GB1413333A - Process for producing silica and hydrogen fluoride from waste gases containing silicon- and fluorine containing compounds - Google Patents
Process for producing silica and hydrogen fluoride from waste gases containing silicon- and fluorine containing compoundsInfo
- Publication number
- GB1413333A GB1413333A GB4970372A GB4970372A GB1413333A GB 1413333 A GB1413333 A GB 1413333A GB 4970372 A GB4970372 A GB 4970372A GB 4970372 A GB4970372 A GB 4970372A GB 1413333 A GB1413333 A GB 1413333A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sif
- water
- sulphuric acid
- sio
- acid
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/18—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
- C01B33/181—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by a dry process
- C01B33/183—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by a dry process by oxidation or hydrolysis in the vapour phase of silicon compounds such as halides, trichlorosilane, monosilane
- C01B33/184—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof by a dry process by oxidation or hydrolysis in the vapour phase of silicon compounds such as halides, trichlorosilane, monosilane by hydrolysis of tetrafluoride
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B7/00—Halogens; Halogen acids
- C01B7/19—Fluorine; Hydrogen fluoride
- C01B7/191—Hydrogen fluoride
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Silicon Compounds (AREA)
Abstract
1413333 Hydrogen fluoride and SiO 2 from waste gases G L FLEMMERT 27 Oct 1972 [28 Oct 1971] 49703/72 Heading C1A Pure HF and SiO 2 are produced from waste gas containing SiF 4 and HF and optionally SiO 2 , by absorbing the gas in water when hydrofluorosilicic acid is formed, which is then mixed with conc. sulphuric acid so as to be decomposed and form a gaseous effluent comprising SiF 4 + HF ; the residual sulphuric acid is withdrawn from the decomposition stage, and the gaseous effluent is treated with cone. sulphuric acid to absorb water and HF, the SiF 4 being recovered and hydrolysed by blending it with combustible gas and air and burning to form SiO 2 and HF, the temperature of the reaction being maintained above the dew point to prevent the water condensing on the silica, separating the silica, and treating the effluent gases with water or aqueous HE to form hydrofluorosilicic acid, venting the remaining gas, and then decomposing the hydrofluoro-silicic acid with sulphuric acid, so liberating gases containing SiF 4 , HF and water vapour, removing the water vapour and HF, recycling the SiF 4 to the hydrolysis stage, separating the HF and recovering the sulphuric acid. The hydrofluorosilicic acid produced from the initial waste gas and that produced after the SiF 4 hydrolysis stage may be combined and decomposed together. When SiO 2 is also present in the waste gases, then conditions may be such that the reaction with conc. sulphuric acid produces only water and SiF 4 . The proportion of HF to SiF 4 formed in the decomposition may be controlled by adjusting the molar proportions of SiF 4 and H 2 SiF 6 in the reaction mixture. Steam may be added to the combustion zone to improve the hydrolysis of the SiF 4 . Particular concentrations and conditions of the various reaction stages are given in the Specification.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US19346771A | 1971-10-28 | 1971-10-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1413333A true GB1413333A (en) | 1975-11-12 |
Family
ID=22713763
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4970372A Expired GB1413333A (en) | 1971-10-28 | 1972-10-27 | Process for producing silica and hydrogen fluoride from waste gases containing silicon- and fluorine containing compounds |
Country Status (8)
Country | Link |
---|---|
BE (1) | BE790472A (en) |
CA (1) | CA979179A (en) |
DE (1) | DE2251787C2 (en) |
FR (1) | FR2158314B1 (en) |
GB (1) | GB1413333A (en) |
IT (1) | IT975395B (en) |
NL (1) | NL170402C (en) |
SE (1) | SE396060B (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2300201A1 (en) * | 2006-11-15 | 2008-06-01 | Casals Cardona Industrial, S.A. | Method for cleaning waste gas containing methyl mercaptan, solid particles and silicon tetrafluoride for obtaining concentrated fluosilicic acid, involves passing waste gases through wash-venturi and cyclone |
CN107601434A (en) * | 2017-11-07 | 2018-01-19 | 衢州市鼎盛化工科技有限公司 | A kind of method and apparatus that hydrogen fluoride is prepared by fluosilicic acid |
CN108816029A (en) * | 2018-08-02 | 2018-11-16 | 浙江中宁硅业有限公司 | A kind of method and its processing equipment using low concentration HF acid processing silicon tetrafluoride gas |
CN114988920A (en) * | 2022-04-20 | 2022-09-02 | 贵州新东浩化工材料科技有限公司 | Method for utilizing fluorine and silicon resources in phosphate ore in grading manner |
US11891344B2 (en) | 2022-04-20 | 2024-02-06 | Chtem Limited | Methods for graded utilization of fluorine and silicon resources in phosphate ores |
CN117509548A (en) * | 2023-12-04 | 2024-02-06 | 云南氟磷电子科技有限公司 | Method for preparing hydrofluoric acid and co-producing white carbon black by fluosilicic acid |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3206766A1 (en) * | 1982-02-25 | 1983-09-01 | Siemens AG, 1000 Berlin und 8000 München | METHOD FOR PRODUCING SILICON USED FOR SOLAR CELLS |
CN112551531A (en) * | 2020-11-24 | 2021-03-26 | 浙江巨化技术中心有限公司 | Method for coproducing hydrogen fluoride, white carbon black and potassium sulfate |
CN114920202B (en) * | 2022-05-31 | 2023-06-06 | 江西天行化工有限责任公司 | Preparation method of hydrogen fluoride |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2819151A (en) * | 1954-03-02 | 1958-01-07 | Flemmert Gosta Lennart | Process for burning silicon fluorides to form silica |
US2833628A (en) * | 1954-06-09 | 1958-05-06 | Grace W R & Co | Manufacture of silicon tetrafluoride |
NL139012B (en) * | 1961-10-02 | 1973-06-15 | Stauffer Chemical Co | PROCEDURE FOR THE WINNING OF THE FLUOR IN THE FORM OF CONCENTRATED HYDROGEN FLUORIDE. |
-
0
- BE BE790472D patent/BE790472A/en not_active IP Right Cessation
-
1972
- 1972-09-27 CA CA152,675A patent/CA979179A/en not_active Expired
- 1972-10-21 DE DE19722251787 patent/DE2251787C2/en not_active Expired
- 1972-10-23 SE SE1363572A patent/SE396060B/en unknown
- 1972-10-26 NL NL7214517A patent/NL170402C/en not_active IP Right Cessation
- 1972-10-27 GB GB4970372A patent/GB1413333A/en not_active Expired
- 1972-10-27 FR FR7238217A patent/FR2158314B1/fr not_active Expired
- 1972-10-27 IT IT7039572A patent/IT975395B/en active
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2300201A1 (en) * | 2006-11-15 | 2008-06-01 | Casals Cardona Industrial, S.A. | Method for cleaning waste gas containing methyl mercaptan, solid particles and silicon tetrafluoride for obtaining concentrated fluosilicic acid, involves passing waste gases through wash-venturi and cyclone |
CN107601434A (en) * | 2017-11-07 | 2018-01-19 | 衢州市鼎盛化工科技有限公司 | A kind of method and apparatus that hydrogen fluoride is prepared by fluosilicic acid |
CN108816029A (en) * | 2018-08-02 | 2018-11-16 | 浙江中宁硅业有限公司 | A kind of method and its processing equipment using low concentration HF acid processing silicon tetrafluoride gas |
CN108816029B (en) * | 2018-08-02 | 2023-10-13 | 浙江中宁硅业有限公司 | Method for treating silicon tetrafluoride gas by using low-concentration HF acid and treatment equipment thereof |
CN114988920A (en) * | 2022-04-20 | 2022-09-02 | 贵州新东浩化工材料科技有限公司 | Method for utilizing fluorine and silicon resources in phosphate ore in grading manner |
US11891344B2 (en) | 2022-04-20 | 2024-02-06 | Chtem Limited | Methods for graded utilization of fluorine and silicon resources in phosphate ores |
CN117509548A (en) * | 2023-12-04 | 2024-02-06 | 云南氟磷电子科技有限公司 | Method for preparing hydrofluoric acid and co-producing white carbon black by fluosilicic acid |
Also Published As
Publication number | Publication date |
---|---|
IT975395B (en) | 1974-07-20 |
BE790472A (en) | 1973-02-15 |
NL170402C (en) | 1982-11-01 |
CA979179A (en) | 1975-12-09 |
NL7214517A (en) | 1973-05-02 |
FR2158314B1 (en) | 1977-12-23 |
SE396060B (en) | 1977-09-05 |
DE2251787C2 (en) | 1982-08-26 |
DE2251787A1 (en) | 1973-05-10 |
NL170402B (en) | 1982-06-01 |
FR2158314A1 (en) | 1973-06-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PE20 | Patent expired after termination of 20 years |