CN110092354A - Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride - Google Patents

Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride Download PDF

Info

Publication number
CN110092354A
CN110092354A CN201810092466.7A CN201810092466A CN110092354A CN 110092354 A CN110092354 A CN 110092354A CN 201810092466 A CN201810092466 A CN 201810092466A CN 110092354 A CN110092354 A CN 110092354A
Authority
CN
China
Prior art keywords
hydrogen fluoride
melamine
solution
diafiltration
syria
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810092466.7A
Other languages
Chinese (zh)
Inventor
姚鼎文
姚宁
岳莉莉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201810092466.7A priority Critical patent/CN110092354A/en
Publication of CN110092354A publication Critical patent/CN110092354A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B7/00Halogens; Halogen acids
    • C01B7/19Fluorine; Hydrogen fluoride
    • C01B7/191Hydrogen fluoride
    • C01B7/192Preparation from fluorspar

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Silicon Compounds (AREA)
  • Removal Of Specific Substances (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

Cab-O-sil is added in Fluorspar Powder, is allowed to CaF2、SiO2Mole ratio be 1: 1, it is placed in electric furnace, it is passed through water vapour and produces hydrogen fluoride in 800-900 degree Celsius roasting, furnace gas first passes through gravitational settling dedusting, it is passed through melamine slurry again and hydrogen fluoride generates hydrogen fluoride melamine complex salt crystal body, it is reacted again with potassium fluoride solution through diafiltration, generate potassium bifluoride solution and melamine, the latter is returned and goes to react with the HF in furnace gas before this process, the former condensing crystallizing diafiltration is dried to solid, it is placed in thermal decomposition releasing hydrogen fluoride in 400 degree of electric furnaces Celsius and is condensed into anhydrous hydrogen fluoride product, the potassium fluoride for decomposing generation returns to wiring solution-forming before this process and reacts again with hydrogen fluoride melamine double salt, the solid of roaster discharge is through levigate as high-quality siliceous fertilizer.

Description

Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride
Technical field
The present invention is the manufacturing technology of anhydrous hydrogen fluoride, is to belong to halide salt hydrothermal calcine technology neck city.
Background material
Fluorite produces anhydrous hydrogen fluoride, is enriching sulfuric acid decomposition technique both at home and abroad, yet there are no so far and sulfuric acid is not added and obtains To the technology of anhydrous hydrogen fluoride.
Summary of the invention
1, by CaF2H5/SiO2Equal gram molecules hydro-thermal reaction principle is added and fluorite CaF in Fluorspar Powder2It is equimolar SiO2Cab-O-sil.
2, mixture is steam roasting 1 hour logical at 800 1 900 degree Celsius
3, roaster gas is first passed through into gravitational dust collection, enters back into and reacts generation HF, C in melamine slurry with HF3H6N6, nH2O complex salt crystal body, the moisture content in furnace gas are discharged with gaseous state and liquid
4, complex salt crystal body generates potassium bifluoride solution and melamine is solid through diafiltration and certain density kF solution reaction Body, the latter return to front and react with the HF in furnace gas.
5, by KHF2Solution condensing crystallizing is dry, is placed in 400 degree of electric furnaces Celsius and thermally decomposes, and the HF condensation of generation is AHF product, the KF return front for decomposing generation are modulated into kF solution and react again with double salt.
6, by the solid of roaster discharge through levigate as high-quality siliceous fertilizer.
Detailed description of the invention
Fig. 1 is that fluorite adds silica hydrothermal calcine to fabricate anhydrous hydrogen fluoride process flow diagram
By CaF2、SiO2Equal gram molecules hydro-thermal reaction principle is added and fluorite CaF in Fluorspar Powder2Equimolar SiO2's Cab-O-sil.It is mixed into 800 1 900 degree of electric furnaces Celsius and is passed through steam roasting 1 hour, the furnace gas of generation passes through gravitational settling It is passed through reaction in melamine slurry liquid after dedusting and generates HF, C3H6N6, nH2O complex salt crystal body, after diafiltration by its with it is certain dense The KF solution reaction of degree generates potassium bifluoride solution and melamine, the latter's diafiltration return before this process again with the HF in furnace gas It reacts, is placed in 400 degree of electric furnace Celsius and thermally decomposes after the concentrated crystallizing and drying of potassium bifluoride solution, the hydrogen fluoride of generation is through cold Solidifying to become AHF product, the potassium fluoride for thermally decomposing generation is reacted with double salt again back to wiring solution-forming before this process.
Embodiment
Take 1000 grams of CaF2SiO is added in=97% Fluorspar Powder2=98% Cab-O-sil 761.6g, stirs evenly, merging Lead to steam roasting 1 hour in Celsius 850 native 5 degree of electric furnaces, roaster gas first passes through gravity settling basin, enters back into melamine slurry Expect that reactor generates hydrogen fluoride melamine complex salt crystal body, through diafiltration, its fluorination nak response for being 20% with concentration is generated Potassium bifluoride solution simultaneously releases melamine, returns after the latter's diafiltration and goes to react with the HF in furnace gas before this process, generation The concentrated crystallizing and drying of potassium bifluoride solution obtains solid KHF2, it is put into 400 degree of electric furnaces Celsius and thermally decomposes, the gas of generation It is 99.96% mass is 472.8 grams of AHF that body condensation, which is purity, and the KF for decomposing generation, which is returned, is fitted on into solution before this process It is reacted with double salt, the sizing of roaster discharge is carefully high-quality siliceous fertilizer.
Product quality analysis (weight %)

Claims (7)

1. pressing CaF2、SiO2Equal gram molecules hydrothermal calcine reaction principle is added and fluorite CaF in Fluorspar Powder2Equimolar SiO2 Cab-O-sil.
2. being put into 800-900 degree electric furnace Celsius, lead to steam roasting 0.5-1 hours.
3. the flue gas come out from roaster enters trimerization after first passing through gravitational dust collection according to the method that claim 2 Syria is stated Cyanamide slurry liquid generates HF, C3H6N6, nH2O double salt is fixed up.
4. being reacted again with certain density potassium fluoride solution according to double salt in the method that claim 3 Syria is stated through diafiltration, generate Potassium bifluoride solution simultaneously releases melamine.
5. according to the method that claim 4 Syria is stated the HF gone before this process with furnace gas will be returned to after melamine diafiltration Reaction, solution condensing crystallizing diafiltration it is dry potassium bifluoride solid.
6. according to the method that claim 5 Syria is stated, by potassium bifluoride be placed in heat resolve in 400 degree of electric furnaces Celsius go out it is pure HF gas, is condensed into AHF product, and the potassium fluoride of generation returns to wiring solution-forming before this process and goes to answer with hydrogen fluoride melamine The anti-Me of salt.
7. it is high-quality siliceous fertilizer that the solid of roaster discharge is levigate through cooling according to the method that claim 2 Syria is stated.
CN201810092466.7A 2018-01-29 2018-01-29 Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride Pending CN110092354A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810092466.7A CN110092354A (en) 2018-01-29 2018-01-29 Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810092466.7A CN110092354A (en) 2018-01-29 2018-01-29 Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride

Publications (1)

Publication Number Publication Date
CN110092354A true CN110092354A (en) 2019-08-06

Family

ID=67441979

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810092466.7A Pending CN110092354A (en) 2018-01-29 2018-01-29 Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride

Country Status (1)

Country Link
CN (1) CN110092354A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0514701B2 (en) * 1984-06-07 1993-02-25 Tokuyama Soda Kk
CN101269816A (en) * 2008-05-16 2008-09-24 夏克立 Method for producing fluorine series compounds and white carbon black
CN107188145A (en) * 2016-03-14 2017-09-22 姚鼎文 The method that one kind makes industrial potassium dihydrogen phosphate with hydrochloric acid decomposing medium and low grade, melamine complex salt crystal legal system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0514701B2 (en) * 1984-06-07 1993-02-25 Tokuyama Soda Kk
CN101269816A (en) * 2008-05-16 2008-09-24 夏克立 Method for producing fluorine series compounds and white carbon black
CN107188145A (en) * 2016-03-14 2017-09-22 姚鼎文 The method that one kind makes industrial potassium dihydrogen phosphate with hydrochloric acid decomposing medium and low grade, melamine complex salt crystal legal system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张邦建等: "《食品卫生检测技术》", 海洋出版社 *

Similar Documents

Publication Publication Date Title
FI56556C (en) FOERFARANDE FOER AVLAEGSNANDE AV KVICKSILVER UR GASER
CN103896215A (en) Fluorite-sulfuric acid method for preparing hydrogen fluoride
CN105314599B (en) A kind of method that anhydrous hydrogen fluoride and white carbon are produced using fluosilicic acid
CN101708418A (en) Method for recycling waste gas containing fluorine
US2631083A (en) Production of calcium fluoride and silica
CN110092354A (en) Fluorite adds the method for silica hydrothermal calcine processing and manufacturing anhydrous hydrogen fluoride
JP2010517904A (en) Preparation of hydrogen fluoride from calcium fluoride and sulfuric acid
US2785953A (en) Process for preparing a dry mixture of ammonium fluosilicate and silica
US2833628A (en) Manufacture of silicon tetrafluoride
CN110759368B (en) Method for extracting aluminum oxide by activating fly ash
IE41784B1 (en) Recovery of fluorine from aqueous liquids
US3338673A (en) Recovery of substantially anhydrous hydrogen fluoride from an impure aqueous ammonium fluoride solution
US3219410A (en) Method for recovering hydrogen fluoride from waste gases
US3021194A (en) Production of ammonium hydrogen fluoride
US3101254A (en) Production of silica free hydrogen fluoride
US3140152A (en) Process for preparing and recovering of substantially anhydrous hydrogen fluoride gas from a dry alkali metal bifluoride
Andreev et al. Fluorination of beryllium concentrates with ammonium fluorides
US4363789A (en) Alumina production via aluminum chloride oxidation
CN110092353A (en) The method for fabricating anhydrous hydrogen fluoride with roasting in fluosilicic acid
US3157469A (en) Controlled process for producing alkali metal bifluoride and substantially anhydrous gaseous hydrogen fluoride
US3310369A (en) Process for producing anhydrous ammonium bifluoride from an aqueous solution of ammonium fluoride
CN104229836A (en) Acid-base co-production process and aid-base co-production system for preparing sodium carbonate and hydrochloric acid by utilizing sodium chloride
US2865711A (en) Process for the production of hydrogen fluoride
CN108455531A (en) The method for fabricating anhydrous hydrogen fluoride with roasting in fluosilicic acid
CN109502614A (en) A kind of large size spray drying prepares the method and device of anhydrous magnesium chloride

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
DD01 Delivery of document by public notice
DD01 Delivery of document by public notice

Addressee: Yao Dingwen

Document name: Notice of First Examination Opinion

DD01 Delivery of document by public notice
DD01 Delivery of document by public notice

Addressee: Yao Dingwen

Document name: Deemed withdrawal notice

WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20190806