WO1998027006A1 - Procede ameliore et intermediaires de production de fluor actif - Google Patents
Procede ameliore et intermediaires de production de fluor actif Download PDFInfo
- Publication number
- WO1998027006A1 WO1998027006A1 PCT/GB1997/003348 GB9703348W WO9827006A1 WO 1998027006 A1 WO1998027006 A1 WO 1998027006A1 GB 9703348 W GB9703348 W GB 9703348W WO 9827006 A1 WO9827006 A1 WO 9827006A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- alkali metal
- active fluorine
- fluorine
- reaction
- fluorohalate
- 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.)
- Ceased
Links
Classifications
-
- 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
- C01B7/24—Inter-halogen compounds
-
- 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
- C01B7/20—Fluorine
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/02—Inorganic compounds
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D2111/00—Cleaning compositions characterised by the objects to be cleaned; Cleaning compositions characterised by non-standard cleaning or washing processes
- C11D2111/10—Objects to be cleaned
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K3/00—Apparatus or processes for manufacturing printed circuits
- H05K3/22—Secondary treatment of printed circuits
- H05K3/26—Cleaning or polishing of the conductive pattern
Definitions
- This invention relates to the production of active fluorine through an intermediate, such as alkali metal tetrafluorohalate, and to improvements in the production of those intermediates .
- Alkali metal tetrafluorohalates are relatively stable materials which we have now established provide a convenient source of active fluorine.
- Active fluorine sources have many uses such as specialised fluorinating agents and as a high performance cleaning agents due to their extremely reactive nature. They may also be used as a dry cleaning agent in the electronics industry. However, conventionally used sources of active fluorine in their form ready for use are highly dangerous substances .
- the active fluorine produced from the source may be or include F, F 2 , C1F, C1F 3 , ClF 5 , IF 5 , IF 7 , BrF, BrF 3 , BrF 5 or mixtures thereof .
- the gases produced may further include Cl 2 , Cl , I, I 2 , Br, Br 2 or mixtures thereof.
- Active fluorine consists of highly energetic fluorine species.
- a method for producing alkali metal fluorohalate comprising the direct fluorination of one or more alkali metal halides.
- Preferably only one alkali metal halide is employed.
- Preferably a potassium form is used.
- the halate is preferably provided in the chlorate form, although the iodate or bromate forms may be used.
- KCl is a preferred starting material, most preferably according to the reaction : -
- the reaction is carried out at temperatures in the range of 15 to 250°C and most preferably 90 to 250°C.
- the reaction temperature, and preferably the maximium reaction temperature may be between 190 to 325 °C, and more preferably may be between 220 and 270°C.
- the reaction is preferably carried out in a vacuum system which excludes air and moisture.
- vacuum system is meant a high pressure system capable of being evacuated to remove moisture and/or air.
- the fluorine may be provided at elevated pressure.
- at least the inital, fluorine pressure is between 1 and 10 atm, and more preferably between 2.5 and 5 atm.
- the reaction is preferably carried out for a time period of at least 60 minutes, and more preferably a time period of between 80 and 400 minutes.
- the fluorine may be scrubbed with sodium fluoride prior to the reaction to remove HF .
- a cold trap for instance at less than -70°C, may be employed. The complete removal of HF from the fluorine is desirable .
- the intermediate may be formed as a transitional state in the production of active fluorine or as an intermediate form for transportation and/or storage, preferably prior to conversion to active fluorine.
- the reaction products may be purified prior to storage.
- the alkali metal tetrafluorohalate is preferably provided in pellet form.
- the alkali metal tetrafluorohalate may be RbClF 4 or CsClF 4 or any other suitable alkali metal.
- the form may be used as a solid suitable for transportation.
- KCIF 4 is particularly preferred.
- the active fluorine is produced from the alkali metal tetrafluorohalate by thermal decomposition.
- the active fluorine may be or include one or more of XF n , where X is Cl, Br or I , and n is 1, 3, 5 or 7.
- alkali metal flurohalate preferably tetrafluorohalate
- active fluorine produced from alkali metal fluorohalate, preferably tetrafluorohalate, produced according to the method of the first aspect.
- the use of the active fluorine sources may be in cleaning or etching semi-conductor materials or apparatus or equipment involved in their production and processing.
- alkali metal fluorohalate preferably tetrafluorohalate, produced according to the first aspect of the invention, as a transportable and/or storable source of active fluorine.
- the fluorination is carried out at between 15-300°C and yields a dense melt. Temperatures of 90-200°C are appropriate to the potassium and caesium forms. The exclusion of water from the reaction vessel is important for obtaining the correct products .
- a nickel reaction vessel was charged with KCl (0.31g, 0.0042mols) at room temperature. Still at room temperature, the vessel was charged with F 2 (2.86atm, 0.012mol) giving rise to an exothermic reaction almost instantly.
- the system was then heated to a maximium of 263°C over a period of 90 minutes, before being allowed to cool.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Technique améliorée de production de fluor actif au moyen de la production d'un intermédiaire sous forme de fluorohalate de métal alcalin. On prépare cet intermédiaire par fluoration directe d'un chlorure de métal alcalin. Cette technique présente des avantages en ce qui concerne les coûts et la facilité de production de l'intermédiaire et des produits finis et permet également de simplifier le transport des matériaux.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU77379/98A AU7737998A (en) | 1996-12-19 | 1997-12-16 | Process for the production of active fluorine and intermediates invol ved in active fluorine production and use of this active fluorine |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB9626318.1A GB9626318D0 (en) | 1996-12-19 | 1996-12-19 | Improvements in and relating to the production of active fluorine |
| GB9626318.1 | 1996-12-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1998027006A1 true WO1998027006A1 (fr) | 1998-06-25 |
Family
ID=10804656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/GB1997/003348 Ceased WO1998027006A1 (fr) | 1996-12-19 | 1997-12-16 | Procede ameliore et intermediaires de production de fluor actif |
Country Status (4)
| Country | Link |
|---|---|
| AU (1) | AU7737998A (fr) |
| GB (1) | GB9626318D0 (fr) |
| WO (1) | WO1998027006A1 (fr) |
| ZA (1) | ZA9711442B (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2012016997A1 (fr) * | 2010-08-05 | 2012-02-09 | Solvay Sa | Procédé de purification du fluor |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3143391A (en) * | 1959-10-12 | 1964-08-04 | Olin Mathieson | Alkali metal tetrafluorochlorates and their preparation |
| US3361543A (en) * | 1963-04-01 | 1968-01-02 | Monsanto Res Corp | Synthesis of alkali metal tetrafluorochlorates |
| US3989808A (en) * | 1975-07-28 | 1976-11-02 | The United States Of America As Represented By The United States Energy Research And Development Administration | Method of preparing pure fluorine gas |
| US4284617A (en) * | 1979-11-30 | 1981-08-18 | The United States Of America As Represented By The Secretary Of The Navy | Solid compositions for generation fluorine and gaseous fluorine compounds |
-
1996
- 1996-12-19 GB GBGB9626318.1A patent/GB9626318D0/en active Pending
-
1997
- 1997-12-16 WO PCT/GB1997/003348 patent/WO1998027006A1/fr not_active Ceased
- 1997-12-16 AU AU77379/98A patent/AU7737998A/en not_active Abandoned
- 1997-12-19 ZA ZA9711442A patent/ZA9711442B/xx unknown
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3143391A (en) * | 1959-10-12 | 1964-08-04 | Olin Mathieson | Alkali metal tetrafluorochlorates and their preparation |
| US3361543A (en) * | 1963-04-01 | 1968-01-02 | Monsanto Res Corp | Synthesis of alkali metal tetrafluorochlorates |
| US3989808A (en) * | 1975-07-28 | 1976-11-02 | The United States Of America As Represented By The United States Energy Research And Development Administration | Method of preparing pure fluorine gas |
| US4284617A (en) * | 1979-11-30 | 1981-08-18 | The United States Of America As Represented By The Secretary Of The Navy | Solid compositions for generation fluorine and gaseous fluorine compounds |
Non-Patent Citations (2)
| Title |
|---|
| CHEMICAL ABSTRACTS, vol. 85, no. 12, 20 September 1976, Columbus, Ohio, US; abstract no. 80474, FOGLE, C. E. ET AL: "Solid reactants for fluorine gas generators" XP002062746 * |
| U. S. NTIS, AD REP. (1976), AD-A022099, 112 PP. AVAIL.: NTIS FROM: GOV. REP. ANNOUNCE. INDEX (U. S.) 1976, 76(10), 211 CODEN: XADRCH, 1976 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2012016997A1 (fr) * | 2010-08-05 | 2012-02-09 | Solvay Sa | Procédé de purification du fluor |
| US8821821B2 (en) | 2010-08-05 | 2014-09-02 | Solvay Sa | Method for the purification of fluorine |
Also Published As
| Publication number | Publication date |
|---|---|
| ZA9711442B (en) | 1999-06-21 |
| AU7737998A (en) | 1998-07-15 |
| GB9626318D0 (en) | 1997-02-05 |
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