CN111423801B - Water-based nano heavy-duty coating for chemical sewage tank and preparation thereof - Google Patents
Water-based nano heavy-duty coating for chemical sewage tank and preparation thereof Download PDFInfo
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- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
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- C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
- C09D5/08—Anti-corrosive paints
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- C09D7/61—Additives non-macromolecular inorganic
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
- C09D7/40—Additives
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- C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
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Abstract
The invention relates to the technical field of chemical heavy-duty anticorrosion, in particular to a water-based nano heavy-duty anticorrosion coating for a chemical sewage pool and a preparation method thereof. The coating is formed by mixing components A, B and C according to the mass ratio of 1:1-3: 1-3; wherein, the component A contains modified resin mixture of modified polyisocyanate and modified polyester resin, mixed phosphate color paste, wetting agent, defoaming agent and anti-sagging agent, the component B is silicate aqueous solution, and the component C is modified montmorillonite slurry. The preparation process of the coating comprises the steps of uniformly mixing the component A and the component C according to the proportion, then mixing the component A and the component C, uniformly dispersing inorganic nanoparticles generated in situ in the coating after mixing while polymerizing to generate a cross-linked structure, so that the corrosion resistance of the coating is greatly improved, the coating can be used for treating concrete with poor base surface conditions, and can be used in the field of corrosion resistance of sewage pools such as chemical sewage pools of concrete base materials or metal base materials, and the like, and the defects of the concrete can be overcome to improve the strength and compactness of the base materials.
Description
Technical Field
The invention relates to the technical field of chemical heavy-duty anticorrosion, in particular to a water-based nano heavy-duty anticorrosion coating for a chemical sewage pool and a preparation method thereof.
Background
Chemical industry can produce the poisonous harmful waste liquid that contains strong corrosive medium such as strong acid, alkali, organic solvent in a large number in process of production, and the chemical industry effluent water sump is the concrete material mostly, and a small amount of effluent water sump is the steel construction material, and the effluent water sump of these materials is able to bear or endure the medium ability less strongly, thereby stores for a long time that corrosive medium can cause revealing of waste liquid and pollute groundwater and soil, causes irreversible environmental pollution. In recent years, along with the increasing national requirements on environmental protection and pollution discharge of chemical enterprises, the seepage prevention of the chemical sewage tank becomes an important index for evaluating whether the enterprises can pass the environmental protection acceptance. If a leak occurs, the enterprise will incur high economic losses such as downtime and handling of environmental pollution caused by the leak.
The coating for solving the corrosion prevention of the chemical sewage pool at present mainly adopts rubber coatings such as epoxy glass fiber reinforced plastic, vinyl resin, polysulfide rubber and the like and traditional polyurea coatings, and the scheme has the defects that (1) the coating is cracked in a thick coating, has single medium resistance and poor durability, is easy to cause corrosion, swelling and leakage or peel off the whole coating from a base material, and has poor adhesive force; (2) the elasticity is low, and the corresponding elastic deformation cannot be generated along with the contraction and expansion of the base material; (3) more toxic and harmful VOC components are generated during construction, and great harm is caused to the body of constructors and the environment; (4) for example, although the traditional polyurea anti-corrosive coating has the advantage of performance, the curing speed is too high, so that the performance of the coating is reduced and the requirement on the construction process is higher.
Therefore, the invention aims to prepare the modified montmorillonite slurry by adopting different types of montmorillonite, thereby reducing the cohesive force of the solidified coating to improve the dry film adhesive force and the wet adhesive force of the coating and improving the physical mechanical strength by the crosslinking of a catalytic system, and improving the compactness of the coating and the medium resistance of acid, alkali, solvent and the like.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a preparation method of an aqueous nano heavy-duty coating for a chemical wastewater treatment tank, which is used in the field of chemical wastewater treatment tank corrosion prevention.
In order to achieve the purpose, the invention adopts the technical scheme that:
a water-based nano heavy-duty anticorrosive coating for chemical sewage pools is formed by mixing components A, B and C according to the mass ratio of 1:1-3: 1-3; wherein, the component A contains modified resin mixture of modified polyisocyanate and modified polyester resin, mixed phosphate color paste, wetting agent, defoaming agent and anti-sagging agent, the component B is silicate aqueous solution, and the component C is modified montmorillonite slurry.
The component A (calculated by 100 portions): 10-80 parts of modified resin mixture, 1-15 parts of mixed phosphate color paste, 0.5-2 parts of wetting agent, 0.3-1 part of defoaming agent and 1-5 parts of anti-sagging agent; wherein the modified resin mixture is prepared by mixing modified polyisocyanate and modified polyester resin according to the mass ratio of 10: 1-2: 1; preferably 3: 1;
the component B (calculated by 100 portions): 40-60 parts of silicate and 40-60 parts of deionized water;
the component C (calculated by 100 parts) is as follows: 40-60 parts of modified montmorillonite, 5-30 parts of phosphate and 5-30 parts of modified polyisocyanate.
The polyisocyanates in the component A and the component C can be the same or different and are selected from one or more of liquefied MDI, TDI dimer, TDI trimer, TDI-TMP addition product, HDI dimer, HDI trimer, HDI biuret, IPDI trimer, TDI-HDI mixed polymer, HDI-IPDI mixed polymer, triphenylmethane triisocyanate, dimethyltriphenylmethane tetraisocyanate, thiophosphoric acid tri (4-phenyl isocyanate) and heptaisocyanate; among them, liquefied MDI and TDI dimer are preferable.
The mixed phosphate color paste in the component A is a mixture of a pigment and phosphate with the mass ratio of 1: 1-1: 5; then grinding the mixture to be below 0.1 mu m by a horizontal sand mill for standby.
The component A modified polyester resin is saturated polyester resin, unsaturated polyester resin, alkyd polyester resin, polycaprolactone resin and polycarbonate resin, and is preferably DigaLTW resin;
the wetting agent in the component A is modified benzyl silicone oil;
the defoaming agent in the component A is a polysiloxane mixture containing hydrophobic particles;
the anti-sagging agent in the component A is one of fumed silica, modified bentonite, hydrogenated castor oil and polyamide wax powder. Fumed silica or modified bentonite is preferred.
The phosphate in the component A and the component C can be the same or different and is selected from one or two of monophenyl phosphate, dibutyl phosphate, butyl diethyl phosphate, trimethyl phosphate, triethyl phosphate, tributyl phosphate, trioctyl phosphate, triphenyl phosphate, tricresyl phosphate, diphenyl phosphate and other primary phosphate, secondary phosphate and tertiary phosphate, trichloroethyl phosphate, tris (dibromopropyl) phosphate, methacryloyloxyethyl phosphate, 2-hydroxyethyl methacrylate phosphate, ethylene glycol methacrylate phosphate, 2-hydroxyethyl methacrylate phosphate, alkyl acrylate phosphate and other modified phosphate. The mass ratio of the two mixed materials is 1: 1-1: 10, triethyl phosphate and tricresyl phosphate, trimethyl phosphate and triphenyl phosphate, tributyl phosphate and diphenyl phosphate are preferred.
The component B is sodium silicate or potassium silicate powder with the modulus of 3-4. Preferably potassium silicate powder having a modulus of 3.
The component C is prepared by blending phosphate and modified montmorillonite, grinding, and adding modified polyisocyanate to modify hydroxyl on montmorillonite layer; wherein the lamella spacing of the modified montmorillonite is nano-scale and is about 1-3 nm.
Further, the component C is prepared by adding modified montmorillonite into phosphate ester under stirring, uniformly dispersing, grinding for 1h, adding modified polyisocyanate, fully stirring and uniformly mixing, and filtering for later use.
The modified montmorillonite is one or a mixture of inorganic modified montmorillonite, inorganic modified montmorillonite or organic-inorganic composite modified montmorillonite.
The inorganic modified montmorillonite is modified montmorillonite prepared from inorganic metal salt;
further, the inorganic modified montmorillonite includes modified montmorillonite prepared from inorganic acids such as sulfuric acid, hydrochloric acid, phosphoric acid and mixed acids thereof and inorganic metal salts such as aluminum salt, zinc salt, magnesium salt and copper salt, preferably AlCl3And ZnCl2。
The organic modified montmorillonite is modified montmorillonite prepared from long-chain alkyl quaternary ammonium salt, quaternary phosphonium salt and methyl-imidazolium salt;
further, the organically modified montmorillonite includes modified montmorillonite such as long-chain alkyl quaternary ammonium salts (e.g., dodecyl, tetradecyl, hexadecyl, and octadecyl trimethyl ammonium bromides), quaternary phosphonium salts (e.g., tetradecyl, hexadecyl trimethyl quaternary phosphonium, hexadecyl triphenyl phosphonium bromide, 3-aminopropyl triethoxy silane, and tetradecyl tributyl phosphonium chloride in mixture), methyl-imidazolium salts (e.g., 1-decyl-2-methylimidazolium salt, 1, 2-dimethylimidazolium salt, 11-bromoundecaprate imidazolium salt, 1-bromodecane imidazolium salt, and 11-bromo-1-undecenol imidazolium salt), and preferably hexadecyl and octadecyl trimethyl ammonium bromide modified montmorillonite.
The organic-inorganic composite modified montmorillonite is prepared from aluminum salt, zinc salt, magnesium salt or copper salt inorganic salt and quaternary ammonium salt, quaternary phosphonium salt or methyl-imidazole salt organic salt.
The organic-inorganic composite modification includes inorganic salts such as aluminum salt, zinc salt, magnesium salt, and copper salt, and organic salts such as quaternary ammonium salt, quaternary phosphonium salt, and methyl-imidazole salt, and preferably includes aluminum salt and quaternary ammonium salt.
A preparation method of an aqueous nanometer heavy-duty coating for a chemical sewage pool,
the preparation process of the component A comprises the following steps: according to the proportion, under the protection of dry air, the modified polyisocyanate and the polyester resin are mixed, then the mixed phosphate color paste, the auxiliary agent and the anti-sagging agent are added under the stirring condition, and the mixture is stirred uniformly for later use;
the preparation process of the component B comprises the following steps: adding deionized water into silicate under stirring, and dispersing uniformly to prepare a silicate solution with the mass fraction of 40-60%;
the preparation process of the component C comprises the following steps: blending phosphate and modified montmorillonite, grinding, and adding modified polyisocyanate to modify hydroxyl on montmorillonite layer; wherein the lamella spacing of the modified montmorillonite is nano-scale and is about 1-3 nm.
The components A, B and C are respectively obtained and weighed according to the mass ratio of 1:1-3:1-3, then the component C and the component A are uniformly mixed, and the component B is mixed when in use (mixing at present) to obtain the coating for construction.
Further, the component A is prepared by mixing the modified polyisocyanate and the polyester resin according to the proportion under the protection of dry air, adding the mixed phosphate color paste and the auxiliary agent under the stirring condition at the speed of 500r/min, then adding the anti-sagging agent under the stirring condition at the speed of 700r/min, and stirring uniformly for later use.
And the component C is prepared by adding modified montmorillonite into phosphate ester under stirring, dispersing uniformly, grinding for 1h, adding modified polyisocyanate, stirring and mixing uniformly, and filtering for later use.
Compared with the prior art, the invention has the following advantages:
the invention relates to a water-based nano heavy-duty anticorrosive coating, which belongs to a high-solid solvent-free environment-friendly coating, wherein components A, B and C are fully and uniformly mixed under the stirring condition to form a film through polymerization and crosslinking, the crosslinking structure of the coating is mainly polyurea structure, and other multi-functionality crosslinking structure groups are assisted to form a coating with high hardness, strong acid and alkali resistance, strong solvent resistance and strong corrosion resistance, and the coating has certain flexibility so that the coating can not be broken when being attached to a concrete base surface.
The preparation process of the component C of the invention is to enlarge the interlayer spacing of the nano-sheet layer of the montmorillonite by grinding and blending the phosphate and the modified montmorillonite, so that the modified polyisocyanate can enter the interlayer of the montmorillonite to pre-react with the hydroxyl of the montmorillonite, and the foaming and excessive heat release phenomena generated by mixing of A, B, C three components are avoided.
The component C in the coating is added with the modified montmorillonite slurry with a nano-sheet structure, so that the mechanical strength and the barrier property of the coating can be improved, and organic and inorganic functional groups such as metal ions, amino bonds and the like on the sheet layer can promote the crosslinking of a system, increase the crosslinking density, further improve the reaction degree of the system and reduce the residual active groups in the system, thereby improving the mechanical strength, the corrosion resistance and the aging resistance of the coating and simultaneously ensuring that the flame retardant property of the system is better; and the modified montmorillonite is added into the component C, so that the problem of overlarge cohesive force of the high-solid-content coating is solved, and the dry film adhesive force, the wet adhesive force and the medium corrosion resistance of the coating are obviously improved.
The preparation process of the coating comprises the steps of uniformly mixing the component A and the component C according to the proportion, then mixing the component A and the component C, uniformly dispersing inorganic nanoparticles generated in situ in the coating after mixing while polymerizing to generate a cross-linked structure, so that the corrosion resistance of the coating is greatly improved, the coating can be used for treating concrete with poor base surface conditions, and can be used in the field of corrosion resistance of sewage pools such as chemical sewage pools of concrete base materials or metal base materials, and the like, and the defects of the concrete can be overcome to improve the strength and compactness of the base materials.
The coating has construction diversity, and can adopt the construction modes of brush coating, roller coating, high-pressure airless spraying and two-component spraying.
Detailed Description
The technical solutions, the technical problems to be solved, the technical solutions and the advantages of the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it should be understood that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the coating, the components A and C are solvent-free oily components, the component B is an aqueous solution, and different types of montmorillonite are adopted to prepare modified montmorillonite slurry, so that the cohesion of the coating after curing is reduced to improve the dry film adhesive force and wet adhesive force of the coating, and the physical mechanical strength is improved by the crosslinking of a catalytic system, and the compactness of the coating, acid and alkali resistance, solvent resistance and other medium resistance properties are improved.
Example 1
The components are mixed according to the proportion recorded in the table 1 according to the parts by weight
The preparation process of the mixed phosphate color paste comprises the following steps: adding 4 parts of color powder into mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate under the stirring state of 200r/min, and grinding the mixture to be less than 0.5 mu m by a horizontal sand mill to obtain the mixed phosphate color paste.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of sulfuric acid modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, uniformly mixing after stirring for 30min, and filtering to obtain the component C.
Preparing a coating: taking the components according to the mass ratio of the component A to the component B to the component C of 1:2:1, wherein the component A is a resin main body, the component B is a curing agent, and the component C is modified montmorillonite slurry; then, firstly, uniformly stirring and mixing the component A and the component C in a mass ratio of 1:1, and then uniformly mixing the component A and the component C with the component B (mixing at present) to obtain a coating; and uniformly mixing, spraying, blade coating and roller coating to coat the coating on the surface of the corresponding matrix.
TABLE 1A component mixing ratio
TABLE 2 mixing ratio of the components B
TABLE 3C component mixing ratio
Wherein, the wetting agent is modified benzyl silicone oil, the defoaming agent is a moderate 6800, the anti-sagging agent is fumed silica and mixed phosphate (the mass ratio of triethyl phosphate to tricresyl phosphate is 4:7), and the modified montmorillonite is a commercial product.
Meanwhile, the A, B, C component proportion is mixed according to the proportion range given in the previous description, and the auxiliary agent in the A component can be replaced according to the existing record, so that the coating with corresponding effect characteristics can be obtained.
Example 2
The difference from the embodiment 1 is that:
the preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of hydrochloric acid modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, uniformly mixing after stirring for 30min, and filtering to obtain the component C.
Wherein, the wetting agent is modified benzyl silicone oil, the defoaming agent is a moderate 6800, and the anti-sagging agent is fumed silica and mixed phosphate (the mass ratio of triethyl phosphate to tricresyl phosphate is 4: 7).
Meanwhile, the A, B, C component proportion is mixed according to the proportion range given in the previous description, and the auxiliary agent in the A component can be replaced according to the existing record, so that the coating with corresponding effect characteristics can be obtained.
Example 3
The difference from the embodiment 1 is that:
the preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4:7, 40 parts in total, and adding 40 parts of AlCl under the stirring condition of 500r/min3Modified montmorillonite is dispersed for 30min, ground for 1h by a horizontal sand mill, and then added with 20 parts of 500 parts of liquefied MDIr/min stirring for 30min, mixing, and filtering to obtain component C.
Example 4
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4:7, 40 parts in total, and adding 40 parts of ZnCl under the stirring condition of 500r/min2Modified montmorillonite is dispersed for 30min, ground for 1h by a horizontal sand mill, then added with 20 parts of liquefied MDI (diphenyl-methane-diisocyanate) at a speed of 500r/min, stirred for 30min, uniformly mixed and filtered to obtain the component C.
Example 5
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of dodecyl trimethyl ammonium bromide modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 6
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of tetradecyl trimethyl ammonium bromide modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 7
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of hexadecyl trimethyl ammonium bromide modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 8
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of octadecyl trimethyl ammonium bromide modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenyl-methane-diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 9
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of tetradecyl trimethyl quaternary phosphine modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 10
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of hexadecyl trimethyl quaternary phosphine modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C. Example 11
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder is added into mixed phosphate of 3 parts of trimethyl phosphate and 8 parts of triphenyl phosphate under the stirring state, and the mixture is ground to be below 0.5 mu m by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: uniformly mixing 40 parts of trimethyl phosphate and triphenyl phosphate according to the mass ratio of 3:8, adding 40 parts of hexadecyl triphenylphosphine modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 12
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder is added into mixed phosphate of 3 parts of trimethyl phosphate and 8 parts of triphenyl phosphate under the stirring state, and the mixture is ground to be below 0.5 mu m by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: uniformly mixing 40 parts of trimethyl phosphate and triphenyl phosphate according to the mass ratio of 3:8, adding 40 parts of 3-aminopropyltriethoxysilane and tetradecyl tributyl phosphine chloride mixed modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 13
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of tributyl phosphate and 7 parts of diphenyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: tributyl phosphate and diphenyl phosphate are mixed according to the mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of 1-decyl-2-methylimidazolium salt modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, uniformly mixing after stirring for 30min, and filtering to obtain the component C.
Example 14
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 5 parts of tributyl phosphate and 6 parts of diphenyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: tributyl phosphate and diphenyl phosphate are mixed according to the mass ratio of 5: 6, uniformly mixing 40 parts in total, adding 40 parts of 1, 2-dimethyl imidazolium salt modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 15
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder is added into mixed phosphate of 4 parts of trimethyl phosphate and 7 parts of triphenyl phosphate under the stirring state, and the mixture is ground to be below 0.5 mu m by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: trimethyl phosphate and triphenyl phosphate are mixed according to a mass ratio of 4: and 7, uniformly mixing 40 parts in total, adding 40 parts of 11-bromoundecanoic acid imidazole salt modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 16
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 5.5 parts of tributyl phosphate and 5.5 parts of diphenyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: tributyl phosphate and diphenyl phosphate are mixed according to the mass ratio of 1:1, uniformly mixing 40 parts in total, adding 40 parts of 1-bromodecane imidazolium salt modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenylmethane diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 17
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder is added into 11 parts of triethyl phosphate under stirring, and the mixture is ground to be less than 0.5 mu m by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: adding 40 parts of triethyl phosphate into 40 parts of 11-bromo-1-undecylenic imidazole salt modified montmorillonite under the stirring condition of 500r/min, dispersing for 30min, grinding for 1h by using a horizontal sand mill, adding 20 parts of liquefied MDI (diphenyl-methane-diisocyanate) at 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 18
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4:7, 40 parts in total, and adding 40 parts of ZnCl under the stirring condition of 500r/min2Dispersing the montmorillonite modified by cetyl trimethyl ammonium bromide for 30min, and horizontally sandingGrinding for 1h, adding 20 parts of liquefied MDI (diphenyl methane diisocyanate) at a speed of 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 19
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4:7, 40 parts in total, and adding 40 parts of AlCl under the stirring condition of 500r/min3And octadecyl trimethyl ammonium bromide modified montmorillonite, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenyl methane diisocyanate) at a speed of 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Example 20
The difference from the embodiment 1 is that
The preparation process of the mixed phosphate color paste comprises the following steps: 4 parts of color powder was added to a mixed phosphate of 4 parts of triethyl phosphate and 7 parts of tricresyl phosphate with stirring, and ground to 0.5 μm or less by a horizontal sand mill.
The preparation process of the component A comprises the following steps: under the protection of dry air, 60 parts of liquefied MDI and 20 parts of LTW resin are uniformly mixed at 500r/min to prepare mixed resin, 15 parts of mixed phosphate color paste, 2 parts of wetting agent and 2 parts of defoaming agent are added under the stirring of 500r/min under the protection of dry air, 2 parts of anti-sagging agent is added under the stirring of 700r/min, the mixture is uniformly stirred, and the component A is obtained after the filtration.
The preparation process of the component B comprises the following steps: 60 parts of deionized water is added with 40 parts of potassium silicate powder with the modulus of 3 under the stirring state, dispersed for 1 hour at the temperature of 30 ℃ at the speed of 700r/min, and filtered to obtain the component B.
The preparation process of the component C comprises the following steps: triethyl phosphate and tricresyl phosphate are mixed according to the mass ratio of 4:7, 40 parts in total, and adding 40 parts of AlCl under the stirring condition of 500r/min3And hexadecyl trimethyl ammonium bromide modified montmorillonite, dispersing for 30min, grinding for 1h by a horizontal sand mill, adding 20 parts of liquefied MDI (diphenyl-methane-diisocyanate) at a speed of 500r/min, stirring for 30min, uniformly mixing, and filtering to obtain the component C.
Comparative example 1
The coating was applied to a system in which the A, B components of example 1 were mixed in a ratio of 1: 2.
Comparative example 2
The A, B component in the example 1 is not changed, the modified montmorillonite in the C component is replaced by a talcum powder system, and then the three components are mixed according to the proportion of 1:2:1 to be used as a coating.
The coatings obtained in the examples described above were tested, as well as comparative coatings, (see tables 4-6), where the adhesion of the materials was tested according to standard GB/T5210-; testing the solvent resistance and acid and alkali resistance of the material by using a standard GB/T9274-1988; testing the bending property of the material by using a standard GB/T93412008; testing the tensile property test of the material by the standard GB/T1040-2006; the abrasion resistance of the material is tested by the standard GB/T1768-.
Table 4 physical mechanical property test data of each example
TABLE 5 Corrosion resistance test data for the examples
Note: the mixed acid solution was 5% hydrochloric acid: 10% sulfuric acid 1:1 (mass ratio)
The mixed alkali solution is 10% sodium hydroxide: 10% Potassium hydroxide 1:1 (mass ratio)
The saline solution is 10% sodium chloride
The mixed solvent is kerosene: xylene: ethanol 1:1:1 (mass ratio)
Table 6 compares to conventional preservative regimens
As can be seen from Table 4, the physical mechanical properties and corrosion resistance data of the coatings obtained in the examples are superior to those of comparative examples 1 and 2. As shown in Table 4, the solids content of the examples is greater than 92%, which indicates that the invention belongs to the environment-friendly coating with high solid content; the adhesive force of the steel base material of the embodiment is 9-15 MPa, and is greater than 5MPa and 6MPa of comparison 1 and comparison 2; the adhesive force of the concrete base material in the embodiment is 13-21 MPa, which is greater than 8MPa and 9MPa of the concrete base material in comparison 1 and comparison 2; the bending strength of the embodiment is 43-55 MPa, which is more than 23MPa and 25MPa of comparison 1 and comparison 2; the tensile strength of the example is 9-21 MPa, which is greater than 5MPa and 6MPa of comparison 1 and comparison 2; the wear resistance of the embodiment is 9-22 MPa, which is less than 35MPa and 27MPa of comparison 1 and comparison 2; the examples are superior in flexibility to comparative 1 and comparative 2.
As can be seen from Table 5, the mixed acid, mixed alkali, brine, mixed solvent, and thermal shock cycle resistance and high temperature and high pressure resistance of the coatings obtained in the examples are better than those of comparative examples 1 and 2. The examples 1 and 2 are slightly foamed after resisting the medium 120d, the paint film is intact after resisting the inorganic medium 120d in the examples 3-20, and more foams are generated after resisting the inorganic medium 120d in the comparison examples 1 and 2; the paint film is good after the hot and cold shock resistant cycle of the examples 1 and 2 is carried out for 30 times and the high temperature and high pressure resistant cycle of the examples 7d, the paint film is good after the hot and cold shock resistant cycle of the examples 3-20 and the high temperature and high pressure resistant cycle of the examples 7d, and more foams after the hot and cold shock resistant cycle of the examples 1 and 2 is carried out for 30 times and the high temperature and high pressure resistant cycle of the examples 7 d.
As can be seen from tables 4 and 5, the physical mechanical properties and the medium resistance of examples 7, 8, 19 and 20 are better, particularly the performances of examples 8 and 19 are optimal, so that the catalytic effect of the quaternary ammonium salt modified montmorillonite on the system is most obvious, particularly the long-carbon-chain quaternary ammonium salt modified montmorillonite catalytic system generates higher crosslinking density, and the physical mechanical strength and the medium resistance of the system are remarkably improved. As can be seen from comparative examples 8 and 19, the addition of the metal salt is beneficial to the crosslinking of the catalytic system, so that the system generates higher crosslinking density, and the physical mechanical strength and the medium resistance of the system are obviously improved. The comparison of the adhesion of the embodiment and the comparative sample shows that the addition of the modified montmorillonite greatly reduces the cohesion of the system, so that the adhesion of the coating on the steel substrate and the concrete substrate is greatly improved, and the adhesion is improved to 15MPa from 5-6 MPa.
As shown in Table 6, the aqueous nano heavy-duty anticorrosive coating is environment-friendly and pollution-free in the construction process and the paint film drying process, the thickness of the construction coating is low, the construction method is convenient and fast, the selectivity is high, the construction scheme can be changed according to actual conditions, and the construction performance of the coating is superior to that of polyurea elastomers and epoxy glass fiber reinforced plastics.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (7)
1. The utility model provides an aqueous nanometer heavy anti-corrosion coating for chemical industry effluent water sump which characterized in that: the coating is formed by mixing the components A, B and C according to the mass ratio of 1:1-3: 1-3; wherein, the component A contains a modified resin mixture of modified polyisocyanate and modified polyester resin, mixed phosphate color paste, a wetting agent, a defoaming agent and an anti-sagging agent, the component B is a silicate aqueous solution, and the component C is modified montmorillonite slurry;
the component A (calculated by 100 portions): 10-80 parts of modified resin mixture, 1-15 parts of mixed phosphate color paste, 0.5-2 parts of wetting agent, 0.3-1 part of defoaming agent and 1-5 parts of anti-sagging agent; wherein the modified resin mixture is prepared by mixing modified polyisocyanate and modified polyester resin according to the mass ratio of 10: 1-2: 1;
the component B (calculated by 100 portions): 40-60 parts of silicate and 40-60 parts of deionized water;
the component C (calculated by 100 parts) is as follows: 40-60 parts of modified montmorillonite, 5-40 parts of phosphate and 5-30 parts of modified polyisocyanate;
the specific preparation processes of the component A, the component B and the component C are as follows:
the preparation process of the component A comprises the following steps: according to the proportion, under the protection of dry air, firstly, the modified polyisocyanate and the modified polyester resin are mixed, then, the mixed phosphate color paste, the wetting agent, the defoaming agent and the anti-sagging agent are added under the stirring condition, and the mixture is uniformly stirred for later use;
the preparation process of the component B comprises the following steps: adding deionized water into silicate under stirring, and dispersing uniformly to prepare a silicate solution with the mass fraction of 40-60%;
the preparation process of the component C comprises the following steps: blending phosphate and modified montmorillonite, grinding, and adding modified polyisocyanate to modify hydroxyl on montmorillonite layer; wherein the lamella spacing of the modified montmorillonite is nano-scale and is 1-3 nm;
weighing the components A, B and C respectively according to the mass ratio of 1:1-3:1-3, uniformly mixing the component C and the component A, and mixing the component C and the component A into the component B to obtain the coating.
2. The aqueous nano heavy-duty coating for chemical wastewater treatment ponds according to claim 1, characterized in that: the polyisocyanate in the component A and the component C is one or more of liquefied MDI, TDI dimer, TDI trimer, TDI-TMP addition product, HDI dimer, HDI trimer, HDI biuret, IPDI trimer, TDI-HDI mixed polymer, HDI-IPDI mixed polymer, triphenylmethane triisocyanate, dimethyl triphenylmethane tetraisocyanate, thiophosphoric acid tri (4-phenyl isocyanate) and heptaisocyanate;
the phosphate ester color paste mixed in the component A is a mixture of a pigment and phosphate ester, wherein the pigment and the phosphate ester are mixed according to the mass ratio of 1: 1-1: 5.
3. The aqueous nano heavy-duty coating for chemical wastewater treatment ponds according to claim 1 or 2, characterized in that: the phosphate is one or two of primary phosphate, secondary phosphate and tertiary phosphate such as monophenyl phosphate, dibutyl phosphate, butyl diethyl phosphate, trimethyl phosphate, triethyl phosphate, tributyl phosphate, trioctyl phosphate, triphenyl phosphate, tricresyl phosphate, diphenyl phosphate and the like, trichloroethyl phosphate, tris (dibromopropyl) phosphate, methacryloyloxyethyl phosphate, 2-hydroxyethyl methacrylate phosphate, ethylene glycol methacrylate phosphate, 2-hydroxyethyl methacrylate phosphate and alkyl acrylate phosphate.
4. The aqueous nano heavy-duty coating for chemical wastewater treatment ponds according to claim 1, characterized in that: the silicate of the component B is sodium silicate or potassium silicate powder with a modulus of 3-4.
5. The aqueous nano heavy-duty coating for chemical wastewater treatment ponds according to claim 1, characterized in that: the modified montmorillonite is one or a mixture of inorganic modified montmorillonite, inorganic modified montmorillonite or organic-inorganic composite modified montmorillonite.
6. The aqueous nano heavy-duty coating for chemical wastewater treatment ponds according to claim 5, characterized in that: the inorganic modified montmorillonite is modified montmorillonite prepared from inorganic metal salt;
the organic modified montmorillonite is modified montmorillonite prepared from long-chain alkyl quaternary ammonium salt, quaternary phosphonium salt and methyl-imidazolium salt;
the organic-inorganic composite modified montmorillonite is prepared from aluminum salt, zinc salt, magnesium salt or copper salt inorganic salt and quaternary ammonium salt, quaternary phosphonium salt or methyl-imidazole salt organic salt.
7. The preparation method of the aqueous nanometer heavy-duty coating for the chemical wastewater treatment tank as claimed in claim 1, which is characterized in that: the component A is prepared by mixing modified polyisocyanate and modified polyester resin according to the proportion under the protection of dry air, adding the mixed phosphate color paste, wetting agent and defoaming agent under the stirring condition at the speed of 500r/min, adding the anti-sagging agent under the stirring condition at the speed of 700r/min, and stirring uniformly for later use.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201910022783.6A CN111423801B (en) | 2019-01-10 | 2019-01-10 | Water-based nano heavy-duty coating for chemical sewage tank and preparation thereof |
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