CN102887531B - Technique for producing potassium fluoride from potassium fluosilicate - Google Patents

Technique for producing potassium fluoride from potassium fluosilicate Download PDF

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CN102887531B
CN102887531B CN201210389440.1A CN201210389440A CN102887531B CN 102887531 B CN102887531 B CN 102887531B CN 201210389440 A CN201210389440 A CN 201210389440A CN 102887531 B CN102887531 B CN 102887531B
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potassium
fluoride
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fluosilicate
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CN102887531A (en
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张军航
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Yunnan Fluorine Industry Environmental Protection Polytron Technologies Inc
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Abstract

The invention relates to a technique for producing potassium fluoride and coproducing high-purity silicon dioxide and sodium fluoride mainly from potassium fluosilicate, liquid potassium (liquid potassium hydroxide) and sodium hydroxide. The invention provides a method for producing potassium fluoride from a new fluorine source potassium fluosilicate instead of anhydrous hydrogen fluoride. All potassium for generating the potassium fluoride is derived from potassium in the potassium fluosilicate, thereby lowering the raw material cost of the potassium fluoride; a silicon complexing reagent is added to prevent the ammonia from generating complex precipitates of ammonium fluosilicate and ammonium fluoride during desilication and enhance the separability between silicon dioxide and water; and the potassium fluosilicate is synthesized from the anhydrous hydrogen fluoride production line byproduct fluosilicic acid and byproduct potassium chloride, thereby enhancing the product quality of potassium fluoride, lowering the raw material cost for potassium fluoride and enhancing the benefits of the potassium fluoride production enterprise.

Description

A kind of technique that uses potassium silicofluoride to produce Potassium monofluoride
Technical field
The invention belongs to chemical field, specifically a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride.
Background technology
Potassium monofluoride purposes is quite extensive, and for various glass etchings, food is anticorrosion, electroplate, wood preservative, welding fusing assistant, agricultural insecticide and pesticide intermediate, pharmaceutical industry raw material and organic raw material, catalyzer, absorption agent (absorbing HF and moisture) etc. fluoridized.Also be the raw material of producing potassium hydrogen fluoride.
The features such as fluorine-containing medicines has efficiently, wide spectrum, low toxicity, low residue, Drugs Containing Fluorine reaches hundreds of in the world at present, it is a very important class in synthetic drugs, there are many medicines to become the principal item for the treatment of some disease, as fluoroquinolones antibiotics Ofloxacine USP 23, antidepressant class medicine fluoxetine, diabetes class medicine sitagliptin etc.Because fluorine organic compound has special biological activity and biological fitness, the exploitation that therefore sets it as medicine is very active, and many product innovations are still among exploitation endlessly.At present, the research and development of fluoro-containing pesticide, medicine, dye well liquid crystal are in the ascendant with production, occurred a large amount of high performance fluorochemicalss, and wherein the fluorine of a lot of products gets on by Potassium monofluoride " extension ".Potassium monofluoride is as the important source material of fluorine-containing medicines intermediate, and development prospect is considerable.Mostly the method for traditional mode of production Potassium monofluoride is to adopt the reaction of potassium hydroxide-hydrofluoric acid neutralisation to make, and the hydrofluoric acid in traditional technology is mainly made by fluorite and sulfuric acid reaction, and traditional technology need to consume valuable resource fluorite, and hydrofluoric acid cost is quite high.
Summary of the invention
In order to solve the problems of the technologies described above, the invention provides a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride.
Reaction formula of the present invention is:
K2SiF6+4KOH――→6KF+SiO2+4H2O
KF+NaOH――→KOH+NaF
Use potassium silicofluoride to produce a technique for Potassium monofluoride, it is characterized in that it comprises the steps:
1) liquid potassium hydroxide is added to reactor, starts stirring, add silicon complexing agent, at the uniform velocity add potassium silicofluoride solid, fully reaction;
2) reaction solution carries out solid-liquid separation, and solid is pulled an oar to clean and is high-purity silicon dioxide, obtains after drying white carbon black;
3) a part of reaction solution of second step is added to Sodium Fluoride synthesis reactor, open and stir, input sodium hydroxide at the uniform velocity, after having reacted, carry out solid-liquid separation, solid is dried and is finished product Sodium Fluoride, and liquid enters liquid potassium hydroxide storage tank, uses in order to desiliconization;
4) a part of reaction solution of second step is added to transfer tank, precipitation 24h, clear liquid adds Potassium monofluoride concentration kettle;
5) the Potassium monofluoride mother liquor after concentrated is added to groove to be painted, then squeeze into spray-drying tower by groove to be painted and spray and be dried, finished product is anhydrous potassium fluoride.
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, is characterized in that the mass percentage concentration of the liquid potassium hydroxide described in step 1) is 48%.
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, the amount that it is characterized in that the silicon complexing agent adding in step 1) is 0.2% of liquid potassium hydroxide weight.
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, is characterized in that adding potassium silicofluoride solid according to 0.9 times of the required mole number of reaction in step 1).
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, it is characterized in that reacting in step 1) to the pH value of reaction end be 8.5-9.
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, is characterized in that, in step 3), 2/3 reaction solution of second step is added to Sodium Fluoride synthesis reactor, in step 4), 1/3 remaining reaction solution of second step is added to transfer tank.
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, is characterized in that adding sodium hydroxide according to 0.9-1 times of the required mole number of reaction in step 3).
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, is characterized in that the mass percentage concentration that is concentrated into solution in still in step 4) reaches 48%-50%.
Described a kind of technique that uses potassium silicofluoride to produce Potassium monofluoride, is characterized in that the silicon complexing agent in step 1) is nitrilotriacetic acid(NTA) sodium.
A kind of technique that uses potassium silicofluoride to produce Potassium monofluoride of the present invention, provide a kind of new fluorine source potassium silicofluoride to replace anhydrous hydrogen fluoride to produce the method for Potassium monofluoride, the potassium that generates Potassium monofluoride all derives from the potassium in potassium silicofluoride, greatly reduce the raw materials cost of Potassium monofluoride, add silicon complexometric reagent, while preventing with ammonia desiliconization, generate the complex compound sediment of ammonium silicofluoride and Neutral ammonium fluoride, improve the separation property of silicon-dioxide and water, to be that anhydrous hydrogen fluoride production line byproduct silicofluoric acid and by-product Repone K are synthetic make potassium silicofluoride, improve Potassium monofluoride quality product, reduce Potassium monofluoride material cost, promote Potassium monofluoride manufacturing enterprise benefit.
Embodiment
Embodiment 1
1, the liquid potassium hydroxide that is 48% by mass percentage concentration adds reactor, start stirring, add the nitrilotriacetic acid(NTA) sodium of 0.2% amount of liquid potassium hydroxide weight, at the uniform velocity add potassium silicofluoride solid according to 0.9 times of the required mole number of reaction formula, fully reaction, the pH value of reaction end is 8.5-9.
2, after reacting completely in reactor, reaction solution carries out solid-liquid separation, and solid is pulled an oar to clean and is high-purity silicon dioxide, can do after drying white carbon black and sell.
3,2/3 reaction solution of second step is added to Sodium Fluoride synthesis reactor, open and stir, at the uniform velocity drop into sodium hydroxide according to 1 times of the required mole number of reaction formula, after having reacted, carry out solid-liquid separation, solid is dried and is finished product Sodium Fluoride, liquid enters liquid potassium hydroxide storage tank, uses in order to desiliconization.
4, the 1/3 remaining reaction solution of second step is added to transfer tank, precipitation 24h, clear liquid adds Potassium monofluoride concentration kettle, and in still, strength of solution reaches 48%, concentrated end.
5, the Potassium monofluoride mother liquor after concentrated is added to groove to be painted, then it is dry to add spray-drying tower to spray by groove to be painted, finished product is anhydrous potassium fluoride.
Embodiment 2
1, the liquid potassium hydroxide that is 48% by mass percentage concentration adds reactor, start stirring, add the nitrilotriacetic acid(NTA) sodium of 0.2% amount of liquid potassium hydroxide weight, at the uniform velocity add potassium silicofluoride solid according to 0.9 times of the required mole number of reaction formula, fully reaction, the pH value of reaction end is 8.5-9.
2, after reacting completely in reactor, reaction solution carries out solid-liquid separation, and solid is pulled an oar to clean and is high-purity silicon dioxide, can do after drying white carbon black and sell.
3,2/3 reaction solution of second step is added to Sodium Fluoride synthesis reactor, open and stir, at the uniform velocity drop into sodium hydroxide according to 1 times of the required mole number of reaction formula, after having reacted, carry out solid-liquid separation, solid is dried and is finished product Sodium Fluoride, liquid enters liquid potassium hydroxide storage tank, uses in order to desiliconization.
4, the 1/3 remaining reaction solution of second step is added to transfer tank, precipitation 24h, clear liquid adds Potassium monofluoride concentration kettle, and in still, strength of solution reaches 50%, concentrated end.
5, the Potassium monofluoride mother liquor after concentrated is added to groove to be painted, then it is dry to add spray-drying tower to spray by groove to be painted, finished product is anhydrous potassium fluoride.
Embodiment 3
1, the liquid potassium hydroxide that is 48% by mass percentage concentration adds reactor, start stirring, add the nitrilotriacetic acid(NTA) sodium of 0.2% amount of liquid potassium hydroxide weight, at the uniform velocity add potassium silicofluoride solid according to 0.9 times of the required mole number of reaction formula, fully reaction, the pH value of reaction end is 8.5-9.
2, after reacting completely in reactor, reaction solution carries out solid-liquid separation, and solid is pulled an oar to clean and is high-purity silicon dioxide, can do after drying white carbon black and sell.
3,2/3 reaction solution of second step is added to Sodium Fluoride synthesis reactor, open and stir, at the uniform velocity drop into sodium hydroxide according to 0.9 times of the required mole number of reaction formula, after having reacted, carry out solid-liquid separation, solid is dried and is finished product Sodium Fluoride, liquid enters liquid potassium hydroxide storage tank, uses in order to desiliconization.
4, the 1/3 remaining reaction solution of second step is added to transfer tank, precipitation 24h, clear liquid adds Potassium monofluoride concentration kettle, and in still, strength of solution reaches 48%, concentrated end.
5, the Potassium monofluoride mother liquor after concentrated is added to groove to be painted, then it is dry to add spray-drying tower to spray by groove to be painted, finished product is anhydrous potassium fluoride.
Table 1 is the Potassium monofluoride product quality analysis result (each embodiment respectively carries out twice experiment) of utilizing method of the present invention to produce, conformance with standard: HG/T 2829-2008
The Potassium monofluoride product quality analysis result that table 1 utilizes method of the present invention to produce
Figure DEST_PATH_IMAGE002
Table 2 is Sodium Fluoride product quality analysis results (each embodiment respectively carries out twice experiment) of utilizing method of the present invention to produce, conformance with standard: GB4293-84
The Sodium Fluoride product quality analysis result that table 2 utilizes method of the present invention to produce
Figure DEST_PATH_IMAGE004
Table 3 is high-purity silicon dioxide (rubber ingredients precipitated hydrated silica) mass analysis results (each embodiment respectively carries out twice experiment) of utilizing method of the present invention to produce, conformance with standard: HG/T 3061-2009
High-purity silicon dioxide (rubber ingredients precipitated hydrated silica) the mass analysis result that table 3 utilizes method of the present invention to produce
Figure DEST_PATH_IMAGE006
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any amendments of doing within the spirit and principles in the present invention, be equal to and replace and improvement etc., within being all included in protection scope of the present invention.

Claims (1)

1. use potassium silicofluoride to produce a technique for Potassium monofluoride, it is characterized in that it comprises the steps:
1) liquid potassium hydroxide that is 48% by mass percentage concentration adds reactor, start stirring, add 0.2% nitrilotriacetic acid(NTA) sodium of liquid potassium hydroxide weight as silicon complexing agent, at the uniform velocity add potassium silicofluoride solid according to reaction 0.9 times of required mole number, fully react to the pH value of reaction end be 8.5-9;
2) reaction solution carries out solid-liquid separation, and solid is pulled an oar to clean and is high-purity silicon dioxide, obtains after drying white carbon black;
3) 2/3 reaction solution of second step is added to Sodium Fluoride synthesis reactor, open and stir, at the uniform velocity drop into sodium hydroxide according to reaction 0.9-1 times of required mole number, after having reacted, carry out solid-liquid separation, solid is dried and is finished product Sodium Fluoride, liquid enters liquid potassium hydroxide storage tank, uses in order to desiliconization;
4) the 1/3 remaining reaction solution of second step is added to transfer tank, precipitation 24h, the mass percentage concentration that clear liquid adds Potassium monofluoride concentration kettle to be concentrated into solution in still reaches 48%-50%;
5) the Potassium monofluoride mother liquor after concentrated is added to groove to be painted, then squeeze into spray-drying tower by groove to be painted and spray and be dried, finished product is anhydrous potassium fluoride.
CN201210389440.1A 2012-10-15 2012-10-15 Technique for producing potassium fluoride from potassium fluosilicate Active CN102887531B (en)

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Publication number Priority date Publication date Assignee Title
CN104030250B (en) * 2014-06-25 2016-04-27 江西渠成氟化学有限公司 A kind of technique using silicofluoric acid to produce sodium bifluoride
CN105439160A (en) * 2015-11-29 2016-03-30 洛阳绿仁环保设备有限公司 Method for preparing potassium silicate from potassium feldspar
CN105439167A (en) * 2015-11-29 2016-03-30 洛阳绿仁环保设备有限公司 Method for preparing 3A molecular sieve from potassium feldspar
CN109019984A (en) * 2018-09-13 2018-12-18 衢州市鼎盛化工科技有限公司 A kind of method and system recycling efficient resource from glass thinning acid pickle
CN109160636A (en) * 2018-10-15 2019-01-08 大连东泰产业废弃物处理有限公司 A kind of technique of high-concentration fluorine-contained base extraction and recycling
CN113060745A (en) * 2021-03-19 2021-07-02 严永生 Preparation method for preparing potassium fluoride by using potash and potassium fluosilicate
CN113233476A (en) * 2021-05-14 2021-08-10 江西渠成氟化学有限公司 Method for preparing potassium fluoride and sodium fluoride
CN114031100A (en) * 2021-12-20 2022-02-11 湖北祥云(集团)化工股份有限公司 Method for preparing fluoride salt from phosphorus ore associated fluorine

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US3656894A (en) * 1970-05-08 1972-04-18 Central Glass Co Ltd Process for the production of high quality synthetic cryolite
US3842161A (en) * 1971-12-13 1974-10-15 Kemira Oy Method of refining the fluorine obtained as a by-product in the fertilizer industry
CN101028934A (en) * 2006-03-01 2007-09-05 多氟多化工股份有限公司 Method for linked producing potassium fluoride white carbon black
CN101376509A (en) * 2007-08-31 2009-03-04 多氟多化工股份有限公司 Method for preparing potassium fluoride

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WO2009113088A2 (en) * 2008-01-14 2009-09-17 Aditya Birla Science & Technology Co. Limited A process for manufacturing of potassium fluoride

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3656894A (en) * 1970-05-08 1972-04-18 Central Glass Co Ltd Process for the production of high quality synthetic cryolite
US3842161A (en) * 1971-12-13 1974-10-15 Kemira Oy Method of refining the fluorine obtained as a by-product in the fertilizer industry
CN101028934A (en) * 2006-03-01 2007-09-05 多氟多化工股份有限公司 Method for linked producing potassium fluoride white carbon black
CN101376509A (en) * 2007-08-31 2009-03-04 多氟多化工股份有限公司 Method for preparing potassium fluoride

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