CN1693199A - Method for fine grading synthesis mica powder by wet method - Google Patents
Method for fine grading synthesis mica powder by wet method Download PDFInfo
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- CN1693199A CN1693199A CN 200510034877 CN200510034877A CN1693199A CN 1693199 A CN1693199 A CN 1693199A CN 200510034877 CN200510034877 CN 200510034877 CN 200510034877 A CN200510034877 A CN 200510034877A CN 1693199 A CN1693199 A CN 1693199A
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Abstract
A method for precisely classifying the synthetic mica powder includes such steps as creating the mathematical model about the granularity of raw material and the setting speed meeting the granularity distribution of product, pulping the synthetic mica powder, feeding it into classifying pool, defining its setting speed, measuring the pulp depth, calculating the setting time, natural setting, draining the suspension and baking the deposit.
Description
Technical field
The present invention relates to the stage division of the accurate size-grade distribution control of a kind of wet method compound mica.
Background technology
Modern production pearly pigment and the functional stuffing of making the cosmetics of super quality all need to use accurate narrow distribution wet method compound mica, could produce pearl effect preferably.But the fine grading of wet method compound mica is the technical barrier that the wet method compound mica is produced always, traditional screening is not suitable for less than 400 purpose classifications, even greater than 400 purpose products, because its sieving property is poor, thereby requiring pulp density little, this just causes a large amount of waters and equipment huge.The hydrocyclone of other wet methods, the cyclone classifier of dry method all can not obtain the mica powder of narrow size-grade distribution.
Summary of the invention
At the defective of traditional stage division, the present invention proposes a kind of method for fine grading synthesis mica powder by wet method.
Technical scheme of the present invention may further comprise the steps:
(1). set up feed size and the mathematical model that meets the settling velocity that Granularity Distribution requires;
(2). compound mica is smash slurry disperse;
(3). the ore pulp that step (2) forms is sent into grading pool, the sampling and testing ore pulp feed size, determine settling velocity according to the mathematical model that step (1) is set up;
(4). measure the degree of depth of ore pulp in the grading pool, calculate the settling time according to settling velocity then;
(5). allow ore pulp natural subsidence in the settling time that calculates;
(6). the suspension of draining, take out sediment;
(7). sediment is dried standard-required, obtain product.
In one embodiment, described mathematical model is to adopt following method to set up:
(1). select a certain feed size
A. will prop up in the container through smashing the slurry dispersive mica powder ore pulp N that packs into simultaneously, and it is identical to keep N to prop up the height of ore pulp in the container, all is H;
B. the suspension T drains at interval each container successively with specific time after the time in takes out sediment and oven dry;
C. measure and write down the particle size distribution data of sediment;
D. analyze particle size distribution data, determine to meet the settling time that Granularity Distribution requires,, calculate best settling velocity then according to the height H of ore pulp;
(2). to different feed sizes, repeating step a-d sets up the mathematical model of feed size and best settling velocity.
Described to smash that slurry disperses be with the compound mica through the rolling desanding, smashes the slurry dispersion by solid-to-liquid ratio 1: 7～10 batchings.
Described smash the slurry jitter time be 0.5～1 hour.
Described oven dry is to adopt the drying room oven dry, and drying time is 18～24 hours, up to the water content of product less than 1%.
The present invention has proposed a kind of control method of fine grading first---the natural sedimentation under the mathematical model control.Narrow size-grade distribution and the adjustable compound mica product of size-grade distribution can be produced with this method, the technical requirement of pearl mica and makeup can be satisfied.And this stage division is simple and easy to do, equipment can be numerous can letter, very easily realize industrialization, and constant product quality.
Embodiment
Embodiment 1
Product requirement: granularity 600 orders, the size-grade distribution standard-required is: d
95=48 ± 1 μ m, d
90=42.5 ± 1 μ m, d
50=22 ± 1 μ m, d
10=10.8 ± 0.8 μ m, d
5=8.5 ± 0.5 μ m.
(1). meet the feed size of Granularity Distribution requirement and the mathematical model of settling velocity in laboratory foundation;
A. selecting a certain feed size, will be on a small quantity pack into simultaneously in 3 containers through smashing slurry dispersive mica powder ore pulp, and keep the height of ore pulp in 3 containers identical, all is 10cm; After 40 minutes, the suspension in the 1st container of draining takes out sediment and oven dry, measures and write down the particle size distribution data of sediment; After 45 minutes, the suspension in the 2nd container of draining takes out sediment and oven dry equally, measures and write down the particle size distribution data of sediment; After 50 minutes, the suspension in the 2nd container of draining takes out sediment and oven dry equally, measures and write down the particle size distribution data of sediment; Three groups of experimental datas and product requirement are compared, and drawing 45 minutes was the best settling time of suspension of draining, and then according to formula: the height ÷ settling time of settling velocity=ore pulp, can calculate best settling velocity is 0.22cm/ minute.
B. reselect feed size, and repeat the A experiment, can set up mathematics curved line relation a: y=-1.2*10
-2X+0.74, wherein y is for falling heavy speed (cm/ minute), and x is charging d
90(μ m).
(2). with all synthetic mica powder raw materials through the rolling desanding, smash slurry by solid-to-liquid ratio 1: 7～10 batchings and disperse, the time is 0.5 hour;
(3). the ore pulp that step (2) forms is sent into grading pool, sampling record ore pulp feed size be distributed as d
95=46 ± 3 μ m, d
90=39 ± 3 μ m, d
50=21 ± 2 μ m, d
10=8.2 ± 1 μ m, d
5=6.0 ± 0.5 μ m, the mathematical model that contrast step (1) is set up determines that settling velocity is 0.26cm/ minute;
(4). the degree of depth that records ore pulp in the grading pool is 40cm, and then drawing the settling time is 154 minutes;
(5). allow ore pulp natural subsidence in 154 minutes; The suspension of draining then takes out sediment; With sediment oven dry 20 hours, can obtain water content less than 1% qualified product.
Claims (5)
1. method for fine grading synthesis mica powder by wet method may further comprise the steps:
(1). set up feed size and the mathematical model that meets the settling velocity that Granularity Distribution requires;
(2). compound mica is smash slurry disperse;
(3). the ore pulp that step (2) forms is sent into grading pool, and the feed size of sampling and testing ore pulp is determined settling velocity according to the mathematical model that step (1) is set up;
(4). measure the degree of depth of ore pulp in the grading pool, calculate the settling time according to settling velocity then;
(5). allow ore pulp natural subsidence in the settling time that calculates;
(6). the suspension of draining, take out sediment;
(7). sediment is dried standard-required, obtain product.
2. according to the method for fine grading synthesis mica powder by wet method of claim 1, wherein said mathematical model is to adopt following method to set up:
(1). select a certain feed size
A. will prop up in the container through smashing the slurry dispersive mica powder ore pulp N that packs into simultaneously, and it is identical to keep N to prop up the height of ore pulp in the container, all is H;
B. the suspension T drains at interval each container successively with specific time after the time in takes out sediment and oven dry;
C. measure and write down the particle size distribution data of sediment;
D. analyze particle size distribution data, determine to meet the settling time that Granularity Distribution requires,, calculate best settling velocity then according to the height H of ore pulp;
(2). to different feed sizes, repeating step a-d sets up the mathematical model of feed size and best settling velocity.
3. according to the method for fine grading synthesis mica powder by wet method of claim 1, wherein said to smash that slurry disperses be with the compound mica through the rolling desanding, smashes the slurry dispersion by solid-to-liquid ratio 1: 7～10 batchings.
4. according to the method for fine grading synthesis mica powder by wet method of claim 3, wherein said to smash the slurry dispersive time be 0.5～1 hour.
5. according to the method for fine grading synthesis mica powder by wet method of claim 1, wherein said oven dry is to adopt the drying room oven dry, and drying time is 18～24 hours, up to the water content of product less than 1%.
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
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| WO2009062886A1 (en) | 2007-11-16 | 2009-05-22 | Basf Se | Bright interference pigments |
| WO2011051122A1 (en) | 2009-10-28 | 2011-05-05 | Basf Se | Pigments with improved sparkling effect |
| CN101209836B (en) * | 2006-12-28 | 2011-07-06 | 深圳市比克电池有限公司 | Classification method for graphite material |
| WO2011095447A2 (en) | 2010-02-04 | 2011-08-11 | Basf Se | Pigment compositions with improved sparkling effect |
| CN101671034B (en) * | 2009-09-21 | 2011-11-23 | 江阴市友佳珠光云母有限公司 | Synthetic mica prepared from calcined talcum and preparation method and processing method of fluorophlogopite powder and fluorophlogopite pearlescent pigment |
| CN102788743A (en) * | 2012-07-23 | 2012-11-21 | 辽宁科技大学 | Elutriation device |
| CN107216688A (en) * | 2017-05-26 | 2017-09-29 | 杭州弗沃德精细化工有限公司 | A kind of grinding stage division of mica powder of wet process |
| CN110595965A (en) * | 2019-09-20 | 2019-12-20 | 中煤科工集团武汉设计研究院有限公司 | Selection method for slurry particle grading for pipeline transportation |
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| CN101524663B (en) * | 2009-03-18 | 2013-01-16 | 福州坤彩精化有限公司 | Method for classifying compound mica |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1020708C (en) * | 1988-01-21 | 1993-05-19 | 希欧欧匹化学株式会社 | Method for producing fluorine mica |
| JP3904337B2 (en) * | 1999-02-24 | 2007-04-11 | トピー工業株式会社 | Synthetic mica powder, method for producing the same, and cosmetics containing the powder |
| CN1253372C (en) * | 2003-09-30 | 2006-04-26 | 孙海英 | Artificial crystal synthetic mica, preparing method and apparatus thereof |
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2005
- 2005-06-01 CN CNB2005100348773A patent/CN1305766C/en active Active
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101209836B (en) * | 2006-12-28 | 2011-07-06 | 深圳市比克电池有限公司 | Classification method for graphite material |
| WO2009062886A1 (en) | 2007-11-16 | 2009-05-22 | Basf Se | Bright interference pigments |
| CN101671034B (en) * | 2009-09-21 | 2011-11-23 | 江阴市友佳珠光云母有限公司 | Synthetic mica prepared from calcined talcum and preparation method and processing method of fluorophlogopite powder and fluorophlogopite pearlescent pigment |
| WO2011051122A1 (en) | 2009-10-28 | 2011-05-05 | Basf Se | Pigments with improved sparkling effect |
| WO2011095447A2 (en) | 2010-02-04 | 2011-08-11 | Basf Se | Pigment compositions with improved sparkling effect |
| CN102788743A (en) * | 2012-07-23 | 2012-11-21 | 辽宁科技大学 | Elutriation device |
| CN102788743B (en) * | 2012-07-23 | 2014-04-09 | 辽宁科技大学 | Elutriation device |
| CN107216688A (en) * | 2017-05-26 | 2017-09-29 | 杭州弗沃德精细化工有限公司 | A kind of grinding stage division of mica powder of wet process |
| CN107216688B (en) * | 2017-05-26 | 2018-12-04 | 杭州弗沃德精细化工有限公司 | A kind of grinding stage division of mica powder of wet process |
| CN110595965A (en) * | 2019-09-20 | 2019-12-20 | 中煤科工集团武汉设计研究院有限公司 | Selection method for slurry particle grading for pipeline transportation |
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| CN1305766C (en) | 2007-03-21 |
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Address after: 515000 first floor of Jia Feng mansion, B11-5 block, Shantou Free Trade Zone, Guangdong. Patentee after: Guangdong Triratna new material Science and Technology Co.,Ltd. Address before: 515000 first floor of Jia Feng mansion, B11-5 block, Shantou Free Trade Zone, Guangdong. Patentee before: SHANTOU SANBAO MICA TECHNOLOGY CO.,LTD. |
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Address after: 515000 first floor of Jia Feng mansion, B11-5 block, Shantou Free Trade Zone, Guangdong. Patentee after: SHANTOU SANBAO MICA TECHNOLOGY CO.,LTD. Address before: 515041 room 902, Longxiang commercial building, Changping Road, Shantou, Guangdong Patentee before: SHANTOU FTZ SANBAO PEARL LUSTER MICA TECHNOLOGY Co.,Ltd. |
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