CN100463945C - Nacrous slurry and its prepn. technique - Google Patents

Nacrous slurry and its prepn. technique Download PDF

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CN100463945C
CN100463945C CNB200610024813XA CN200610024813A CN100463945C CN 100463945 C CN100463945 C CN 100463945C CN B200610024813X A CNB200610024813X A CN B200610024813XA CN 200610024813 A CN200610024813 A CN 200610024813A CN 100463945 C CN100463945 C CN 100463945C
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pearly
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pearlite slurry
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lustre
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CN1834169A (en
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刘艳新
陈国贵
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Linhai Huahong Coatings Co.,Ltd.
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Zhejiang Weixing Industrial Development Co Ltd
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Abstract

This invention provides a method for preparing pearl plaster, which comprises pearl crystal 20-65 wt.%, plasticizer 2-50 wt.% and organic solvent 3-60 wt.%. The pearl plaster is prepared by the steps of: phase-transformation treating, distilling and concocting. The pearl plaster in this invention has such advantages as high affinity to organic media, high brightness, simple manufacturing process and short manufacturing time, while has no coagulation or aggregation.

Description

A kind of pearlite slurry
Technical field
The present invention relates to a kind of pearlite slurry; Relate in particular to a kind of formulated pearlite slurry of multiple composition that adopts; Belong to field of fine chemical.
Background technology
Pearlite slurry or pearly coating are a kind of sheet coating of high refractive index, and good luster can present the metal-like of flicker, are widely used in the use that coating such as car, furniture, machine or resin button, handicraft surface are handled.The metal oxide of existing pearlite slurry by transparent or semitransparent high refractive index covers on the flat substrates and is prepared from, thereby makes from the reflection of incident light light at flat substrates tectum interface and launch the color of interference from the mutual interference effect between the reflection of incident light light of cover surface; As Chinese patent application number 96100476.2 novel macreous pigments that provide and be combined with coating, cosmetic material, printing ink and the plastics of this pigment, promptly on synthetic mica, scribble metal oxide; Though this pearly pigment shows pearl effect preferably; But because the nucleus of mica titanium is atypic crystal; Its light that shows is inhomogeneous dispersion, so its flash of light poor-performing; Scribble on the mica in addition that metal oxide has high polarity and other organic medium avidity is lower; The someone expected adopting the pearlite slurry of surface modification afterwards; As the pearly pigment of the Chinese patent application number 01804811.0 new surface modification that provides and the method for producing this material; its particular content is a kind of pearly pigment of surface modification; wherein hydrated metal oxide covers the surface of pearly pigment; polymer fine particles is chemically bonded on the pearly pigment of hydrated metal oxide coating; and not mutually do not assemble, polymer fine particles is adhered on the outermost surface of pearly pigment of described hydrated metal oxide coating.Though having changed the prior art metal oxide, this patent application covers flat substrates and the lower problem of organic medium avidity; But, then make the flash of light performance of pearly pigment reduce greatly owing on the outermost surface of pearly pigment, coat thin of polymkeric substance; Adopt this method production technique complicated especially in addition, production cost is higher, and practicality is relatively poor.
Summary of the invention
The present invention is directed to prior art adopts metal oxide to cover the pearlite slurry that is prepared from the flat substrates to exist high polarity and the lower shortcoming of other organic medium avidity that a kind of pearlite slurry and compound method thereof that organic medium is had avidity is provided.
The present invention is also at the pearlite slurry of prior art for preparing flash of light poor-performing, and complex manufacturing, the higher shortcoming of production cost provide a kind of have high flash degree, production process is simple, production cost is lower pearlite slurry.
Above-mentioned purpose of the present invention solves by the following technical programs: a kind of pearlite slurry is characterized in that comprising that the composition of following weight per-cent is formulated:
Pearly-lustre crystal: 20%~65%; Softening agent 2%~50%
Organic solvent: 3%~60%;
Wherein said softening agent is a dioctyl phthalate (DOP), dibutyl phthalate, diisobutyl phthalate, dioctyl terephthalate, adipic acid dioctyl ester, dioctyl sebacate, one or more mixing in the dimethyl phthalate; Described organic solvent is one or more mixing in ester solvent, alcohol ether solvents, the ketone solvent.
Because pearly-lustre crystalline size, shape and surface smoothness have determined the optical property quality of product; Pearly-lustre crystal of the present invention is by studying for a long period of time and by come the white lead carbonate xln of synthetic regular hexagon, high flash degree after the repetition test process through dynamic reaction process, in whole pearly-lustre crystal reaction process, reactant all is continuous adding, the pH value of reaction is by predefined curve controlled, adopt size that dynamic response can strict control hexagon xln and thickness, size, make the synthetic crystallographic dimension even, controllable thickness, and can make the xln of interference color such as Huang, green, red, orchid; Wherein the concrete synthesis technique inventor of pearly-lustre crystalline applies for a patent separately; To repeat no more in the present invention.
The present invention adopts softening agent not only to help the distillation of pearlite slurry crystal but also helps pearlite slurry in use, and other product surface smooth finish and toughness of adding pearlite slurry is had improved action; Adopt organic solvent to help the dispersion and the blast of pearly-lustre product in the present invention.
In above-mentioned a kind of pearlite slurry, the preferred percent by weight of described composition is:
Pearly-lustre crystal: 25%~60%; Softening agent: 10%~40%
Organic solvent: 5%~50%.
In above-mentioned a kind of pearlite slurry, as preferably, described ester solvent is mixed by in N-BUTYL ACETATE, vinyl acetic monomer, the amyl acetate-n one or more.
In above-mentioned a kind of pearlite slurry, as preferably, described alcohol ether solvents is an ethylene glycol ethyl ether.Ethylene glycol ethyl ether can improve pearly-lustre crystalline dispersiveness and finished product brightness in use.
In above-mentioned a kind of pearlite slurry, as preferably, described ketone solvent is one or more mixing in hexone, pimelinketone, acetone, the methylethylketone.The used ketone of the present invention can improve pearly-lustre crystalline dispersiveness.
In above-mentioned a kind of pearlite slurry, can also comprise in the composition of following weight per-cent one or more in the described composition; Flow agent 0~50%; Defoamer 0~4%; Naphthane: 0~8%; Wherein said flow agent is a kind of in Synolac, acrylic resin, the nitro-resin; Described defoamer is a silicone oil; Described naphthane (TSP) can be promoted the levelling property and the generation that prevents bubble, pin hole of product.
As preferably, described silicone oil is methyl-silicone oil.The methyl-silicone oil surface tension is little, and water insoluble, and in vegetable and animals oils and the high boiling point mineral oil, chemical stability is good, nontoxic again, just has good defoamer effect as long as add the methyl-silicone oil of 10-100PPM.
The present invention also provides the compound method of above-mentioned pearlite slurry in addition, it is characterized in that may further comprise the steps:
A, phase inversion are handled: the aqueous suspension of the pearly-lustre crystal being put into the pure water formation xln of specific conductivity≤0.5 μ s/cm, while stirring emulsifying agent is mixed with the aqueous suspension of xln, carry out sedimentation after the mixing, after the sedimentation 1~3 hour, extraction solvent is sprayed on the blended liquid level, carries out phase inversion and handle;
B, distillation: softening agent is joined in xln-extraction solvent after phase inversion is handled, stir and vacuum condition under add thermal distillation, wherein vacuum tightness be-0.01MPa~-0.092MPa, distillation time is 2~5 hours;
C, allotment: allocate through the adding of the pearly-lustre crystal after distillation organic solvent above-mentioned, promptly obtain finished product after the allotment; Wherein the weight ratio of pearly-lustre crystal, softening agent and organic solvent is 20~60:2~50:3~60; Described softening agent is a dioctyl phthalate (DOP), dibutyl phthalate, diisobutyl phthalate, dioctyl terephthalate, adipic acid dioctyl ester, dioctyl sebacate, one or more mixing in the dimethyl phthalate; Described organic solvent is one or more mixing in ester solvent, alcohol ether solvents, the ketone solvent.
In a kind of pearlite slurry of the present invention, adopt emulsifying agent and extraction solvent to carry out separating and dehydrating, the pearly-lustre crystal is changed over to oil phase from aqueous phase, prevent pearly-lustre crystalline secondary bonding, kept the good flash of light performance of pearlite slurry, if the inventor finds that by studying for a long period of time moisture content is too high, will cause the cohesion of pearly-lustre crystalline, bonding phenomenon, influence the glossiness of pearlite slurry, moisture crosses low pearly-lustre crystal and other organic medium avidity is just lower; And under stirring and vacuum condition, add thermal distillation among the present invention, and with vacuum degree control-0.01MPa~-0.092MPa, distillation time was controlled at 2~5 hours, the water content of distillment has been controlled in strictness, both prevent the generation of cohesion, bonding phenomenon, kept pearly-lustre crystal and other organic medium higher avidity again.
In above-mentioned a kind of pearlite slurry, the emulsifying agent described in the step a is an oleic acid sodium sulfonate compound; As preferably, described oleic acid sodium sulfonate compound is one or more mixing in Sodium dodecylbenzene sulfonate, disodium 4-dodecyl-2,4 '-oxydibenzenesulfonate, the Viscotrol C sodium sulfate.In the phase inversion treating processes, the easy and pearly-lustre crystal combination of mentioned emulsifier that the present invention is used forms aqueous suspension.
In above-mentioned a kind of pearlite slurry, the extraction solvent described in the step a is a kind of in methylene dichloride, trichloromethane, tributyl phosphate, dibutyl butylphosphonate, di(2-ethylhexyl)phosphate (the 2-ethyl) ester.The used extraction solvent of the present invention is in crystal and emulsifying agent sepn process, and demulsification is better.
In above-mentioned a kind of pearlite slurry, as preferably; Vacuum degree control described in the step b-0.05MPa~-0.092MPa, distillation time was controlled at 3~4 hours.
Therefore the present invention has the following advantages:
1, it is formulated that pearlite slurry of the present invention adopts multiple composition; Both kept and organic medium between higher avidity, can not produce cohesion, adhesion phenomenon between the pearly-lustre crystal again, glossiness is higher, the flash of light better performances;
2, the present invention adopts the compound method that phase inversion is handled, and prevents pearly-lustre crystalline secondary bonding, has kept the good flash of light performance of pearlite slurry;
3, production technique of the present invention is simpler, and the production time is shorter; Both improve output, greatly reduced production cost again.
Embodiment
Below by specific embodiment, technical scheme of the present invention is described in further detail; But the present invention is not limited to these embodiment.
One: the pearly-lustre crystalline is synthetic
The acetic acid that adds purity 〉=99.9% by processing requirement, add behind the acetic acid after 5~20 minutes, stir acetic acid and add the plumbous oxide of purity 〉=99.99%, after adding finishes, continue to stir 15~40 minutes, add activated carbon and add the pure water of specific conductivity≤0.5 μ s/cm, continue to stir 5~20 minutes, leave standstill; After treating feed clarification, filter and make intermediate, basin is stand-by; Wherein reactant accounts for the weight percent of entire reaction liquid and is: acetic acid: 0.1%~3%, and lead ion: 1%~10%;
The yellow soda ash of purity 〉=99.8% is joined in the pure water of specific conductivity≤0.5 μ s/cm and generate crystal seed, wherein to account for the weight percent of entire reaction liquid be 0.018%~0.04% to yellow soda ash;
The pure water that adds specific conductivity≤0.5 μ s/cm in reactor after 0.5~3 minute, adds the mixed solution of above-mentioned intermediate and AG acetic acid while stirring, after 0.5~3 minute, adds crystal seed; Through synthetic pearly-lustre crystal after the dynamic response, in dynamic reaction process, add pure water or the SODIUMNITRATE of Soda Ash Light 99.2min., above-mentioned intermediate, specific conductivity≤0.5 μ s/cm; Wherein the time of dynamic response is 3~10 hours; The pH value 6.50~7.50 of reaction process solution, temperature of reaction are 0~50 ℃; Wherein the concrete synthesis technique inventor of pearly-lustre crystalline applies for a patent separately; To repeat no more in the present invention.
Two: pearlite slurry and compound method thereof
Weight percent proportioning by following table 1 takes by weighing the pearlite slurry composition
The weight percent of table 1: embodiment 1~5 each composition
Figure C200610024813D00101
Wherein used softening agent is a dioctyl phthalate (DOP) in embodiment 1, dibutyl phthalate, diisobutyl phthalate; Its weight ratio is 1:5:1:3; Used organic solvent is the mixed solvent of ester solvent and ketone solvent; Its weight ratio is 8:2; What wherein ester solvent was used is N-BUTYL ACETATE; What ketone solvent was used is pimelinketone.
Wherein used softening agent is a dibutyl phthalate in embodiment 2, diisobutyl phthalate, and dioctyl terephthalate, its weight ratio is 8:1:1; Used organic solvent is ester solvent and alcohol ether solvents, and its weight ratio is 6:4; What wherein ester solvent was used is N-BUTYL ACETATE, vinyl acetic monomer, and its weight ratio is 5:5; What wherein alcohol ether solvents was used is ethylene glycol ethyl ether; Used flow agent is a Synolac; Used defoamer is a methyl-silicone oil.
Wherein used softening agent is the adipic acid dioctyl ester in embodiment 3, dioctyl sebacate, and dimethyl phthalate, its weight ratio is 3:3:4; Used organic solvent is a ketone solvent; What wherein ketone solvent was used is hexone; Used flow agent is a nitro-resin; Used defoamer is a methyl-silicone oil.
Wherein used softening agent is a dibutyl phthalate in embodiment 4, and used organic solvent is an ester solvent, alcohol ether solvents, and ketone solvent, its weight ratio is 2:5:3; Wherein ester solvent is a N-BUTYL ACETATE, and alcohol ether solvents is an ethylene glycol ethyl ether, and wherein ketone solvent is hexone, acetone, methylethylketone, and its weight ratio is 7:2:1; Used flow agent is an acrylic resin, and used defoamer is a methyl-silicone oil; TSP is the naphthane solvent.
Wherein used softening agent is a dibutyl phthalate in embodiment 5, the adipic acid dioctyl ester, and its weight ratio is 9:1; Used organic solvent is an ester solvent, and alcohol ether solvents, its weight ratio are 5:5; Wherein ester solvent is a N-BUTYL ACETATE, and alcohol ether solvents is an ethylene glycol ethyl ether, and used flow agent is a Synolac, and used defoamer is a methyl-silicone oil.
The compound method of embodiment 1
A, phase inversion are handled: the aqueous suspension of the pearly-lustre crystal being put into the pure water formation xln of specific conductivity≤0.5 μ s/cm, is that Sodium dodecylbenzene sulfonate, disodium 4-dodecyl-2,4 '-oxydibenzenesulfonate, the Viscotrol C sodium sulfate emulsifying agent of 1:1:1 mixes with pearly-lustre crystalline aqueous suspension and put into the sedimentation of sedimentation still with churned mechanically mode with ratio, stops to stir after pearly-lustre crystalline aqueous suspension has been put; After the sedimentation 1 hour, adopt spray machinery that methylene dichloride is sprayed on the blended liquid level, carry out phase inversion and handle;
B, distillation: the xln-extraction solvent mixed solution after the phase inversion processing is put into still kettle, add as the softening agent in the table 1, add thermal still under stirring and vacuum condition, drive vacuum pump, regulating vacuum tightness is-0.01MPa that distillation time is 5 hours;
C, allotment: allocated as other composition in the table 1 above-mentioned the adding through the pearly-lustre crystal after the distillation, promptly obtain finished product after the allotment;
Extraction solvent in the compound method of embodiment 2~5 is a tributyl phosphate, and other technological process is with embodiment 1, and the present invention will repeat no more.
Weight percent proportioning by following table 2 takes by weighing the pearlite slurry composition
The weight percent of table 2: embodiment 6~10 each composition
Figure C200610024813D00121
Wherein used softening agent is a diisobutyl phthalate in embodiment 6, and used organic solvent is a ketone solvent, and wherein ketone solvent is acetone, methylethylketone, and TSP is the naphthane solvent.
Wherein used softening agent is the adipic acid dioctyl ester in embodiment 7, dioctyl sebacate, and its weight ratio is 5:5; Used organic solvent is that ester solvent, alcohol ether solvents, ketone solvent, its weight ratio are 2:5:3; Wherein ester solvent is used be vinyl acetic monomer, alcohol ether solvents used for ethylene glycol ethyl ether, ketone solvent used be hexone; Used flow agent is a Synolac; Used defoamer is a methyl-silicone oil.
Wherein used softening agent is a dibutyl phthalate in embodiment 8, and used organic solvent is ester solvent, alcohol ether solvents, and its weight ratio is 5:5; Wherein ester solvent used for N-BUTYL ACETATE, alcohol ether solvents used for ethylene glycol ethyl ether, used flow agent be acrylic resin.
Wherein used softening agent is the adipic acid dioctyl ester in embodiment 9; Used organic solvent is a ketone solvent; What wherein ketone solvent was used is methylethylketone; Used flow agent is a nitro-resin.
Wherein used softening agent is a dibutyl phthalate in embodiment 10, and used organic solvent is that ester solvent, alcohol ether solvents, ketone solvent, its weight ratio are 3:4:3; Wherein ester solvent used for amyl acetate-n, alcohol ether solvents used for ethylene glycol ethyl ether, ketone solvent used for hexone, its weight ratio of methylethylketone are 7:3, used flow agent is a Synolac.
The compound method of embodiment 6
A, phase inversion are handled: the aqueous suspension of the pearly-lustre crystal being put into the pure water formation xln of specific conductivity≤0.5 μ s/cm, with churned mechanically mode emulsifying agent Viscotrol C sodium sulfate is mixed with pearly-lustre crystalline aqueous suspension and to put into the sedimentation of sedimentation still, after pearly-lustre crystalline aqueous suspension has been put, stop to stir; After the sedimentation 2 hours, adopt spray machinery that trichloromethane is sprayed on the blended liquid level, carry out phase inversion and handle;
B, distillation: the xln-extraction solvent mixed solution after the phase inversion processing is put into still kettle, add as the softening agent in the table 2, add thermal still under stirring and vacuum condition, drive vacuum pump, regulating vacuum tightness is-0.05MPa that distillation time is 3.5 hours;
C, allotment: allocated as other composition in the table 2 above-mentioned the adding through the pearly-lustre crystal after the distillation, promptly obtain finished product after the allotment;
The extraction solvent of the compound method of embodiment 7~10 is di(2-ethylhexyl)phosphate (the 2-ethyl) ester, and other technological process is with embodiment 6, and the present invention will repeat no more.
Weight percent proportioning by following table 3 takes by weighing the pearlite slurry composition
The weight percent of table 3: embodiment 11~15 each composition
Figure C200610024813D00131
Figure C200610024813D00141
Wherein used softening agent is a dibutyl phthalate in embodiment 11, and used organic solvent is a ketone solvent, and what ketone solvent was used is hexone.
Wherein used softening agent is a dioctyl terephthalate in embodiment 12, and used organic solvent is an ester solvent, alcohol ether solvents, and ketone solvent, its weight ratio is 4:4:2; Wherein ester solvent is a N-BUTYL ACETATE, and alcohol ether solvents is an ethylene glycol ethyl ether, and wherein ketone solvent is a hexone, and used flow agent is a Synolac, and used defoamer is a methyl-silicone oil.
Wherein used softening agent is a dibutyl phthalate in embodiment 13, the adipic acid dioctyl ester, and its weight ratio is 6:4; Used organic solvent is an alcohol ether solvents; What wherein alcohol ether solvents was used is ethylene glycol ethyl ether.
Wherein used softening agent is a dibutyl phthalate in embodiment 14, and used organic solvent is an ester solvent, alcohol ether solvents, and the mixed solvent of ketone solvent, its weight ratio is 5:3:2; Wherein ester solvent is a vinyl acetic monomer, amyl acetate-n, and its weight ratio is an ethylene glycol ethyl ether for the 9:1 alcohol ether solvents, wherein ketone solvent is a hexone, the mixture of pimelinketone, acetone, methylethylketone, its weight ratio is 3:2:3:2; Used flow agent is a nitro-resin, and used defoamer is a methyl-silicone oil.
Wherein used softening agent is a dioctyl phthalate (DOP) in embodiment 15, dibutyl phthalate, diisobutyl phthalate, dioctyl terephthalate, adipic acid dioctyl ester, dioctyl sebacate, dimethyl phthalate; Its weight ratio is 1:4:1:1:1:1:1; Used organic solvent is the mixed solvent of ester solvent and alcohol ether solvents; Its weight ratio is 6:4; What wherein ester solvent was used is N-BUTYL ACETATE; What alcohol ether solvents was used is ethylene glycol ethyl ether; Used flow agent is a Synolac, and used defoamer is a methyl-silicone oil.
The compound method of embodiment 11
A, phase inversion are handled: the aqueous suspension of the pearly-lustre crystal being put into the pure water formation xln of specific conductivity≤0.5 μ s/cm, with churned mechanically mode emulsifying agent Viscotrol C sodium sulfate is mixed with pearly-lustre crystalline aqueous suspension and to put into the sedimentation of sedimentation still, after pearly-lustre crystalline aqueous suspension has been put, stop to stir; After the sedimentation 3 hours, adopt spray machinery that dibutyl butylphosphonate is sprayed on the blended liquid level, carry out phase inversion and handle;
B, distillation: the xln-extraction solvent mixed solution after the phase inversion processing is put into still kettle, add as the softening agent in the table 3, add thermal still under stirring and vacuum condition, drive vacuum pump, regulating vacuum tightness is-0.092MPa that distillation time is 2 hours;
C, allotment: allocated as other composition in the table 3 above-mentioned the adding through the pearly-lustre crystal after the distillation, promptly obtain finished product after the allotment;
The extraction solvent of the compound method of embodiment 12~15 is a methylene dichloride, and other technological process is with embodiment 11, and the present invention will repeat no more.
Specific embodiment described in the present invention only is that the present invention's spirit is illustrated.The technician of the technical field of the invention can to described specific embodiment make various modifications replenish or adopt like mode substitute, but can't depart from spirit of the present invention or surmount the defined scope of appended claims.
Although the present invention has been made detailed explanation and has quoted some specific exampless as proof, to those skilled in the art, only otherwise leave that the spirit and scope of the present invention can be done various variations or correction is obvious.

Claims (11)

1. pearlite slurry, it is characterized in that: this pearlite slurry is formulated by following method:
A, phase inversion are handled: the aqueous suspension of the pearly-lustre crystal being put into the pure water formation xln of specific conductivity≤0.5 μ s/cm, while stirring emulsifying agent is mixed with the aqueous suspension of xln, carry out sedimentation after the mixing, after the sedimentation 1~3 hour, extraction solvent is sprayed on the blended liquid level, carries out phase inversion and handle;
B, distillation: softening agent is joined in xln-extraction solvent after phase inversion is handled, stir and vacuum condition under add thermal distillation, wherein vacuum tightness be-0.01MPa~-0.092MPa, distillation time is 2~5 hours;
C, allotment: allocate through the adding of the pearly-lustre crystal after distillation organic solvent above-mentioned, promptly obtain finished product after the allotment; Wherein the weight ratio of pearly-lustre crystal, softening agent and organic solvent is 20~65:2~50:3~60; Described softening agent is a dioctyl phthalate (DOP), dibutyl phthalate, diisobutyl phthalate, dioctyl terephthalate, adipic acid dioctyl ester, dioctyl sebacate, one or more mixing in the dimethyl phthalate; Described organic solvent is one or more mixing in ester solvent, alcohol ether solvents, the ketone solvent; Described pearly-lustre crystal is synthetic by the following method: the acetic acid that adds purity 〉=99.9% on request, add behind the acetic acid after 5~20 minutes, stir acetic acid and add the plumbous oxide of purity 〉=99.99%, after adding finishes, continue to stir 15~40 minutes, add activated carbon and add the pure water of specific conductivity≤0.5 μ s/cm, continue to stir 5~20 minutes, leave standstill; After treating feed clarification, filter and make intermediate, basin is stand-by; Wherein reactant accounts for the weight percent of entire reaction liquid and is: acetic acid: 0.1%~3%, and lead ion: 1%~10%;
The yellow soda ash of purity 〉=99.8% is joined in the pure water of specific conductivity≤0.5 μ s/cm and generate crystal seed, wherein to account for the weight percent of entire reaction liquid be 0.018%~0.04% to yellow soda ash;
The pure water that adds specific conductivity≤0.5 μ s/cm in reactor after 0.5~3 minute, adds the mixed solution of above-mentioned intermediate and AG acetic acid while stirring, after 0.5~3 minute, adds crystal seed; Through synthetic pearly-lustre crystal after the dynamic response, in dynamic reaction process, add pure water or the SODIUMNITRATE of Soda Ash Light 99.2min., above-mentioned intermediate, specific conductivity≤0.5 μ s/cm; Wherein the time of dynamic response is 3~10 hours; The pH value 6.50~7.50 of reaction process solution, temperature of reaction are 0~50 ℃.
2. pearlite slurry according to claim 1 is characterized in that, the weight percent of described composition is:
Pearly-lustre crystal: 25%~60%; Softening agent 10%~40%
Organic solvent: 5%~50%.
3. pearlite slurry according to claim 1 and 2 is characterized in that, described ester solvent is mixed by in N-BUTYL ACETATE, vinyl acetic monomer, the amyl acetate-n one or more.
4. pearlite slurry according to claim 1 and 2 is characterized in that, described alcohol ether solvents is an ethylene glycol ethyl ether.
5. pearlite slurry according to claim 1 and 2 is characterized in that, described ketone solvent is one or more mixing in hexone, pimelinketone, acetone, the methylethylketone.
6. pearlite slurry according to claim 1 and 2 is characterized in that also comprising in the composition of following weight per-cent one or more; Flow agent 0~50%; Defoamer 0~4%; Naphthane: 0~8%; Wherein said flow agent is a kind of in Synolac, acrylic resin, the nitro-resin; Described defoamer is a silicone oil.
7. pearlite slurry according to claim 6 is characterized in that, described silicone oil is methyl-silicone oil.
8. pearlite slurry according to claim 1 and 2 is characterized in that, described emulsifying agent is an oleic acid sodium sulfonate compound.
9. pearlite slurry according to claim 8 is characterized in that, described oleic acid sodium sulfonate compound is one or more mixing in Sodium dodecylbenzene sulfonate, disodium 4-dodecyl-2,4 '-oxydibenzenesulfonate, the Viscotrol C sodium sulfate.
10. pearlite slurry according to claim 1 and 2 is characterized in that, described extraction solvent is a kind of in methylene dichloride, trichloromethane, tributyl phosphate, dibutyl butylphosphonate, di(2-ethylhexyl)phosphate (the 2-ethyl) ester.
11. pearlite slurry according to claim 1 and 2 is characterized in that, described vacuum degree control-0.05MPa~-0.092MPa, distillation time was controlled at 3~4 hours.
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CN1045594A (en) * 1989-03-16 1990-09-26 郑之平 Stereoscopic decorating materials
CN1616568A (en) * 2003-09-22 2005-05-18 本田技研工业株式会社 White pearlescent paint compositions and coatings

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