductant solution is slowly uniformly added into polymerization system, and should not
Add before monomer all adds reaction system.Because the presence of half-life, thermal decomposition initiating elicitation procedure is relatively gentle, therefore
And can once add, it is also possible to slowly it is uniformly added into.But for redox initiation system, general activation energy is relatively low, such as
Fruit once adds and causes, then not only can be too low because of later stage number of free radical so that conversion ratio is low, early stage number of free radical mistake
Height is easily caused more serious gel effect so that polymeric viscosity is excessive.
The Organic substance E is the silane that a kind of more than three alkoxyls replace, and is tetraethoxysilane, tetramethoxy-silicane
Alkane, vinyltrimethoxy silane, VTES, methacryloxypropyl trimethoxy silane, methyl
Appointing in acryloxypropyl triethoxysilane, γ-mercaptopropyl trimethoxysilane or 3- aminopropyl triethoxysilanes
Meaning is a kind of.Organic substance E produces in the reaction organic siliconoxygen bond, passes through-Si-O- tetrahedral frameworks with sodium silicate and soluble inorganic
The inorganic composite of silicon-calcium-magnesium oxide that calcium salt and magnesium salt reaction are produced is connected with each other.
The inorganic component F is made up of sodium silicate and soluble inorganic salt, and affiliated soluble inorganic salt is by soluble inorganic
One or two compositions in calcium salt or soluble inorganic magnesium salt, mole total amount and silicon of the soluble inorganic salt cationic
The ratio of the mole of sour sodium be 0.8-1.0, the soluble inorganic calcium salt be calcium nitrate, calcium chloride, calcium acetate in one kind or
Several arbitrary proportion mixture, the soluble inorganic magnesium salt be magnesium acetate, magnesium chloride, magnesium nitrate or magnesium sulfate in one kind or
Several arbitrary proportion mixture.Calcium salt and magnesium sulfate can be used separately in same reaction and cannot be used in mixed way.
The gross mass of described polymerisable monomer A, B, D and cross-linking agent C and account for the 5- of polymerization system gross mass in step (1)
45%, the quality of the polymerisable monomer A accounts for the 0-5% of the gross mass of described polymerisable monomer A, B, D and cross-linking agent C, described
The quality of cross-linking agent C accounts for the 0-5% of the gross mass of described polymerisable monomer A, B, D and cross-linking agent C, the polymerisable monomer B's
Quality accounts for the ratio of the gross mass of polymerisable monomer B and D not less than 10%, the quality of the initiator account for polymerisable monomer A, B,
The 0.05-3% of D and cross-linking agent C gross masses.
The gross mass for limiting polymerisable monomer A, B, D and cross-linking agent C is because the additive not less than 5% for cement based
During material modification, mixing the solid effective ingredient consumption of system should be no less than the 0.5% of total glue material, and otherwise it is to mechanical property
Contribution it is unobvious.And if additive total solid content is too low, possibly use requirement cannot be met.Even if in fact, polymerizable
, less than under the conditions of total polymerization system solid content 5%, the reaction also can be successfully to carry out for monomer A, B, D and cross-linking agent C consumptions.
Initiator amount for monomer gross mass 0.05-3%, according to thermal decomposition initiating, then initiator quality consumption
For polymerisable monomer A, B, D and the 0.05-3% of cross-linking agent C gross masses;According to redox initiator, then consumption is aoxidizing
Side's gross mass that mole is relatively low in agent and reducing agent is calculated, and is polymerisable monomer A, B, D and cross-linking agent C gross masses
0.05-3%.Initiator amount may cause organic monomer conversion ratio not enough less than 0.05% monomer mass, if initiator amount
Higher than 3%, then may cruelly gather because initial velocity of initiation is too fast makes reaction failure (a large amount of precipitations or gel occur).
The gross mass of contained element silicon accounts for the organic polymer obtained in step (1) in the Organic substance E and inorganic component F
The 2-20% of particle gross mass, contained element silicon amount accounts for element silicon in Organic substance E and inorganic component F in the inorganic component F
The 0-25% of gross mass, if element silicon total amount is too low in Organic substance E used and inorganic component F, is difficult in organic polymer core
The silicon dioxide layer of adequate thickness is coated on particle;Consumption is too high, then when the additive is modified for cement-based material, need
The corresponding volume that improves could introduce enough organic constituentses so that the additive is to rupture strength under the conditions of low-dosage and splits drawing
The improvement of intensity is not obvious.Extra inorganic salt can be generated in inorganic component F courses of reaction, therefore its used in amounts will be controlled.Institute
The quality for stating organic polymer G accounts for the 2-50% of the organic polymer particle gross mass obtained in step (1).Organic polymer G
Consumption is too low can not to play Stabilization, when final additive described in the too high impact this patent of consumption is modified for cement-based material
Performance boost amplitude.
The organic polymer G is the elecrtonegativity organic polyelectrolyte of long side chain, the Weight-average molecular of the organic polymer G
Amount scope is 5000≤Mw≤100000.Too low then siloxanes covalent bond coupled reaction efficiency when for step (2) of molecular weight
Too low, molecular weight is too high, can significantly increase system viscosity.The inside and surface of the inorganic composite shell has by silicon
The elecrtonegativity organic polyelectrolyte of the belt length side chain that oxygen key is covalently attached, by Coulomb repulsion and space stability ultimate load hydridization grain
Son, enables fully dispersed in the cement-based material of highly basic high salt.
Organic polymer G is that (synthetic method can refer to for the polymer that prepared by radical copolymerization by monomer H, I and J
Document Journal of the Chinese Ceramic Society, 2014,42,635;Cement and Concrete
Research 2012,42,166)。
Monomer H is acrylic acid, methacrylic acid or corresponding sodium salt and the one kind in potassium salt, and monomer I is polyethyleneglycol
Methyl ether acetate, polyethylene glycol monomethyl ethermethacrylic acid esters, allyl polyethenoxy ether, methacrylic Polyethylene oxide
One kind in ether, cyclobutenyl polyoxyethylene ether, methyl butene base polyoxyethylene ether, vinyl polyoxyethylene ether, monomer J is ethylene
Base trimethoxy silane, VTES (VTES), methacryloxypropyl trimethoxy silane
(MAPTMS), methacryloxypropyl (MAPTES), methacryloxymethyl triethoxysilicane
One kind in alkane, acryloyloxymethyl trimethoxy silane, acryloxypropyl trimethoxy silane.
Polyglycol chain average repeat unit (- CH in monomer I structures2CH2O-) number span is 4-55, and value is too low
Its is sterically hindered so as to the effect of stable dispersion liquid particles to be difficult to performance, and too high then its polymerization activity of value is low, and residual quantity is higher,
Air content when affecting final dispersion liquid to be applied to cement-based material.
The molar fraction for accounting for total monomer (H+I+J) of monomer H, I and J is m1、n1、p1, its span meets m1+n1+p1
=100% and 2%≤m1≤ 80%, 0.5%≤n1≤ 96%, 2%≤p1≤ 30%.Monomer H provides elecrtonegativity functional group, single
Body I provides long side chain (sterically hindered effect), and monomer J provides silicone functionalities, make polymer G can by hydrolysis with-
The form of Si-O- is connected to the inorganic composite inside and surface that silicon-calcium-magnesium oxide is main body.
The molar fraction of H, I and J is too low to be unfavorable for that corresponding monomer effectively plays a role.Control monomer H molar fractions are not
It is that molar fraction in order to control I and J is not less than 20% higher than 80%, so that there is the sterically hindered functional group of enough offers
(from monomer I) is covalently attached on the particle prepared by step (2), makes particle more stable.J molar fractions are high, then polymer G
Efficiency high is covalently attached, but J molar fractions are too high, and polymer G may be caused water insoluble.
Reaction temperature in the step (1) is 20-90 DEG C, and the response time is 2-8h, and this area research worker can be with root
Judge the suitable initiation temperature of initiator used according to other documents and using experience, redox initiation system initiation temperature compared with
It is low, or even close room temperature, thermal decomposition initiator system initiation temperature can be according to its half-life decision.Polymerization time is longer, conversion ratio
It is higher.Body series polymerization time control in 2-8h, be usually necessary to ensure that initiator substantially completely decompose when polymerization is completed with
Exempt from the synthesis step on after and produce impact.
Reaction temperature in the step (2) is 40-90 DEG C, and the response time is 3-8h.Organic substance E, inorganic component F and have
Machine polymer G is in course of reaction uniform Deca, and in inorganic component F two kinds of components separate Deca (be made generally in aqueous solution,
And both component time for adding are identical), Organic substance E, inorganic component F and organic polymer G time for adding are controlled in 3-8h.
When temperature is high, response speed increases, and can adopt the relatively short response time;When temperature is low, typically using during relatively long reaction
Between.Time for adding is too short will in a large number to generate particle precipitation (silicon-calcium-magnesium inorganic composite and polymer G coupling polymer particles
Core), rather than the outer shell for being coated on step (1) gained organic polymer nuclear particle.The long then organic polymer G of time for adding holds
It is perishable, it is difficult to produce covalently bonded.
Beneficial effect:Additive of the present invention, will be to improve Mechanical Properties of Cement-based Materials by inorganic component
Organic constituentses coupled together with CSH granules by covalent bond, improve organic constituentses play toughness properties efficiency;Together
When, layer structure can pass through that stronger electrostatic repulsion and space steric effect are substantially stabilized to disperse these particles, enable with
Monodispersed (soilless sticking) form is scattered in cement-based material pore solution, further improves particle for cement matrix
Efficiency when material is modified.In addition, the outer layer of additive core-shell particles is with the composite oxides of silicon-calcium-magnesium as main component
Shell, can play a part of CSH gels induction nucleation and crystallization during hydrated cementitious, thus can greatly accelerate early stage
Hydrated cementitious, rather than extend the setting time of cement-based material, cement-based material early stage mechanical strength can be greatly improved.
Additive effective ingredient of the present invention is spheroidal particle, its all directions stress than fiber evenly, thus not
There are problems that orientation.
It is of the present invention compared to simple polymer-modified cementitious materials or polymer fiber and modified cement-based material
Admixture dosage can be greatly reduced (0.5-5.0% that core-shell particles consumption is total glue material quality), with traditional polymer emulsion
Cement-based material fracture resistance and tension (or splitting drawing) performance boost are become apparent under the conditions of same volume, overcomes conventional polymeric
The modified cement-based material of thing is because the high defect so as to affect Compressive Strength of Cement-based Materials of polymer volume.Even more enter one
Step, because the inorganic component for introducing can produce more CSH bonding components, has been lifted to Compressive Strength of Cement-based Materials.
Volume of the present invention refers to pure effective ingredient (hybrid inorganic-organic in the final aqueous dispersions for synthesizing of the invention
Particle) quality relative to glue material quality in cement-based material ratio.
The additive is modified for cement-based material, volume is higher, its rupture strength and tension (splitting drawing) intensity are improved
More obvious, the lifting amplitude of cement-based material rupture strength and tension (or splitting drawing) intensity is even up under the conditions of volume 5%
More than 25%, while to its comprcssive strength almost without negative effect.
Description of the drawings
Fig. 1 is the nucleocapsid structure transmission electron microscope picture of organic inorganic hybridization particle of the present invention.
Fig. 2 is gained particle energy dispersive x-ray spectroscopy (EDS) collection of illustrative plates of the embodiment of the present invention 2.
Fig. 3 is the infrared spectrogram (FT-IR) after the separated purification of each synthesis step of the embodiment of the present invention 2 gained particle.
Fig. 4 is the dynamic light scattering grain size distribution of each synthesis step of the embodiment of the present invention 2 gained particle.
Specific embodiment
In order to deepen the understanding of the present invention, below in conjunction with embodiment, the invention will be further described, these enforcements
Example is only used for the explanation present invention, does not constitute limiting the scope of the present invention.
In addition, usually, under the conditions of high solids content, these synthetic reactions are more difficult, for example, easily because response speed mistake
Fast and out of control (particle aggregation occur), high solids content can synthesize, then the aqueous dispersions of corresponding low-solid content can also be obtained.With
Lower embodiment is illustrated and contrasted with the preparation of high solids content sample.
1. the synthesis of organic polymer G
The synthesis of polymer G and molecular weight determination list of references (Journal of the Chinese Ceramic
Society,2014,42,635;Cement and Concrete Research 2012,42,166).
(1) organic polymer G01 (m1/n1/p1=2/96/2):
50 parts of distilled water and 0.5 are added in the round-bottomed flask equipped with thermometer, agitator, Dropping funnel and nitrogen conduit
Part mass concentration is 30% hydrogen peroxide, stirs and maintain temperature to be 30 DEG C.By 0.58 part of acrylic acid (AA), 97.44 parts of first
Epoxide polyethylene glycol acrylate (- CH2CH2O- average repeat units number 4, AAM4), 1.98 parts of methacryloxypropyls three
Methoxy silane (MAAPTMS), 0.388 part of vitamin C (VC), 0.42 part of TGA (MEA) and 100 parts of water are sufficiently stirred for mixing
Close, under nitrogen protection, the aqueous dispersions of uniform Deca AA/AAM4/MAAPTMS/VC/MEA in flask, time for adding control
For 5h, completion of dropwise addition continues insulation 1h can obtain the aqueous solution of polymer G02, and polymer effective solid content 40% surveys solid content
40.4%, weight average molecular weight 43700.This aqueous solution is directly used at once in follow-up preparation, is not isolated and purified.
(2) organic polymer G02 (m1/n1/p1=69/1/30):
Add in the round-bottomed flask equipped with thermometer, agitator, Dropping funnel and nitrogen conduit 50 parts of distilled water, 9.14
Part methacrylic Polyethylene Glycol (- CH2CH2O- average repeat units number 25, HPEG25), 44.51 parts of vinyl triethoxyl silicon
Alkane (VTES) and 0.5 part of mass concentration are 30% hydrogen peroxide, stir and maintain temperature to be 40 DEG C.By 46.34 parts of methyl-props
Olefin(e) acid (MAA), 0.388 part of VC, 0.14 part of MEA and 100 part of water are thoroughly mixed, under nitrogen protection, uniform in flask
The aqueous dispersions of Deca MAA/VC/MEA, time for adding is controlled to 3h, and completion of dropwise addition continues insulation 1h can obtain the water of polymer G01
Solution, polymer effective solid content 40% surveys solid content 40.3%, weight average molecular weight 96300.This aqueous solution is subsequently being prepared
In directly use at once, do not isolate and purify.
(3) organic polymer G03 (m1/n1/p1=80/10/10):
In the round-bottomed flask equipped with thermometer, agitator, Dropping funnel and nitrogen conduit, 50 parts of distilled water of addition,
71.24 parts of methyl butene base Polyethylene Glycol (- CH2CH2O- average repeat units number 52, IPEG52) and 0.5 part of mass concentration be
30% hydrogen peroxide, stirs and maintains temperature to be 45 DEG C.Prepare and contain 22.58 parts of sodium acrylate (AANa), 6.18 parts of acryloyls
Epoxide MTMS (AAMTMS), 0.388 part of vitamin C, 1.11 parts of TGAs and 100 parts of water dispersion liquid simultaneously
It is thoroughly mixed, under nitrogen protection, the aqueous dispersions of uniform Deca AANa/IPEG52/AAMTMS in flask, during Deca
Between be controlled to 2h, completion of dropwise addition continues to be incubated 1h can obtain the aqueous solution of polymer G03, polymer effective solid content 40%, actual measurement
Solid content 40.3%, weight average molecular weight 12600.This aqueous solution is directly used at once in follow-up preparation, is not isolated and purified.
(4) organic polymer G04 (m1/n1/p1=60/30/10):
In the round-bottomed flask equipped with thermometer, agitator, Dropping funnel and nitrogen conduit, add 50 parts of distilled water and
0.5 part of mass concentration is 30% hydrogen peroxide, stirs and maintain temperature to be 10 DEG C.Prepare and contain 17.67 parts of methacrylic acid potassium
(MAAK), 76.10 parts of methoxy polyethylene glycol methacrylate-styrene polymer (- CH2CH2O- average repeat units number 22, MAAM22),
6.22 parts of methacryloxymethyl triethoxysilanes (MAAMTES), 0.388 part of vitamin C, 1.26 parts of TGAs and
The dispersion liquid of 100 parts of water is simultaneously thoroughly mixed, under nitrogen protection, uniform Deca MAAK/MAAM22/ in flask
The aqueous dispersions of MAAMTES, time for adding is controlled to 5h, and completion of dropwise addition continues insulation 1h can obtain the aqueous solution of polymer G04, gather
Compound effective solid content 40%, surveys solid content 40.5%, weight average molecular weight 5400.This aqueous solution is straight at once in follow-up preparation
Connect and use, do not isolate and purify.
2. the synthesis of additive
Polymerisable monomer used below is commercial goods, or synthesizes the gained (source of polymerisable monomer A according to document:
(1) it is commercially available;(2) macromolecule circular, 2008,16;Polymer Bulletin 1999,42287;Journal of Applied
Polymer Science 2000,77,2768;(3)Langmuir 2001,17,6077-6085.).
4- aminostyryl hydrochlorates (4-VBAH) is composite, and reference literature synthesizes gained (Analytical
Chemistry 2012,84,3500)。
Embodiment 1
(1) polymerisable monomer A (numbering A1, polyethylene glycol methacrylate-styrene polymer, polyglycol chain are added in reactor
In-CH2CH2O- average repeat units number is 6, and end group is hydroxyl, 0.1 part of consumption), polymerisable monomer B (AA0.29 parts and methyl
9.22 parts of acrylic acid methyl ester. (MMA)), (5 parts of divinylbenzene (DVB), commodity DVB includes meta and para-position isomery to cross-linking agent C
Body) and 92.22 parts of water, it is thoroughly mixed;Lead to N in mixed liquor2Except O2, temperature of reactor is risen to into 80 DEG C, under stirring condition
Once add in reactor initiator (0.05 part of Ammonium persulfate. APS is dissolved in 30 parts of water) cause polymerization, start simultaneously to
Deca polymerisable monomer D (4.28 parts of acrylic acid and MMA81.13 parts), Deca 5h in reactor.Self-initiating agent is initially added into reaction
Timing during device, reacts 6h under polymerizing condition, then removes inert atmosphere protection, obtains organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 40 DEG C, be added thereto to 19.69 parts of water, stir
Under the conditions of in organic polymer nuclear particle dispersion liquid the uniform the desired amount of Organic substance E of Deca (tetraethoxysilane TEOS,
13.37 parts, 1.8 parts of silicon content), (0.87 part of sodium silicate is dissolved in 5.00 parts of water, 0.2 part of silicon content to inorganic component F;One hydration vinegar
1.01 parts of sour calcium is dissolved in 10.00 parts of water) and 25.00 parts of organic polymer G01 aqueous solutions having prepared, dropwise reaction 8h.Reaction
Volatilizable organic molecule is extracted in decompression after end out, and the additive of the anti-folding of cement-based material and tensile strength is improved needed for can obtaining
W01。
Embodiment 2
(1) polymerisable monomer A (numbering A2, monomethyl polyethylene glycol acrylate ester, polyglycol chain are added in reactor
In-CH2CH2O- average repeat units number is 22, and end group is methyl, and consumption is 2.00 parts), polymerisable monomer B (4- aminobenzene second
97.51 parts of 0.49 part of pinene hyhrochloride (4-VBAH) and styrene (St)), 3 parts of APS and 92.22 part of water, be thoroughly mixed;To
Lead to N in mixed liquor2Except O2, temperature of reactor is risen to into 70 DEG C, under stirring condition in reactor uniform Deca initiator (1.71
Part sodium sulfite SBS is dissolved in 30 parts of water) cause polymerization, Deca 6h.Timing when self-initiating agent is initially added into reactor, in
7h is reacted under polymerizing condition, then removes inert atmosphere protection, obtain organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 60 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca in particle dispersion (tetramethoxy-silicane TMOS, 48.86 parts, 9.0 parts of silicon content), without unit
Divide F (4.36 parts of sodium silicate is dissolved in 20.00 parts of water, 1.0 parts of silicon content;6.29 parts of Calcium diacetate monohydrate is dissolved in 42.92 parts of water) and
37.50 parts of organic polymer G02 aqueous solutions, dropwise reaction 4h.Volatilizable organic molecule is extracted in decompression after reaction terminates out, can
The additive W02 of the anti-folding of cement-based material and tensile strength is improved needed for obtaining.
As shown in figure 1, by the particle obtained by step (2) Jing process after carry out transmission electron microscope shooting, in figure some particles by
The shell for causing script contrast relatively low in particle overlap is difficult to observe, but from monolayer morphology of particles, it is apparent that nucleocapsid
Clear in structure is visible, has marked the outer layer A and inner layer B of particle in figure respectively.
The sample Jing dialysis purifications of step (2) are dropped on silicon chip, its EDS power spectrum (Fig. 2) is observed and tested with SEM, by
High-visible C, the O and Ca element peak (K α and K β) therein of power spectrum, light element C peaks signal itself is weaker, is difficult quantitative.
Fig. 3 is the infrared spectrum (FT- of the particle that step (1)-(2) (Step (1)-Step (2)) obtain in embodiment 2
IR), the sample of all FT-IR tests is through dialysis purification.Step (1) correspondences step (1), Step (2) -1 are step (2) conjunction
Into the nucleocapsid structure that midway (aqueous solution of Organic substance E, inorganic component F and organic polymer G02 Deca 3h) is taken out, Step
(2) -2 is the nucleocapsid structure that embodiment 2 finally gives.
As seen from Figure 3,1581cm in Step (1) spectrogram-1And 1603cm-1, and 3000cm-1-3120cm-1In the range of (can
Point out as unsaturated c h bond) multiplet prove phenyl ring (polystyrene agent structure), from Step (1) to Step (2) -1 again to
Step (2) -2,920-1130cm in spectrogram-1In the range of absorption intensity progressively strengthen in step (2), especially 965,
1070cm-1Two are respectively belonging to Si-O (CSH, Q2) and Si-O (Si-rich phase, SiO2) stretching vibration peak, (Cement and
Concrete Research 2009,39147), spectrogram 1650cm-1Nearby increase an absworption peak, be attributed to carboxylic acid (salt) carbonyl
Base stretching vibration peak, while 2800-3000cm-1In the range of belong to the stretching vibration peak of C-H, this region is relative to 3000cm-1-3120cm-1In the range of unsaturation C-H vibration ratio be increased slightly, it was demonstrated that saturation c h bond increased, contrast synthesis bar
Part confirms as organic polymer G and is constantly connected to during step (2) on particle (to be wrapped in outer layer).In addition, spectrum
3240-3700cm in figure-1Broad peak belongs to the stretching vibration of OH, should be the water of CSH phases.
Fig. 4 is the dynamic light scattering particle diameter of the particle that step (1)-(2) (Step (1)-Step (2)) obtain in embodiment 2
Scattergram, as can be seen from the figure particle radii increase in building-up process.
Embodiment 3
(1) polymerisable monomer A (numbering A3, polyethylene glycol monomethyl ethermethacrylic acid esters, poly- second two are added in reactor
- CH in alcohol chain2CH2O- average repeat units number be 45, consumption be 5.00 parts), polymerisable monomer B (acrylic acid -2- hydroxyl ethyl esters
(HEA) 9.10 parts of 1.38 parts, n-butyl acrylate (n-BuA) 17.12 and lauryl acrylate (LA)), Part I cross-linking agent C
(1 part of DVB) and 92.22 parts of water, are thoroughly mixed;Lead to N in mixed liquor2Except O2, temperature of reactor is risen to into 60 DEG C, stirring
Under the conditions of once add in reactor initiator (1 part of azo diisobutyl amidine hydrochlorate V50 is dissolved in 30 parts of water) cause
Polymerization, start simultaneously in reactor Deca Part II cross-linking agent C (2 parts of DVB) polymerisable monomer D (4-VBAH1.29 parts and
MMA63.11 parts), Part II cross-linking agent C and polymerisable monomer D Deca 3h.Timing when self-initiating agent is initially added into reactor,
4h is reacted under polymerizing condition, then removes inert atmosphere protection, obtain organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp rises to 80 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (VTES VTES101.79 parts, 15 parts of silicon content), nothing in particle dispersion
(21.79 parts of sodium silicate is dissolved in 75.00 parts of water, 1.0 parts of silicon content to machine component F;37.95 parts of calcium nitrate tetrahydrate is dissolved in 52.26 parts
Water) and with 5.00 parts of organic polymer G03 aqueous solutions, dropwise reaction 8h.Decompression after reaction terminates extracts volatilizable organic little out
Molecule, improves the additive W03 of the anti-folding of cement-based material and tensile strength needed for can obtaining.
Embodiment 4
(1) polymerisable monomer A (numbering A4, N- poly glycol monomethyl ethers-acrylamide, poly- second two are added in reactor
- CH in alcohol chain2CH2O- average repeat units number be 45,0.1 part of consumption), polymerisable monomer B (0.75 part of acrylic acid, metering system
1.73 parts of sour (MAA) and n-BuA46.93 parts) and 92.22 parts of water, it is thoroughly mixed;Lead to N in mixed liquor2Except O2, will react
Device temperature rises to 50 DEG C, under stirring condition in reactor uniform Deca initiator (2 parts of isobutyl imidazoline hydrochlorides of azo two
VA044 is dissolved in 30 parts of water) cause polymerization, start simultaneously at Deca cross-linking agent C (1 part of DVB) and polymerizable list in reactor
Body D (0.25 part of 2-hydroxypropyl acrylate (HPA), 24.61 parts of MMA and 24.64 part of St), initiator, cross-linking agent C and can gather
Close equal Deca 6h of monomer D.Timing when self-initiating agent is initially added into reactor, reacts 8h under polymerizing condition, then removes indifferent gas
Atmosphere is protected, and obtains organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp rises to 80 DEG C, to organic polymer core under stirring condition
It is the desired amount of Organic substance E of Deca (MTMS MTMOS7.29 parts, 1.5 parts of silicon content) in particle dispersion, inorganic
(2.18 parts of sodium silicate is dissolved in 20.00 parts of water, 0.5 part of silicon content to the aqueous solution of component F;1.71 parts of anhydrous magnesium sulfates are dissolved in
16.19 parts of water) and 125.00 parts of organic polymer G04 aqueous solutions, dropwise reaction 3h.Reaction terminates decompression and extracts volatilizable out
Organic molecule, improves the additive W04 of the anti-folding of cement-based material and tensile strength needed for can obtaining.
Embodiment 5
(1) polymerisable monomer A is added in reactor, and (numbering A5,4- (8- acryloyl-oxies) n-octyloxy benzene sulfonic acid sodium salt are used
Measure as 3.00 parts), polymerisable monomer B (0.18 part of methacrylic acid -2- amino ethyl ester hydrochlorates (AEMH) and n-octyl
(n-OctA) 9.02 parts), Part I cross-linking agent C (0.2 part of VTES (VTES) and 0.3 part of DVB), 0.13
The H of part mass fraction 30%2O2Aqueous solution and 92.22 parts of water, are thoroughly mixed;Lead to N in mixed liquor2Except O2, by reactor
Temperature maintains 20 DEG C, under stirring condition in reactor uniform Deca initiator (0.1 part of vitamin C (VC) is dissolved in 30 parts
In water) cause polymerization, start simultaneously in reactor Deca Part II cross-linking agent C (1.8 parts of VTES and 2.7 part of DVB) and can
Polymerized monomer D (3- aminostyryls (3-VBA) 0.41 part and n-BuA82.39 parts), initiator, Part II cross-linking agent C and can
Equal Deca 2h of polymerized monomer D.Timing when self-initiating agent is initially added into reactor, reacts 3h under polymerizing condition, then removes inertia
Atmosphere protection, obtains organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp rises to 40 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (tetramethoxy-silicane TMOS40.71 parts, 7.5 parts of silicon content), inorganic component in particle dispersion
(10.89 parts of sodium silicate is dissolved in 35 parts of water, 2.5 parts of silicon content to the aqueous solution of F;21.08 part calcium nitrate tetrahydrate is dissolved in
32.42 parts of water) and 37.50 parts of organic polymer G04 aqueous solutions, dropwise reaction 8h.Reaction end decompression extraction is volatilizable to be had
Machine small molecule, improves the additive W05 of the anti-folding of cement-based material and tensile strength needed for can obtaining.
Embodiment 6
(1) polymerisable monomer A (numbering A6, dodecyl-poly glycol monomethyl ether-maleic acid are added in reactor
Dibasic acid esters ,-CH2-CH2O- average repeat units number 45, consumption be 5.00 parts), polymerisable monomer B (2-hydroxypropyl acrylates (HPA)
0.47 part and 92.54 parts of acrylic acid methyl ester. (MA)), cross-linking agent C (2 parts of VTES), 2.4 parts of sodium peroxydisulfates (SPS) and 92.22 parts
Water, is thoroughly mixed;Lead to N in mixed liquor2Except O2, temperature of reactor is maintained into 60 DEG C, under stirring condition in reactor
Uniform Deca initiator (1 part of sodium pyrosulfite (SMBS) is dissolved in 30 parts of water) causes polymerization, Deca 3.5h.Self-initiating agent is opened
Timing when beginning to add reactor, reacts 4h under polymerizing condition, then removes inert atmosphere protection, obtains organic polymer nuclear particle
Dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 40 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (TEOS111.43 parts, 15 parts of silicon content), the aqueous solution (silicon of inorganic component F in particle dispersion
4.36 parts of sour sodium is dissolved in 40.00 parts of water, 1 part of silicon content;4.76 parts of magnesium nitrate is dissolved in 41.13 parts of water) and 25.00 parts it is organic
Polymer G03 aqueous solutions, dropwise reaction 6h.Reaction terminates decompression and extracts volatilizable organic molecule out, and water is improved needed for can obtaining
The additive W06 of the anti-folding of cement-based material and tensile strength.
Embodiment 7
(1) polymerisable monomer B (0.14 part of sodium acrylate and lauryl methacrylate (LMA) are added in reactor
28.36 parts), Part I cross-linking agent C (4 parts of VTES), the H of 2.02 parts of mass fractions 30%2O2Aqueous solution and 92.22 parts of water, fill
Divide stirring mixing;Lead to N in mixed liquor2Except O2, temperature of reactor is maintained into 30 DEG C, it is uniform in reactor under stirring condition
Deca initiator (2.5 parts of rongalites (SFA) are dissolved in 30 parts of water) causes polymerization, starts simultaneously in reactor
Deca Part II cross-linking agent C (1 part of DVB) polymerisable monomer D (AEMH0.92 parts, 3-VBA0.41 parts, LMA12.74 parts and
St52.43 parts), initiator, Part II cross-linking agent C and equal Deca 5h of polymerisable monomer D.Self-initiating agent is initially added into reactor
When timing, 6h is reacted under polymerizing condition, then remove inert atmosphere protection, obtain organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp rises to 90 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (MTMOS9.52 parts, 1.96 parts of silicon content), the aqueous solution of inorganic component F in particle dispersion
(0.17 part of sodium silicate is dissolved in 15.76 parts of water, 0.04 part of silicon content;0.20 part of magnesium acetate is dissolved in 20 parts of water) and 125.00 parts
Organic polymer G02 aqueous solutions, dropwise reaction 3h.Reaction terminates decompression and extracts volatilizable organic molecule out, carries needed for can obtaining
The anti-additive W07 rolled over tensile strength of high cement-based material.
Embodiment 8
(1) polymerisable monomer A (numbering A8, polyethylene glycol monomethyl ethermethacrylic acid esters, poly- second two are added in reactor
- CH in alcohol chain2CH2O- average repeat units number is 22, and end group is methyl, and consumption is 2.00 parts), polymerisable monomer B (methyl-props
0.41 part of olefin(e) acid ammonia carbethoxy hydrochloride (AEMH), 2.01 parts of methacrylic acid -2- t-butylaminoethyls (t-BAEMA) and methyl
46.55 parts of acrylic acid methyl ester. (MMA)) and 92.22 parts of water, it is thoroughly mixed;Lead to N in mixed liquor2Except O2, by reactor temperature
Degree maintains 90 DEG C, and uniform Deca initiator (3 parts of SPS are dissolved in 30 parts of water) causes poly- in reactor under stirring condition
Close, start simultaneously at Deca polymerisable monomer D (MAA2.45 parts and LMA46.55 parts), initiator and polymerizable list in reactor
Equal Deca 2h of body D.Timing when self-initiating agent is initially added into reactor, reacts 4h under polymerizing condition, then removes inert atmosphere guarantor
Shield, obtains organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 70 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (3- aminopropyl trimethoxysilane APTMS115.07 parts, silicon content 18 in particle dispersion
Part), (8.71 parts of sodium silicate is dissolved in 82.28 parts of water, 2 parts of silicon content to the aqueous solution of inorganic component F;10.14 part magnesium acetate dissolves
In 70 parts of water) and 5.00 parts of organic polymer G01 aqueous solutions, dropwise reaction 4h.Reaction terminates decompression and extracts volatilizable organic out
Small molecule, improves the additive W08 of the anti-folding of cement-based material and tensile strength needed for can obtaining.
Embodiment 9
(1) in reactor add polymerisable monomer A (numbering A9,4- (10- acryloyl-oxies) n-decyloxy benzene sulfonic acid sodium salt,
Consumption is 5.00 parts), polymerisable monomer B (N hydroxymethyl acrylamide (N-HMAAm) 0.18 part and MMA9.02 parts), cross-linking agent C
(2.7 parts of methacryloxypropyl trimethoxy silanes MAAPTMS and 0.3 part of VTES) and 92.22 parts of water, are sufficiently stirred for mixing
Close;Lead to N in mixed liquor2Except O2, temperature of reactor is maintained into 85 DEG C, uniform Deca causes in reactor under stirring condition
Agent (0.1 part of potassium peroxydisulfate KPS is dissolved in 30 parts of water) causes polymerization, starts simultaneously at the Deca polymerisable monomer D in reactor
(1.66 parts of methacrylic acid -2- hydroxy methacrylates (HEMA) and MMA81.14 parts), initiator and equal Deca 5h of polymerisable monomer D.
Timing when self-initiating agent is initially added into reactor, reacts 8h under polymerizing condition, then removes inert atmosphere protection, obtains organic poly-
Compound nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 60 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (MTES MTEOS54.13 parts, 8.5 parts of silicon content), nothing in particle dispersion
(6.54 parts of sodium silicate is dissolved in 29.77 parts of water, 2 parts of silicon content to the aqueous solution of machine component F;5.69 parts of calcium nitrate tetrahydrate and vinegar
3.42 parts of sour magnesium is dissolved in 40 parts of water) and 5.00 parts of organic polymer G02 aqueous solutions, dropwise reaction 4h.Reaction terminates decompression and takes out
Go out volatilizable organic molecule, the additive W09 of the anti-folding of cement-based material and tensile strength is improved needed for can obtaining.
Embodiment 10
(1) polymerisable monomer B (MAA5 parts and t-BuA95 parts) and 92.22 parts of water are added in reactor, is sufficiently stirred for mixing
Close;Lead to N in mixed liquor2Except O2, temperature of reactor is maintained into 80 DEG C, once add in reactor under stirring condition and cause
Agent (3 parts of APS are dissolved in 30 parts of water) causes polymerization.Timing when self-initiating agent is initially added into reactor, it is anti-under polymerizing condition
4h is answered, then removes inert atmosphere protection, obtain organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 60 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (VTES66.50 parts, 9.8 parts of silicon content), the aqueous solution (silicon of inorganic component F in particle dispersion
0.87 part of sour sodium is dissolved in 20.00 parts of water, 0.2 part of silicon content;0.10 part of Calcium diacetate monohydrate is dissolved in 20.00 parts of water;0.73
Part magnesium acetate is dissolved in 34.56 parts of water) and 125.00 parts of organic polymer G01 aqueous solutions, dropwise reaction 8h.Reaction terminates decompression
Extract volatilizable organic molecule out, the additive W10 of the anti-folding of cement-based material and tensile strength is improved needed for can obtaining.
Embodiment 11
(1) polymerisable monomer A (numbering A10, dodecyl-poly glycol monomethyl ether-maleic acid are added in reactor
Dibasic acid esters ,-CH2-CH2O- average repeat units number 6, consumption be 3.00 parts), polymerisable monomer B (3- aminostyryls (3-VBA)
0.57 part and St27.93 parts) and 92.22 parts of water, it is thoroughly mixed;Lead to N in mixed liquor2Except O2, temperature of reactor is maintained
At 70 DEG C, under stirring condition in reactor uniform Deca initiator (0.5 part of APS is dissolved in 15 parts of water;0.55 part of sulfurous acid
Sodium SS is dissolved in 15 parts of water, and both distinguish Deca) cause polymerization, start simultaneously at (2 part third of the Deca cross-linking agent C in reactor
Alkene pivaloyloxymethyl trimethoxy silane AAMTMS) and polymerisable monomer D (AEMH2 parts and LA64.51 parts), initiator, residue
Partial cross-linked dose of C and equal Deca 2.5h of polymerisable monomer D.Timing when self-initiating agent is initially added into reactor, under polymerizing condition
Reaction 3h, then inert atmosphere protection is removed, obtain organic polymer nuclear particle dispersion liquid.
(2) treat that gained organic polymer nuclear particle dispersion liquid temp is down to 50 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (TEOS20.06 parts, 2.7 parts of silicon content), the aqueous solution (silicon of inorganic component F in particle dispersion
1.31 parts of sour sodium is dissolved in 10.00 parts of water, 0.3 part of silicon content;0.13 part of 1.82 parts of calcium nitrate tetrahydrate and magnesium nitrate are dissolved in
27.96 parts of water) and 25.00 parts of organic polymer G04 aqueous solutions, dropwise reaction 6h.Reaction end decompression extraction is volatilizable to be had
Machine small molecule, improves the additive W11 of the anti-folding of cement-based material and tensile strength needed for can obtaining.
Embodiment 12
(1) polymerisable monomer A (numbering A7, dodecyl-hydroxyl polyethylene glycol groups-maleic acid are added in reactor
Dibasic acid esters ,-CH2-CH2O- average repeat units number 32, consumption be 5.00 parts), polymerisable monomer B (HEMA0.23 parts and LMA44.78
Part), Part I cross-linking agent C (2.5 parts of VTES) and 92.22 parts of water, be thoroughly mixed;Lead to N in mixed liquor2Except O2, will be anti-
Device temperature is answered to maintain 60 DEG C, uniform Deca initiator (1 part of V50 is dissolved in 30 parts of water) is drawn in reactor under stirring condition
Polymerization is sent out, the Deca Part II cross-linking agent C (2.5 parts of VTES) and polymerisable monomer D (HEMA0.23 in reactor is started simultaneously at
Part and LMA44.78 parts), initiator, Part II cross-linking agent C and equal Deca 4h of polymerisable monomer D.Self-initiating agent is initially added into
Timing during reactor, reacts 6h under polymerizing condition, then removes inert atmosphere protection, obtains the dispersion of organic polymer nuclear particle
Liquid.
(2) gained organic polymer nuclear particle dispersion liquid temp is maintained to be 60 DEG C, to organic polymer core under stirring condition
The desired amount of Organic substance E of Deca (TEOS118.86 parts, 16 parts of silicon content), the aqueous solution (silicon of inorganic component F in particle dispersion
17.43 parts of sour sodium is dissolved in 52.69 parts of water, 4 parts of silicon content;13.50 parts of calcium nitrate tetrahydrate is dissolved in 20 parts of water;12.17 parts
Magnesium acetate is dissolved in 30 parts of water) and 7.14 parts of organic polymer G03 aqueous solutions, dropwise reaction 8h.Reaction terminates decompression extraction can
The organic molecule of volatilization, improves the additive W12 of the anti-folding of cement-based material and tensile strength needed for can obtaining.
3. additive is used for the modified test of cement-based material
Application Example 1
Improvement to mortar mechanical property:Mortar is prepared using little wild field PII52.5 cement, iso standard sand, sand-lime
Than for 3:1, the ratio of mud is 0.36, and the volume of additive W01-W12, PE01-PE04 is that the folding on the basis of Binder Materials is measured admittedly
Calculate, basically identical by defoamer consumption control each group mortar air content, water reducer used is that Su Bote companies markets are common
Conventional polycarboxylate water-reducer- I, controls each group Mortar'S Flowability basically identical by water reducer consumption.Specimen molding
After be placed in 25 DEG C, conserve under more than 95% damp condition.
PE01:Carboxy (SD622S) emulsion of Shanghai Gaoqiao BASF dispersion company limited;
PE02:According to document synthesis (Journal of Materials in Civil Engineering 2011,23,
1412), its stability is slightly worse, and coagulation can occur in cement filtrate;W01-W12 will not coagulation in cement filtrate;
PE03:BASF pure-acrylic emulsions (Acronal PA 237);
PE04:BASF styrene-acrylic emulsions (Acronal S 400).
The mortar performance of table 1 tests table
Note:Volume refers to pure effective ingredient (hybrid inorganic-organic grain in the aqueous dispersions that various embodiments of the present invention finally synthesize
Son) quality relative to glue material quality in cement-based material ratio.
From experimental result in table, under the conditions of the identical ratio of mud, synthesis additive W01-W12 shown in the embodiment of the present invention
When for modifying mortar:
(1) it is right to mortar comprcssive strength without negative effect (relative to the 1.0% of cement consumption) under the conditions of low-dosage
Its tension and there is a certain degree of lifting, rupture strength also has certain lifting.By contrast, using common polymer emulsion
(commercially available or synthesis, PE01, PE02) nothing is obviously improved.
(2) lift the volume such as W01 to 2.5%, W01, W05 and W09 to mortar comprcssive strength substantially without negative effect, to it
Tensile strength has a certain degree of lifting (28 days strength enhancing~13%), and rupture strength also has certain lifting, and (intensity is carried within 28 days
Rise~30%).By contrast, using common polymer emulsion (commercially available or synthesis, PE01, PE02), action effect is relatively
It is weak.
(3) lift the volume such as W01 without negative effect or to have lifted mortar comprcssive strength to 5.0%, W01-W12
(0%-18%), while having a certain degree of lifting (28 days strength enhancing 13-33%) to its tensile strength, rupture strength also has
It is certain to lift (28 days strength enhancing 22-43%).By contrast, using common polymer emulsion (commercially available or synthesis, PE01-
PE02), although the tension rupture strength of mortar has been lifted and (lifted amplitude respectively~10% and 10-15%, but its pressure resistance
Degree has different degrees of reduction (~10%).
(4) addition of W01-W12 is obviously promoted effect, phase to early age strength of concrete (10h resistance to compressions and anti-folding) development
Than under, PE01-PE04 is to early age strength of concrete development is without facilitation or has retarding action.
It can be seen that the lifting of W01, W05 and W09 volume folding anti-to mortar and tensile strength in the 1-2.5% of cement consumption is
Jing can reach the performance during polymer emulsions 5% such as addition PE01-PE04, while W01, W05 and W09 are to agent on crack resistance of concrete pressure
Spend and have no adverse effect, show obvious advantage.
Application Example 2
Mechanical performance of concrete test is carried out with reference to GB/T50080-2002 and GB/T50081-2002, using reference water
Mud, II level flyash, modulus of fineness is 2.6 river sand, the rubble of 5-25mm continuous gradings.Concrete mix is shown in Table 2, coagulation
Native result of the test is shown in Table 3.
Concrete mix (the kg/m of table 23)
Cement | Flyash | Sand | Stone | Water |
373 | 77 | 700 | 1130 | 145 |
The volume of additive W01-W12, PE01-PE04 is that the folding on the basis of Binder Materials measures calculating admittedly, by froth breaking
Agent control each group mortar air content is basically identical, and water reducer used is the polycarboxylate water-reducer of Su Bote companies market normal conventionals- I, controls each group slump basically identical (20 ± 1cm) by water reducer consumption.25 are placed in after specimen molding
DEG C, conserve under more than 95% damp condition.
The testing concrete performance table of table 3
Note:Volume refers to pure effective ingredient (hybrid inorganic-organic grain in the aqueous dispersions that various embodiments of the present invention finally synthesize
Son) quality relative to glue material quality in cement-based material ratio.
From experimental result in table, under the conditions of the identical ratio of mud, synthesis additive W01-W12 shown in the embodiment of the present invention
When for concrete:
(1) it is right to concrete crushing strength without negative effect (relative to the 1.0 of cement consumption) under the conditions of low-dosage
It splits drawing and rupture strength also certain lifting.By contrast, using common polymer emulsion (commercially available or synthesis, PE01,
PE02) nothing is obviously improved.
(2) lift the volume such as W01 to 2.5%, W01, W05 and W09 to mortar comprcssive strength substantially without negative effect, to it
Split tensile strength has a certain degree of lifting (28 days strength enhancing 10-16%), and rupture strength also has certain lifting, and (intensity is carried within 28 days
Rise 24-34%).By contrast, using common polymer emulsion (commercially available or synthesis, PE01, PE02), action effect is relatively
It is weak.
(3) volume such as lifting W01 without negative effect or has been carried substantially to 5.0%, W01-W12 to concrete crushing strength
Rise (0%-15%), while being obviously improved (28 days strength enhancing 11-26%) to its split tensile strength, rupture strength also has necessarily
Lifted (28 days strength enhancing 24-50%).By contrast, using common polymer emulsion (commercially available or synthesis, PE01-
PE02), although the tension rupture strength of concrete has been lifted and (lifted amplitude respectively~10% and 10-15%, but its resistance to compression
Intensity has different degrees of reduction.
(4) addition of W01-W12 is obviously promoted effect, phase to early age strength of concrete (10h resistance to compressions and anti-folding) development
Than under, PE01-PE04 is to early age strength of concrete development is without facilitation or has retarding action.
It can be seen that W01, W05 and W09 volume in the 1-2.5% of cement consumption to concrete split tensile strength and tensile strength
Lifting can reach the performance during polymer emulsions 5% such as addition PE01-PE04, while W01, W05 and W09 are to concrete
Comprcssive strength simultaneously has no adverse effect, and shows obvious advantage.
It should be noted that for mortar specimen, general experiment can determine tensile strength;For concrete sample, lead to
Tensile splitting strength, the value and being proportionate property of tensile strength are often determined, but (typically slightly above tension is strong to be not equal to tensile strength
Degree), tensile splitting strength is higher, and tensile strength is higher.
The abbreviation of monomer used and initiator in the polymerizing condition of table 4 is represented
。
Claims (8)
1. it is a kind of to improve the anti-additive rolled over tensile strength of cement-based material, it is characterised in that the additive is a kind of tool
There are the aqueous dispersions of the hybrid inorganic-organic particle of nucleocapsid structure, the hybrid inorganic-organic particle is made up of inside and outside two-layer,
Internal layer is organic polymer core, and outer layer is the inorganic composite oxide that inorganic composite oxide or organo-functional group are covalently attached,
Affiliated inorganic composite oxide is silicon-calcium composite oxides or silicon-Magnesium coumpoud oxide or silicon-calcium-Magnesium coumpoud oxide, described
Being covalently attached in the layer of outer layer has elecrtonegativity organic polyelectrolyte;
The organic polymer core is prepared from by polymerisable monomer A, polymerisable monomer B, polymerisable monomer D and cross-linking agent C, institute
It is the one kind met in below general formula (1)-(3) Organic substance to state polymerisable monomer A:
Wherein, R1、R2、R3And R5Separately represent H or CH3, R4Represent the alkyl of 6-30 carbon atom, X1、X2、X3And X4
O or NH is separately represented, a, b are ethyoxyl (- CH2CH2O) chain link average repeat unit number, span is 4-50, c's
Span is 6-12;
The polymerisable monomer B and polymerisable monomer D is by functional group's type monomer and non-functional group type monomer composition, polymerizable list
Monomer in body B accounts for the 0.5-5% of polymerisable monomer B gross masses, and the monomer in polymerisable monomer D accounts for can be gathered
Close monomer D gross masses 0.5-5%, the monomer for hydroxyl, amino or carboxyl polymerisable monomer, the non-official
It is the one kind or more than one combination in any in styrene and monomer shown in formula (4) that type monomer can be rolled into a ball:
Wherein, R6Represent H or CH3, R7Represent the alkyl of 1-12 carbon atom;
The cross-linking agent C is one kind or more than one combination in any in following material:Divinylbenzene, vinyl trimethoxy
Base silane, VTES, methacryloxypropyl trimethoxy silane, methacryloxypropyl three
Ethoxysilane, methacryloxymethyl triethoxysilane, acryloyloxymethyl trimethoxy silane, acryloyl-oxy
Base propyl trimethoxy silicane.
2. it is a kind of to improve the anti-preparation method rolled over the additive of tensile strength of cement-based material, it is characterised in that step is such as
Under:
(1) polymerisable monomer A, polymerisable monomer B, Part I cross-linking agent C and water are added in reactor, is sufficiently stirred for mixing
Close;Lead to N in mixed liquor2Except O2, reactor is risen to into reaction temperature, add initiator to cause in reactor under stirring condition
Polymerization, starting simultaneously at the mixed liquor of Deca Part II cross-linking agent C and polymerisable monomer D in reactor carries out copolymerization, described
Part I cross-linking agent C and Part II cross-linking agent C is arbitrary proportion, and reaction end obtains the dispersion of organic polymer nuclear particle
Liquid;
(2) organic polymer nuclear particle dispersion liquid prepared by step (1) is adjusted to temperature required, is gathered to organic under stirring condition
Organic substance E, organic polymer G and inorganic component F are added in compound nuclear particle dispersion liquid, is reacted in reaction condition, reduced pressure
Extract volatilizable organic molecule out, cooling is improved the additive of the anti-folding of cement-based material and tensile strength;
The Organic substance E is the silane that a kind of more than three alkoxyls replace;
The inorganic component F is made up of sodium silicate and soluble inorganic salt, the soluble inorganic salt cationic it is mole total
Amount is 0.8-1.0 with the ratio of the mole of sodium silicate;
The organic polymer G is the elecrtonegativity organic polyelectrolyte of long side chain, weight average molecular weight range be 5000≤Mw≤
100000;
The gross mass of described polymerisable monomer A, B, D and cross-linking agent C accounts for the 5-45% of polymerization system gross mass in step (1), institute
State polymerisable monomer A quality account for described polymerisable monomer A, B, D and cross-linking agent C gross mass 0-5%, the cross-linking agent C
Quality account for described polymerisable monomer A, B, D and cross-linking agent C gross mass 0-5%, the quality of the polymerisable monomer B is accounted for can
The ratio of the gross mass of polymerized monomer B and D is not less than 10%, and the quality of the initiator accounts for polymerisable monomer A, B, D and crosslinking
The 0.05-3% of agent C gross masses;
The gross mass of contained element silicon accounts for the organic polymer particle obtained in step (1) in the Organic substance E and inorganic component F
The 2-20% of gross mass, contained element silicon amount accounts for total matter of element silicon in Organic substance E and inorganic component F in the inorganic component F
The 0-25% of amount, the quality of the organic polymer G accounts for the 2- of the organic polymer particle gross mass obtained in step (1)
50%.
3. preparation method according to claim 2, it is characterised in that the initiator is thermal decomposition initiator system initiator
Or the one kind in redox initiation system initiator, the thermal decomposition initiator system initiator is the isobutyl imidazoline salt of azo two
One kind in double (2- methyl-prop amidines) dihydrochloride, Ammonium persulfate., potassium peroxydisulfate or the sodium peroxydisulfates of hydrochlorate, 2,2'- azos, it is described
Oxidant in redox initiation system initiator is H2O2, reducing agent is vitamin C or rongalite.
4. preparation method according to claim 3, it is characterised in that the oxygen in the redox initiation system initiator
Agent is the one kind in Ammonium persulfate., sodium peroxydisulfate or potassium peroxydisulfate, and reducing agent is sodium sulfite, sodium sulfite, burnt sulfurous
One kind in sour sodium or rongalite.
5. the preparation method according to claim 3 or 4, it is characterised in that the consumption mole of the oxidant and reducing agent
Than for 0.5-2.0.
6. preparation method according to claim 2, it is characterised in that the monomer is the one kind in following monomer
Or more than one combination in any:3- aminostyryls, 4- aminostyryls, 2- (tert-butylamino) ethyl methacrylate,
The hydrochlorate or sulfonate of aminoethyl methacrylate and above-mentioned monomer, acrylic acid, methacrylic acid and acrylic acid or first
The acrylic acid univalent metal salt of base, acrylic acid -2- hydroxyl ethyl esters, 2-hydroxyethyl methacry-late, 2-hydroxypropyl acrylate, third
Olefin(e) acid -4- hydroxybutyls, methacrylic acid -2- hydroxy propyl esters, methacrylic acid -4- hydroxybutyls, N hydroxymethyl acrylamide,
N- hydroxyethyl acrylamides, N- (2- hydroxypropyls) acrylamide, N- methylol methacrylamides and N- (2- hydroxypropyls) methyl
Acrylamide.
7. preparation method according to claim 2, it is characterised in that the soluble inorganic salt is by soluble inorganic calcium salt
Or one or two compositions in soluble inorganic magnesium salt, the soluble inorganic calcium salt is in calcium nitrate, calcium chloride, calcium acetate
One or more arbitrary proportion mixture, the soluble inorganic magnesium salt be magnesium acetate, magnesium chloride, magnesium nitrate or magnesium sulfate in
One or more arbitrary proportion mixture.
8. preparation method according to claim 2, it is characterised in that the reaction temperature in the step (1) is 20-90
DEG C, the response time is 2-8h, and the reaction temperature in the step (2) is 40-90 DEG C, and the response time is 3-8h.
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5558708A (en) * | 1995-05-11 | 1996-09-24 | C-Cure Corporation | System and method for dispersing pigment in cement based compositions |
CN102020747A (en) * | 2009-09-09 | 2011-04-20 | 北京东联化工有限公司 | Acrylic core-shell polymer emulsion and preparation method thereof |
CN102199243A (en) * | 2011-04-07 | 2011-09-28 | 四川大学 | Polyacrylate elastomer with core-shell structure and its preparation method |
-
2014
- 2014-11-25 CN CN201410690674.9A patent/CN104609759B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5558708A (en) * | 1995-05-11 | 1996-09-24 | C-Cure Corporation | System and method for dispersing pigment in cement based compositions |
CN102020747A (en) * | 2009-09-09 | 2011-04-20 | 北京东联化工有限公司 | Acrylic core-shell polymer emulsion and preparation method thereof |
CN102199243A (en) * | 2011-04-07 | 2011-09-28 | 四川大学 | Polyacrylate elastomer with core-shell structure and its preparation method |
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