US2283142A - Isomerization of normal butane - Google Patents
Isomerization of normal butane Download PDFInfo
- Publication number
- US2283142A US2283142A US103383A US10338336A US2283142A US 2283142 A US2283142 A US 2283142A US 103383 A US103383 A US 103383A US 10338336 A US10338336 A US 10338336A US 2283142 A US2283142 A US 2283142A
- Authority
- US
- United States
- Prior art keywords
- normal butane
- butane
- normal
- hydrogen
- isomerization
- 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 - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2767—Changing the number of side-chains
- C07C5/277—Catalytic processes
- C07C5/2778—Catalytic processes with inorganic acids; with salts or anhydrides of acids
- C07C5/2786—Acids of halogen; Salts thereof
- C07C5/2789—Metal halides; Complexes thereof with organic compounds
Definitions
- This invention relates particularly to the treatment of butane of normal or straight-chain structure.
- the invention is con-, cerned with a process whereby normal butane is converted into iso-butane, the process involving the use of special catalysts and particular conditions of operation which favor the isomerization reactions so that relatively high yields of the isocompound are produced.
- butanes' Butanes are produced in considerable quantifor the production of gasoline. In the case of cracked gas mixtures the relative proportions of iso and normal butanes vary, but the ratio of the iso to the normal compound is as a rule considerably higher than in natural gas.
- Butanes may be considered as more or less marginal compounds in respect to their desirability in ordinary gasoline, that is, a certain percentage of them is essential for sufficient vapor pressure to insure ease in starting, while an excess tends to produce vapor look. For these reasons the total percentage of 4-carbon atom hydrocarbons is commonly adjusted in coniunction with the boiling range andvapor pressure of the other gasoline compounds to produce a gasoline of desirable starting characteristics according to seasonal demands.
- butanes at the present time bear a further important relationship to oil refining in that their excess production is being utilized as a source of gasoline either by ordinary thermal cracking or by special catalytic dehydrogenation processes followed by polymerization in which catalysts may or may not be used. Investigations have shown that iso-butane is considerably more amenable to cracking and dehydrogenation, both with and without catalysts, than the normal compound.
- the normal butenes are considerablyv more difficult topolymerize, either thermally or catalytically, than iso-butene, and it is found also that the octenes representing the dimers of the lsobutene are of higher antiknock value than those from n-butenes which holds also for the octenes produced by hydrogenation. It is, therefore, of considerable importance at the present time to convert as much as possible of the normal butane production into iso-butane,
- catalysts which may be employed in accomplishing the present 50 isomerization' reaction and, while they may be used more or less interchangeably, some are more effective than others and it is not intended to infer that they are equivalent.
- compounds which may be employed may be men tioned aluminum chloride, zinc chloride, iro
- the catalysts comchloride, zirconium chloride, stannic chloride and boron fluoride.
- a hydrogen halide is present in the reactions along with these" compounds.
- Some of the compounds may be employed either in the dry state or in aqueous solution with suitable modifications of operating conditions.
- the hydrogen halides such as for example hydrogen chloride or hydrofluoric acid, being separately introduced in the gaseous state.
- the process may be operated under batch or continuous conditions. Choosing aluminum chloride and hydrogen chloride as example of jointly ,used catalytic materials, batch operations may be conducted by separately adding aluminum chloride, hydrogen chloride and normal butane to a closed pressure container, after which the container is agitated or the contents stirred mechanically while the temperature and pressure are raised by the application of external heat to produce a temperature corresponding to maximum production of the iso-compound. This type of operation is better adapted to small scale production, and plants of considerable capacity are best operated in a continuous manner.
- butan'e may be pumped through a tubular heating element at a given temperature and pressure within the approximate ranges previously specified and reaction brought about along the line of flow by the separate or joint injection of proportioned amounts
- Example I 100 parts by weight of normal butane, 20 parts by weight of aluminum chloride and 2 parts by weight of hydrogen, chloride were introduced under a pressure of about flve atmospheres into a pressure vessel, which was then rotated and heated tor twelve hours at an average temperature of 150 C., the maximum pressure developed being about 30 atmospheres. After the bomb was cooled the hydrocarbons were released and fractionated and it was found that they consisted of 66.5% of iso-butane and 31.9% of normal butane.
- Continuous operations may also be conducted by passing normal butane mixed with a hydrogen halide through beds of heated, granular catalyst, which may comprise any of the solid salts mentioned, either alone or mixed with carrying or spacing materials of a relatively inert character.
- heated, granular catalyst which may comprise any of the solid salts mentioned, either alone or mixed with carrying or spacing materials of a relatively inert character.
- This type of operation is readily utilizable in the case of such compounds as zinc chloride, iron chloride and stannic chloride.
- Treatment of the products in these cases will involve merely the condensation'of the hydrocarbon products and the recycling of the hydrogen halides for further
- the following examples are introduced to indicate in a general way the nature ofthe results obtainable by the use of the process, though they are not introduced with the intention of correspondingly limiting the scope of the invention.
- Example III In this case the catalyst employed was a composite consisting of about 50 parts by weight of ground pumice and 50 parts by weight of substantially anhydrous zinc chloride, terial was placed in a vertical cylindrical reaction chamber which was insulated to conserve heat and the normal butane was preheated to a temperature or approximately 200 C. and passed downwardly through the contact mass under a a pressure of approximately 30 atmospheres. Approximately iso-butane and 30% normal butane were found in the reaction products, the remaining 10% comprising lighter fixed gases and other reaction products.
- Example IV The catalytic materials employed in this case consisted of boron fluoride and hydrogen fluoride.
- Normal butane was preheated to a temperature of approximately 180 C. and passed into an insulated reaction chamber at the same time as boron fluoride and hydrogen fluoride were injected.
- the reaction chamber was nickel-lined, as this was found to further accelerate the isomerization reactions.
- a process for producing isobutane which comprises subjecting normal butane, in the substantial absence of polymerizable olefins, to the action of a metallic halide catalyst of the Friedel-Crafts type and a relatively small amount of a hydrogen halide at temperatures of the order of about 150 to 200 C. and under pressures of the order of about 10 to 50 atmospheres, whereby to efiect isomerization of normal butane into isobutane as the principal reaction in the process.
- a process for producing isobutane which comprises passing normal butane and a hydrogen halide through a reaction zone maintained under 30 isomerizing conditions and containing a metallic halide catalyst of the Friedel-Crafts type, said conditions and the amount of said hydrogen halide being such that isomerization of normal butane constitutes the principal reaction in the process.
- a process for producing isobutane from normal butane which comprises adding a gaseous hydrogen halide to the normal butane, and passing the resultant mixture under isomerizing conditions through .a bed of solid carrier material containing a metallic halide catalyst of the Friedel-Crafts type, said conditions and the amount of said hydrogen halide being-such that isomerization of normal butane constitutes the principal reaction in the process.
- a process for producing isobutane from normal butane which comprises adding a substantially anhydrous hydrogen halide to normal butane, and contacting the resultant mixture under isomerizing conditions with a substantially an hydrous metallic halide catalyst of the Friedel- Crafts type supported on a solid carrier material, said conditions and the amount of said hydrogen halide being such that isomerization of normal butane constitutes the principal reaction in the process.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
Patented May 12, 1942 UNITED STATES ISOMERIZ QTION OF NORMAL BUTANE Vladimir Ipatiefi? and Herman Pines, Chicago, 111., assignors to Universal Oil Products Company, Chicago, lll., a corporation of Delaware No Drawing. Application September 30, 1936,
- Serial No. 103,383
11 Claims.
This invention relates particularly to the treatment of butane of normal or straight-chain structure.
In amore specific sense, the invention is con-, cerned with a process whereby normal butane is converted into iso-butane, the process involving the use of special catalysts and particular conditions of operation which favor the isomerization reactions so that relatively high yields of the isocompound are produced.
Since the invention is concerned principally with thetwo 4-carbon atom paraflln hydrocarbons and their transformation, one into the other, the following table is introduced to indicate the structure and the principal physical characteristics of these two compounds:
Properties. of butanes' Butanes are produced in considerable quantifor the production of gasoline. In the case of cracked gas mixtures the relative proportions of iso and normal butanes vary, but the ratio of the iso to the normal compound is as a rule considerably higher than in natural gas.
Butanes may be considered as more or less marginal compounds in respect to their desirability in ordinary gasoline, that is, a certain percentage of them is essential for sufficient vapor pressure to insure ease in starting, while an excess tends to produce vapor look. For these reasons the total percentage of 4-carbon atom hydrocarbons is commonly adjusted in coniunction with the boiling range andvapor pressure of the other gasoline compounds to produce a gasoline of desirable starting characteristics according to seasonal demands.
The butanes at the present time bear a further important relationship to oil refining in that their excess production is being utilized as a source of gasoline either by ordinary thermal cracking or by special catalytic dehydrogenation processes followed by polymerization in which catalysts may or may not be used. Investigations have shown that iso-butane is considerably more amenable to cracking and dehydrogenation, both with and without catalysts, than the normal compound. Considering the corresponding monooleflins, the normal butenes are considerablyv more difficult topolymerize, either thermally or catalytically, than iso-butene, and it is found also that the octenes representing the dimers of the lsobutene are of higher antiknock value than those from n-butenes which holds also for the octenes produced by hydrogenation. It is, therefore, of considerable importance at the present time to convert as much as possible of the normal butane production into iso-butane,
prise essentially heavy metal chlorides and hydrogen halides.
We have determined that by the use of the class of catalysts mentioned, and particularly by the convenient use of considerable superatmos- I pheric pressure normal 'butane'may be converted into iso-butane with a yield of as high'as 60% to 65%. Evidently the use of super atmospheric pressures of the order of 10 to 5Datmospheres at temperatures of 150 C. and higher, besides depressing the volatilization of granular catalysts tends also to depress numerous undesirable side reactions which would result in the formation of hydrogen and low moleular weight hydrocarbons, so that the reaction proceeds more or less in one direction until an equilibrium is established. There are several alternative catalysts which may be employed in accomplishing the present 50 isomerization' reaction and, while they may be used more or less interchangeably, some are more effective than others and it is not intended to infer that they are equivalent. Among the compounds which may be employed may be men tioned aluminum chloride, zinc chloride, iro
In a preferred embodiment the catalysts comchloride, zirconium chloride, stannic chloride and boron fluoride. Experiments have indicated that best results are obtained when a minor percentage of a hydrogen halide is present in the reactions along with these" compounds. Some of the compounds may be employed either in the dry state or in aqueous solution with suitable modifications of operating conditions. In the case of such compounds as aluminum chloride, which readily sublimes, stannic chloride, which boils-at 114 C., and boron fluoride, which is normally gaseous, these are most conveniently employed in the anhydrous condition, the hydrogen halides, such as for example hydrogen chloride or hydrofluoric acid, being separately introduced in the gaseous state. There will be somevariations in the relative amounts of metal salts and hydrogen halides used at optimum treating conditions, but the determination of the best ratios is somewhat a matter of experiment.
The process may be operated under batch or continuous conditions. Choosing aluminum chloride and hydrogen chloride as example of jointly ,used catalytic materials, batch operations may be conducted by separately adding aluminum chloride, hydrogen chloride and normal butane to a closed pressure container, after which the container is agitated or the contents stirred mechanically while the temperature and pressure are raised by the application of external heat to produce a temperature corresponding to maximum production of the iso-compound. This type of operation is better adapted to small scale production, and plants of considerable capacity are best operated in a continuous manner. In continuous operation the butan'e may be pumped through a tubular heating element at a given temperature and pressure within the approximate ranges previously specified and reaction brought about along the line of flow by the separate or joint injection of proportioned amounts Example I 100 parts by weight of normal butane, 20 parts by weight of aluminum chloride and 2 parts by weight of hydrogen, chloride were introduced under a pressure of about flve atmospheres into a pressure vessel, which was then rotated and heated tor twelve hours at an average temperature of 150 C., the maximum pressure developed being about 30 atmospheres. After the bomb was cooled the hydrocarbons were released and fractionated and it was found that they consisted of 66.5% of iso-butane and 31.9% of normal butane. This indicates that the equilibrium unof metal salts and hydrogen halides, the'best example of this type of operation being the combinationof aluminum chloride and hydrogen chloride or boron fluoride and hydrogen fluoride. In the absence of moisture there will be substantially no corrosion when using these substances. After passage. through the heating element the reactants may be passed to enlarged insulated chambers for the completion of the desired isomerization and the total products subsequently fractionated to recover catalysts and separate the normal and iso-butanes, after which the normal compound may be recycled for further treat- ,ment.
Continuous operations may also be conducted by passing normal butane mixed with a hydrogen halide through beds of heated, granular catalyst, which may comprise any of the solid salts mentioned, either alone or mixed with carrying or spacing materials of a relatively inert character. This type of operation is readily utilizable in the case of such compounds as zinc chloride, iron chloride and stannic chloride. Treatment of the products in these cases will involve merely the condensation'of the hydrocarbon products and the recycling of the hydrogen halides for further The following examples are introduced to indicate in a general way the nature ofthe results obtainable by the use of the process, though they are not introduced with the intention of correspondingly limiting the scope of the invention.
der these conditions is considerabl in favor of iso-butane.
Example.
In this operation normal butane was passed through a tubular heating element and then into an enlarged reaction chamber, into which sublimed aluminum chloride and hydrogen chloride gas were introduced. A pressure of about 25 to SO atmOspheres and a temperature of 160 C. were maintained on. the reaction vessel, after which the reaction products were separatedand it was ifound that the hydrocarbons consisted of about 63% iso-butane and 32% normal butane. This indicates a selective conversion of the normal butane into iso-butane under these conditions.
Example III In this case the catalyst employed was a composite consisting of about 50 parts by weight of ground pumice and 50 parts by weight of substantially anhydrous zinc chloride, terial was placed in a vertical cylindrical reaction chamber which was insulated to conserve heat and the normal butane was preheated to a temperature or approximately 200 C. and passed downwardly through the contact mass under a a pressure of approximately 30 atmospheres. Approximately iso-butane and 30% normal butane were found in the reaction products, the remaining 10% comprising lighter fixed gases and other reaction products.
Example IV The catalytic materials employed in this case consisted of boron fluoride and hydrogen fluoride.
Normal butane was preheated to a temperature of approximately 180 C. and passed into an insulated reaction chamber at the same time as boron fluoride and hydrogen fluoride were injected. The reaction chamber was nickel-lined, as this was found to further accelerate the isomerization reactions. An analysis of the hydrocarbon products'showed that they consisted of approximately 62% by weight of iso-butane and 32% by weight of normal butane, the remaining products being lighter gases and some heavier polymerized products.
Thisma'-.
merizatlon or normal butane constitutes the principal reaction in the process, whereby to convert a major portion of the normal butane into isobutane.
2. A process for producing isobutane which comprises subjecting normal butane, in the substantial absence of polymerizable olefins, to the action of a metallic halide catalyst of the Friedel-Crafts type and a relatively small amount of a hydrogen halide at temperatures of the order of about 150 to 200 C. and under pressures of the order of about 10 to 50 atmospheres, whereby to efiect isomerization of normal butane into isobutane as the principal reaction in the process.
3. The process as described in claim 1 further 1 characterized'in that said catalyst comprises zirconium chloride.
4. The process as described in claim 1 further characterized in that said catalyst comprises zinc chloride.
5. .A process for producing isobutane which comprises subjecting normal butane to the action of a metallic halide catalyst of the Friedel- Crafts type under conditions and in the presence of an amount of a hydrogen halide such that 2 isomerization of normal butane constitutes the principal reaction in the process.
6. A process for producing isobutane which comprises passing normal butane and a hydrogen halide through a reaction zone maintained under 30 isomerizing conditions and containing a metallic halide catalyst of the Friedel-Crafts type, said conditions and the amount of said hydrogen halide being such that isomerization of normal butane constitutes the principal reaction in the process. I
'7. A process for producing isobutane from normal butane which comprises adding a gaseous hydrogen halide to the normal butane, and passing the resultant mixture under isomerizing conditions through .a bed of solid carrier material containing a metallic halide catalyst of the Friedel-Crafts type, said conditions and the amount of said hydrogen halide being-such that isomerization of normal butane constitutes the principal reaction in the process.
8. A process for producing isobutane from normal butane which comprises adding a substantially anhydrous hydrogen halide to normal butane, and contacting the resultant mixture under isomerizing conditions with a substantially an hydrous metallic halide catalyst of the Friedel- Crafts type supported on a solid carrier material, said conditions and the amount of said hydrogen halide being such that isomerization of normal butane constitutes the principal reaction in the process.
9. The process as defined in claim 5 further characterized in that the hydrogen halide and the metallic halide are substantially anhydrous.
10. The process as defined in claim 5 further charactertized in that the metallic halide catalyst comprises zinc chloride.
11. The process as defined in claim '7 further characterized in that the metallic halide catalyst comprises zinc chloride.
. VLADIMIR IPATIEFF'.
HERMAN PINES.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US103383A US2283142A (en) | 1936-09-30 | 1936-09-30 | Isomerization of normal butane |
| US434904A US2318226A (en) | 1936-09-30 | 1942-03-16 | Production of isobutane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US103383A US2283142A (en) | 1936-09-30 | 1936-09-30 | Isomerization of normal butane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2283142A true US2283142A (en) | 1942-05-12 |
Family
ID=22294897
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US103383A Expired - Lifetime US2283142A (en) | 1936-09-30 | 1936-09-30 | Isomerization of normal butane |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2283142A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2423045A (en) * | 1943-09-04 | 1947-06-24 | Kellogg M W Co | Liquid phase catalytic reactions of hydrocarbons |
| US2433020A (en) * | 1944-08-14 | 1947-12-23 | Standard Oil Co | Catalytic alkylation of aromatic hydrocarbons by paraffins |
| US2461540A (en) * | 1942-10-05 | 1949-02-15 | Phillips Petroleum Co | Process for the isomerization of a low-boiling saturated hydrocarbon |
| US2461541A (en) * | 1943-11-23 | 1949-02-15 | Phillips Petroleum Co | Process for isomerizing a low-boiling isomerizable saturated hydrocarbon |
| US2470144A (en) * | 1942-04-10 | 1949-05-17 | Texas Co | Isomerization and alkylation of normal paraffins |
| US2486368A (en) * | 1943-11-23 | 1949-10-25 | Phillips Petroleum Co | Hf-bf3-h2o isomerization catalyst |
| US2504280A (en) * | 1943-04-30 | 1950-04-18 | Standard Oil Co | Isomerization of light hydrocarbons |
-
1936
- 1936-09-30 US US103383A patent/US2283142A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2470144A (en) * | 1942-04-10 | 1949-05-17 | Texas Co | Isomerization and alkylation of normal paraffins |
| US2461540A (en) * | 1942-10-05 | 1949-02-15 | Phillips Petroleum Co | Process for the isomerization of a low-boiling saturated hydrocarbon |
| US2504280A (en) * | 1943-04-30 | 1950-04-18 | Standard Oil Co | Isomerization of light hydrocarbons |
| US2423045A (en) * | 1943-09-04 | 1947-06-24 | Kellogg M W Co | Liquid phase catalytic reactions of hydrocarbons |
| US2461541A (en) * | 1943-11-23 | 1949-02-15 | Phillips Petroleum Co | Process for isomerizing a low-boiling isomerizable saturated hydrocarbon |
| US2486368A (en) * | 1943-11-23 | 1949-10-25 | Phillips Petroleum Co | Hf-bf3-h2o isomerization catalyst |
| US2433020A (en) * | 1944-08-14 | 1947-12-23 | Standard Oil Co | Catalytic alkylation of aromatic hydrocarbons by paraffins |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2423045A (en) | Liquid phase catalytic reactions of hydrocarbons | |
| US2217252A (en) | Process for isomerization of olefin hydrocarbons | |
| US3773845A (en) | Catalytic conversion of saturated hydrocarbons to higher and lower molecular weight hydrocarbons | |
| US1973662A (en) | Process for reacting olefins with carbon monoxide | |
| US2283142A (en) | Isomerization of normal butane | |
| US2325122A (en) | Treatment of butane | |
| US2318226A (en) | Production of isobutane | |
| US2002394A (en) | Process for converting hydrocarbons | |
| US2169494A (en) | Treatment of butane | |
| US2318225A (en) | Production of isobutane | |
| US2278934A (en) | Process and catalyst for conversion of normal paraffins | |
| US1667214A (en) | Condensation product from olefines and hydrocarbons of the naphthalene series and process of making the same | |
| US2283143A (en) | Isomerization of normal butane | |
| US2476416A (en) | Isomerization of paraffin hydrocarbons by contact with catalyst comprising aluminum chloride and ferric chloride | |
| US2407813A (en) | Process for manufacture of supported catalysts | |
| US3446868A (en) | Disproportionation of propane | |
| US2347266A (en) | Isomerization of paraffinic hydrocarbons | |
| US2346768A (en) | Catalytic isomerization | |
| US2342073A (en) | Isomerizing hydrocarbons | |
| US2392924A (en) | Production of isobutane | |
| US2394898A (en) | Isomerizing hydrocarbons | |
| US2428455A (en) | Isomerization of olefins | |
| US2156718A (en) | Polymerization of olefins | |
| US2316775A (en) | Treatment of hydrocarbons | |
| US2259630A (en) | Process for thermally reacting hydrocarbons |