CN104016364A - Sodium modified chlorite - Google Patents

Sodium modified chlorite Download PDF

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Publication number
CN104016364A
CN104016364A CN201410237833.XA CN201410237833A CN104016364A CN 104016364 A CN104016364 A CN 104016364A CN 201410237833 A CN201410237833 A CN 201410237833A CN 104016364 A CN104016364 A CN 104016364A
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China
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chlorite
sodium
flap
mixture
batching
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CN201410237833.XA
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CN104016364B (en
Inventor
黄飞翔
黄允金
陈丽萍
许盛英
许庆华
蒋文兰
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Zhejiang Chuangwei New Material Co ltd
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  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

The invention discloses sodium modified chlorite, and the key points of the technical scheme are that: sodium modified chlorite ingredients comprise chlorite, magnesium oxide, sodium carbonate, instant sodium silicate, polyvinyl alcohol, hydroxypropyl methyl cellulose and sodium acid pyrophosphate. A production method of the sodium modified chlorite is as follows: sodium modified chlorite ingredients are transported into a mill for powder milling, and the milled powder is the sodium modified chlorite. By first sodium modification and then ingredient compounding, chemical reaction of the sodium carbonate and the instant sodium silicate, the polyvinyl alcohol and the hydroxypropyl methyl cellulose can be avoided. According to the needs of product quality, the sodium acid pyrophosphate is used for adjusting the PH of the sodium modified chlorite. The sodium modified chlorite has the characteristics of good adsorption, suspension property, thixotropy, lubricity and thermal stability and high plasticity, and is applicable to the production of filler, sorbents, suspending agents and lubricants for asphalt felts, paper making, pesticides and fire control products.

Description

Chlorite after sodium
Technical field
The present invention relates to sodium processing, be specifically related to the chlorite after a kind of sodium.
Background technology
Chlorite is a kind of aluminium silicate mineral, and normal and spontaneous quartzy symbiosis, is needle shape, bobbles shape, rose-shaped, and the occurrence in hole has hole liner and pore filling.General needle shape chlorite mostly is hole liner and is wrapped in particle surface, bobbles shape and rose-shaped being filled in hole.Chlorite can be by Mineral Transformation such as biotite, hornblende, montmorillonites, and authigenic chlorite is generally rich in high price iron ion, and easily produce precipitation with the acid solution effect such as HCL in drilling fluid, and cause reservoir damage, be acid sensitivity mineral.
In chlorite mining area, usage mining machine carries out mechanical mining chlorite raw ore, excavate out be a kind of compact mass chlorite raw ore, can not be directly used in sodium processing.
Sodium is not carried out follow-up complementary modification after processing, and can not improve the quality of chlorite product comprehensively.
Summary of the invention
The object of the invention is to overcome weak point in prior art, the chlorite after a kind of sodium is provided.
Chlorite batching after sodium is made up of chlorite, magnesium oxide, sodium carbonate, quick dissolved sodium silicate, polyvinyl alcohol, Vltra tears and sodium acid pyrophosphate.
The production method of the chlorite after sodium: by abrasive dust in the chlorite batching input grinding machine after sodium, the meal after abrasive dust is the chlorite after sodium.
Chlorite is extensively present in occurring in nature using forms such as particulate aggregate, crystallization lamellar bodies as the product of normal metamorphism, sedimentation and hydrothermal alteration effect conventionally.Its crystalline structure, physical properties, Chemical Composition and geological occurrence are in close relations, have certain metallogenic relation, chlorite particle fineness≤0.5 millimeter that the present invention selects.
Magnesium oxide has the general character of basic oxide, belongs to gelling material, can improve the colloidal property of chlorite.
Sodium carbonate has the general character and the thermostability of salt, soluble in water, and its aqueous solution is alkalescence, is the main raw material of sodium in the present invention.
Quick dissolved sodium silicate is white pulverulent material, can be dissolved in fast water, has that cohesive force is strong, intensity is higher, acid resistance, good heat resistance, the feature of alkali resistance and poor water resistance.
Polyethenol series white solid, that external form is divided is cotton-shaped, particulate state, Powdered three kinds; Nonpoisonous and tasteless, particulate state can be dissolved in 80--90 DEG C of water, pulverously after other powders pre-dispersed, can dissolve at normal temperatures.There is good viscosity, polymerizability, cohesiveness and water-retentivity.
Vltra tears has thickening capabilities, salt discharge, pH stability, water-retentivity, dimensional stability, good film-forming properties and the feature such as resistance to enzyme, dispersiveness and cohesiveness widely.
Sodium acid pyrophosphate is a kind of white powder, and relative density 1.86 is water-soluble, and the pH value of 1% aqueous solution is 3.5~4.5, for adjusting the chlorite pH value after sodium.
The present invention is achieved by following technical proposals:
1, the batching of the chlorite after sodium is made up of following component by weight percentage: chlorite flap 90~98%, quick dissolved sodium silicate 0.1~5%, polyvinyl alcohol 0.1~5%, Vltra tears 0.01~3% and sodium acid pyrophosphate 0~5%.
2, the production method of the chlorite after sodium: by abrasive dust in the chlorite batching input grinding machine after sodium, particle fineness≤0.074 millimeter, the meal after abrasive dust is the chlorite after sodium.
3, the production method of chlorite flap: (1) by chlorite mixture input fermentation vat, then water is slowly added in chlorite mixture and soaks sodium, sodium soak time is 24~72 hours; (2) take out the chlorite mixture after soaking, input is stirred in biaxial rneader, inputs and in extrusion machine, be extruded into chlorite flap, chlorite thickness of flap≤3 millimeter after stirring.
(3) chlorite flap is transported in rotary type stoving oven and is dried, drying time control is 1~3 hour, and bake out temperature is controlled at 80~100 DEG C, and the chlorite flap water content after oven dry is 10~15%, and PCm is weight percentage.
4, the batching of chlorite flap is made up of following component by weight percentage: chlorite mixture 65~85% and water 15~35%.
5, the production method of chlorite mixture: by stirring in the batching input stirrer of chlorite mixture, be chlorite mixture after stirring.
6, the batching of chlorite mixture is made up of following component by weight percentage: chlorite 92~98%, magnesium oxide 0.5~5% and sodium carbonate 0.5~5%.
The production method of the chlorite after sodium takes first sodium to carry out compounding ingredient again, can avoid sodium carbonate and quick dissolved sodium silicate, polyvinyl alcohol and Vltra tears generation chemical reaction, give full play to raw-material characteristic separately in batching, and obtain complementation, guarantee the chlorite inner quality after sodium.
According to the needs of quality product, adopt sodium acid pyrophosphate to adjust the chlorite pH value after sodium.
Chlorite after sodium has good adsorptivity, suspension, thixotropy, oilness, thermostability and higher plasticity-feature.
Chlorite after sodium is applicable to produce filler, sorbent material, suspension agent and the lubricant of malthoid, papermaking, agricultural chemicals, fire product.
Embodiment
Below in conjunction with embodiment, the invention will be further described:
1, the batching of the chlorite after sodium is made up of following component by weight percentage: chlorite flap 95.6%, quick dissolved sodium silicate 2.1%, polyvinyl alcohol 1.6%, Vltra tears 0.5% and sodium acid pyrophosphate 0.2%.
2, the production method of the chlorite after sodium: by abrasive dust in the chlorite batching input grinding machine after sodium, particle fineness≤0.074 millimeter, the meal after abrasive dust is the chlorite after sodium.
3, the production method of chlorite flap: (1) by chlorite mixture input fermentation vat, then water is slowly added in chlorite mixture and soaks sodium, sodium soak time is 48 hours; (2) take out the chlorite mixture after soaking, input is stirred in biaxial rneader, inputs and in extrusion machine, be extruded into chlorite flap, chlorite thickness of flap≤3 millimeter after stirring; (3) chlorite flap is transported in rotary type stoving oven and is dried, drying time control is 2 hours, and bake out temperature is controlled at 80~100 DEG C, and the chlorite flap water content after oven dry is 10~12%.
4, the batching of chlorite flap is made up of following component by weight percentage: chlorite mixture 76% and water 24%.
5, the production method of chlorite mixture: by stirring in the batching input stirrer of chlorite mixture, be chlorite mixture after stirring.
6, the batching of chlorite mixture is made up of following component by weight percentage: chlorite 94.5%, magnesium oxide 3% and sodium carbonate 2.5%.

Claims (7)

1. the chlorite after a sodium, it is characterized in that, the chlorite batching after sodium is made up of following component by weight percentage: chlorite flap 90~98%, quick dissolved sodium silicate 0.1~5%, polyvinyl alcohol 0.1~5%, Vltra tears 0.01~3% and sodium acid pyrophosphate 0~5%.
2. the production method of the chlorite after sodium according to claim 1, is characterized in that, by abrasive dust in the chlorite batching input grinding machine after sodium, and particle fineness≤0.074 millimeter, the meal after abrasive dust is the chlorite after sodium.
3. the production method of chlorite flap according to claim 1, is characterized in that, (1) by chlorite mixture input fermentation vat, then water is slowly added in chlorite mixture and soaks sodium, and sodium soak time is 24~72 hours; (2) take out the chlorite mixture after soaking, input is stirred in biaxial rneader, inputs and in extrusion machine, be extruded into chlorite flap, chlorite thickness of flap≤3 millimeter after stirring; (3) chlorite flap is transported in rotary type stoving oven and is dried, drying time control is 1~3 hour, and bake out temperature is controlled at 80~100 DEG C, and the chlorite flap water content after oven dry is 10~15%, and PCm is weight percentage.
4. the batching of chlorite flap according to claim 1, is characterized in that, the batching of chlorite flap is made up of following component by weight percentage: chlorite mixture 65~85% and water 15~35%.
5. the production method of chlorite mixture according to claim 3, is characterized in that, by stirring in the batching input stirrer of chlorite mixture, is chlorite mixture after stirring.
6. the batching of chlorite mixture according to claim 5, is characterized in that, the batching of chlorite mixture is made up of following component by weight percentage: chlorite 92~98%, magnesium oxide 0.5~5% and sodium carbonate 0.5~5%.
7. chlorite according to claim 6, is characterized in that chlorite particle fineness≤0.5 millimeter of selecting.
CN201410237833.XA 2014-06-01 2014-06-01 Chlorite after sodium Active CN104016364B (en)

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58135121A (en) * 1982-01-30 1983-08-11 Osaka Soda Co Ltd Manufacture of formed zeolite
CN1912015A (en) * 2006-08-25 2007-02-14 蒋文兰 Concave convex rod suspension agent
CN101781881A (en) * 2009-12-08 2010-07-21 许庆华 Method for absorbing and cleaning road surface oil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58135121A (en) * 1982-01-30 1983-08-11 Osaka Soda Co Ltd Manufacture of formed zeolite
CN1912015A (en) * 2006-08-25 2007-02-14 蒋文兰 Concave convex rod suspension agent
CN101781881A (en) * 2009-12-08 2010-07-21 许庆华 Method for absorbing and cleaning road surface oil

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