US2007208A - Manufacture of halo-fluoro derivative of aliphatic hydrocarbons - Google Patents
Manufacture of halo-fluoro derivative of aliphatic hydrocarbons Download PDFInfo
- Publication number
- US2007208A US2007208A US517854A US51785431A US2007208A US 2007208 A US2007208 A US 2007208A US 517854 A US517854 A US 517854A US 51785431 A US51785431 A US 51785431A US 2007208 A US2007208 A US 2007208A
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- United States
- Prior art keywords
- halo
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- chlorine
- fluorine
- aliphatic hydrocarbons
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- 238000004519 manufacturing process Methods 0.000 title description 6
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 title description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 10
- 229910052801 chlorine Inorganic materials 0.000 description 10
- 239000000460 chlorine Substances 0.000 description 10
- 229910052731 fluorine Inorganic materials 0.000 description 10
- 239000011737 fluorine Substances 0.000 description 10
- 239000003795 chemical substances by application Substances 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 7
- RWRIWBAIICGTTQ-UHFFFAOYSA-N difluoromethane Chemical compound FCF RWRIWBAIICGTTQ-UHFFFAOYSA-N 0.000 description 7
- 125000005843 halogen group Chemical group 0.000 description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- 125000001153 fluoro group Chemical group F* 0.000 description 6
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000005660 chlorination reaction Methods 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- VMPVEPPRYRXYNP-UHFFFAOYSA-I antimony(5+);pentachloride Chemical compound Cl[Sb](Cl)(Cl)(Cl)Cl VMPVEPPRYRXYNP-UHFFFAOYSA-I 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 125000001309 chloro group Chemical group Cl* 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 238000006467 substitution reaction Methods 0.000 description 3
- GUNJVIDCYZYFGV-UHFFFAOYSA-K Antimony trifluoride Inorganic materials F[Sb](F)F GUNJVIDCYZYFGV-UHFFFAOYSA-K 0.000 description 2
- XWCDCDSDNJVCLO-UHFFFAOYSA-N Chlorofluoromethane Chemical compound FCCl XWCDCDSDNJVCLO-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- BHHYHSUAOQUXJK-UHFFFAOYSA-L zinc fluoride Chemical compound F[Zn]F BHHYHSUAOQUXJK-UHFFFAOYSA-L 0.000 description 2
- ODNBVEIAQAZNNM-UHFFFAOYSA-N 1-(6-chloroimidazo[1,2-b]pyridazin-3-yl)ethanone Chemical compound C1=CC(Cl)=NN2C(C(=O)C)=CN=C21 ODNBVEIAQAZNNM-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical class CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical class CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 1
- 150000001462 antimony Chemical class 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000012025 fluorinating agent Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 230000026030 halogenation Effects 0.000 description 1
- 238000005658 halogenation reaction Methods 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- YAFKGUAJYKXPDI-UHFFFAOYSA-J lead tetrafluoride Chemical compound F[Pb](F)(F)F YAFKGUAJYKXPDI-UHFFFAOYSA-J 0.000 description 1
- 229910001512 metal fluoride Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
- 229940029284 trichlorofluoromethane Drugs 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
- C07C17/20—Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms
- C07C17/202—Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms two or more compounds being involved in the reaction
- C07C17/208—Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms two or more compounds being involved in the reaction the other compound being MX
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
- C07C17/10—Preparation of halogenated hydrocarbons by replacement by halogens of hydrogen atoms
Definitions
- Our present invention differs from the former methods in that its objects are to fluorate an allphatic hydrocarbon derivative in which all the halogen atoms desired in the final product are not present before fluoration, and to add the missing halogen atoms, during or after fluoration.
- CC12F2 can be obtained, according to our present invention by fluorating dichloromethane, CHzCl-z to difluoromethane, CHzFz and by subsequently or at the same time chlorinating the CHzFz to dichlorodifiuoromethane CClzFz.
- the latter operation may be modified to form CHClFz or a mixture of CClzFz and CHClFa.
- a partial fluoration of CHzCl: to CHzCIF could be subsequently or simultaneously chlorinated toCHClzF and/or CChF.
- a fluorating' substance such as antimony trifluoride, SbF3, together with a catalytic agent, such as antimony pentachloride, SbCl5, are introduced into the autoclave 20 through the opening 2
- a hydrocarbon derivative such as dichloromethane, CHzClz, which, for convenience, is stored in the tanklZ, is introduce'd'into the autoclave 20 by means-of the pump 23.
- the reaction then proceeds and may, if desired, be promoted by warming the autoclave 20 with a steam jacket 24.
- One method of obtaining a good yield of CHzFz is to maintain the pressure at about 130 pounds gauge and the temperature at about F.
- the CH2F2 is then admitted into chamber 26 where it is chlorinated by chlorine fed through conduit 28.
- the chlorination in the reaction chamber 26 is promoted by the iron filings 21.
- the amounts of chlorine and difluorometh ane entering the reaction chamber 26 may be proportionally regulated by means of the valves 29 and 25 respectively.
- the reaction product CC12F2 is led through the conduit 30 into the washer 3
- the hologenation takes place after the fiuoration. It is possible, however, to vary the process to carry out both the fluoration and the halogenation simultaneously.
- the chlorine may be fed directly into the autoclave 20 and the reaction chamber 26 eliminated. In this manner both the fiuoration and chlorination will be carried out in the autoclave 20.
- both processes may be combined. That is, chlorine may be fed into both the reaction chamber 26 and into the autoclave 20 so as to start the chlorination during fluoration within the autoclave 20 and to bring it to completion in the chamber 26.
- SbFs has been named as the fluorating agent and SbCl5 as the catalytic agent
- other fiuorating agents such as lead fluoride and zinc fluoride may be used in place of antimony trifiuoride and other.
- catalytic agents such as Br, titaniumtetrachloride may be used in place oi. SbCls when an. antimony salt is present.
- the process comprising simultaneously reacting an aliphatic hydrocarbon derivative containing hydrogen and halogen other than fluorine with a fluorating agent and with chlorine, the amount of fluorinating agent being insufllcient to cause fluorine substitution on all of the carbon bonds, substituting one or more. fluorine atoms for the halogen atoms other than fluorine and simultaneously therewith substituting one or more chlorine atoms for one of more hydrogen atoms to thereby obtain a halo-fluoro derivative of an aliphatic hydrocarbon.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Description
y 1935- T. MIDGLEY, JR., ET AL 2,007,208
MANUFACTURE OF HALO-FLUORO DERIVATIVE OF ALIPHATIC HYDROCARBQNS Filed Feb. 24, 1951 IN VENT QR S AITORNEB Patented July 9, 1935 UNITED STATES PATENT oFncE I MANUFACTURE OF HALO-FLUORO DERIVA- TIVE OF ALIPHATIC HYDROCARBONS Thomas Midgley, Jr., Worthington, Albert L. Henne, Columbus, and Robert Reed McNary, Dayton, Ohio, assignors, by mesne assignments, to General Motors Corporation, a. corporation of Delaware Application February 24, 1931, Serial No. 517,854
5 Claims.
other than fluorine, which are desired in the final product are already present in the molecule before fluoration.
Our present invention differs from the former methods in that its objects are to fluorate an allphatic hydrocarbon derivative in which all the halogen atoms desired in the final product are not present before fluoration, and to add the missing halogen atoms, during or after fluoration.
As a specific example, CC12F2, can be obtained, according to our present invention by fluorating dichloromethane, CHzCl-z to difluoromethane, CHzFz and by subsequently or at the same time chlorinating the CHzFz to dichlorodifiuoromethane CClzFz. The latter operation may be modified to form CHClFz or a mixture of CClzFz and CHClFa. A partial fluoration of CHzCl: to CHzCIF could be subsequently or simultaneously chlorinated toCHClzF and/or CChF.
In carrying out this invention, an apparatus similar to that diagrammatically shown on the drawing may be used.
A fluorating' substance, such as antimony trifluoride, SbF3, together with a catalytic agent, such as antimony pentachloride, SbCl5, are introduced into the autoclave 20 through the opening 2|. After the autoclave 20 is closed, a hydrocarbon derivative, such as dichloromethane, CHzClz, which, for convenience, is stored in the tanklZ, is introduce'd'into the autoclave 20 by means-of the pump 23. The reaction then proceeds and may, if desired, be promoted by warming the autoclave 20 with a steam jacket 24. One method of obtaining a good yield of CHzFz is to maintain the pressure at about 130 pounds gauge and the temperature at about F. The CH2F2 is then admitted into chamber 26 where it is chlorinated by chlorine fed through conduit 28. The chlorination in the reaction chamber 26 is promoted by the iron filings 21. The amounts of chlorine and difluorometh ane entering the reaction chamber 26 may be proportionally regulated by means of the valves 29 and 25 respectively. The reaction product CC12F2 is led through the conduit 30 into the washer 3| containing a solution of sodium hydroxide indicated at 32. where HCl and any excess chlorine are removed. Thereafter the dichloro- 'difluoromethane may be compressed into and stored in the container 33 by means of the pump 34.
The above method of manufacture, and the steps involved therein are set forth in the following equation:
The above specific example has been set forth to illustrate the production of CClzFz. However it is possible to also produce a less fluorated substance in chamber 20, for example monochloromonofluoromethane by varying the pressure temperature conditions within this apparatus. In the reaction chamber 26 this monochloromonofluoromethane will be halogenated by the chlorine to produce dichloromonofiuoro or trichloromonofluoromethane according to the amount of chlorine introduced. The reactions involving the production and chlorination of monofluoro compound are as follows:
In the above description, the hologenation takes place after the fiuoration. It is possible, however, to vary the process to carry out both the fluoration and the halogenation simultaneously. For example, the chlorine may be fed directly into the autoclave 20 and the reaction chamber 26 eliminated. In this manner both the fiuoration and chlorination will be carried out in the autoclave 20. Or, if desired, both processes may be combined. That is, chlorine may be fed into both the reaction chamber 26 and into the autoclave 20 so as to start the chlorination during fluoration within the autoclave 20 and to bring it to completion in the chamber 26.
Derivatives of methane have been used for illustrative purposes but it is likewise possible to fluorate and subsequently or at the same time halogenate derivatives of the methane liomologs. Such fiuoro compounds include CHClFz. CClzFz, C2C12F4 illustrative of the ethane series and C3H3F2Bl3 illustrative of the propane series.
In the specific examples, SbFs has been named as the fluorating agent and SbCl5 as the catalytic agent, other fiuorating agents such as lead fluoride and zinc fluoride may be used in place of antimony trifiuoride and other. catalytic agents such as Br, titaniumtetrachloride may be used in place oi. SbCls when an. antimony salt is present.
What is claimed is as follows:
1. The process comprising simultaneously reacting an aliphatic hydrocarbon derivative containing hydrogen and halogen other than fluorine with a fluorating agent and with chlorine, the amount of fluorinating agent being insufllcient to cause fluorine substitution on all of the carbon bonds, substituting one or more. fluorine atoms for the halogen atoms other than fluorine and simultaneously therewith substituting one or more chlorine atoms for one of more hydrogen atoms to thereby obtain a halo-fluoro derivative of an aliphatic hydrocarbon.
2. The process which comprises simultaneously reacting the derivative of methane containing hydrogen atoms and halogen atoms other than fluorine with a metal fluoride and with chlorine, the amount of fluorating agen't being insumcient to cause fluorine substitution on all oi the carbon bonds, substituting one or more fluorine atoms for one or more of the halogen atoms other than fluorine and substituting simultaneously one or more chlorine atoms for one or more of the hydrogen atoms substantially as described to thereby form a halo-fluoro derivative of methane.
3. The process which comprises simultaneously reacting a derivative oi. methane containing hydrogen atoms and halogen atoms other than fluorine with a fluorating agent and with chlorine, the amount of fluorating agent being insuflicient to cause fluorine substitution on all 0! the carbon bonds, substituting one or more fluorine atoms for the halogen atoms other than fluorine and simultaneously therewith substituting one or more chlorine atoms for one or more hydrogen atoms to thereby form a halo-fluoro derivative of methane.
all of the carbon bonds, to obtain a halo-fluoro ll hydrocarbon derivative.
THOMAS MIDGLEY, Ja.
ALBERT L. HENNE. ROBERT REED McNARY.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US517854A US2007208A (en) | 1931-02-24 | 1931-02-24 | Manufacture of halo-fluoro derivative of aliphatic hydrocarbons |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US517854A US2007208A (en) | 1931-02-24 | 1931-02-24 | Manufacture of halo-fluoro derivative of aliphatic hydrocarbons |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2007208A true US2007208A (en) | 1935-07-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US517854A Expired - Lifetime US2007208A (en) | 1931-02-24 | 1931-02-24 | Manufacture of halo-fluoro derivative of aliphatic hydrocarbons |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2007208A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2439299A (en) * | 1946-07-26 | 1948-04-06 | Phillips Petroleum Co | Production of halogenated hydrocarbons containing fluorine |
| US2459767A (en) * | 1946-03-19 | 1949-01-18 | Allied Chem & Dye Corp | Manufacture of chlorofluoro methanes |
| US2566163A (en) * | 1946-03-19 | 1951-08-28 | Allied Chem & Dye Corp | Manufacture of tetrachlorodifluoroethane |
| US2673884A (en) * | 1951-12-06 | 1954-03-30 | Charles L Thomas | Production of fluoro-olefins |
| US2749375A (en) * | 1956-06-05 | Fluorination | ||
| US2749374A (en) * | 1950-02-24 | 1956-06-05 | Dow Chemical Co | Production of methylene fluoride |
| US2824900A (en) * | 1954-06-01 | 1958-02-25 | Montedison Spa | Process for the production of 1,1,1-trifluoro-2-chloroethane |
-
1931
- 1931-02-24 US US517854A patent/US2007208A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2749375A (en) * | 1956-06-05 | Fluorination | ||
| US2459767A (en) * | 1946-03-19 | 1949-01-18 | Allied Chem & Dye Corp | Manufacture of chlorofluoro methanes |
| US2566163A (en) * | 1946-03-19 | 1951-08-28 | Allied Chem & Dye Corp | Manufacture of tetrachlorodifluoroethane |
| US2439299A (en) * | 1946-07-26 | 1948-04-06 | Phillips Petroleum Co | Production of halogenated hydrocarbons containing fluorine |
| US2749374A (en) * | 1950-02-24 | 1956-06-05 | Dow Chemical Co | Production of methylene fluoride |
| US2673884A (en) * | 1951-12-06 | 1954-03-30 | Charles L Thomas | Production of fluoro-olefins |
| US2824900A (en) * | 1954-06-01 | 1958-02-25 | Montedison Spa | Process for the production of 1,1,1-trifluoro-2-chloroethane |
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