GB587615A - Improved process for the isomerization of straight chain paraffinic hydrocarbons - Google Patents
Improved process for the isomerization of straight chain paraffinic hydrocarbonsInfo
- Publication number
- GB587615A GB587615A GB7443/43A GB744343A GB587615A GB 587615 A GB587615 A GB 587615A GB 7443/43 A GB7443/43 A GB 7443/43A GB 744343 A GB744343 A GB 744343A GB 587615 A GB587615 A GB 587615A
- Authority
- GB
- United Kingdom
- Prior art keywords
- isomerization
- carrier
- chloride
- porocel
- aluminium
- 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
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Normal paraffins of at least 5 carbon atoms are isomerized by contact in the vapour phase at superatmospheric pressures up to 180 p.s.i. with an aluminium halide catalyst supported on a solid carrier and arranged in solid beds, at a temperature of 400-500 DEG F., in the presence of 2-22 per cent by weight of a halogen-containing promoter and in the absence of hydrogen, the rate of flow of normal paraffin feed being 0.25-2 vols./vol./hr. and the contact time 16-260 secs. In a modification, hydrogen having a partial pressure of 50-600 p.s.i. may be present, the total pressure being up to 1000 p.s.i. Rate of isomerization and selectivity increase with increase of temperature. The preferred catalyst is aluminium chloride or bromide on a carrier such as activated carbon or alumina, acid-treated clays, bauxite and particularly "Porocel" (Registered Trade Mark). Aluminium chloride may be vaporized and carried by a carrier gas into contact with the carrier or mixed therewith in solid form or in presence of a solvent. The "Porocel" may be preheated to 1000-1400 DEG F. for 1-18 hrs. and, after absorbing the chloride vapours, may be heated to 25-100 DEG F. higher than the isomerization temperature in an inert gas to remove all but tenaciously held chloride, generally about 4-12 per cent by weight. The feed may be normal pentane, which may contain small amounts of isopentane, or hexane, heptane or higher paraffins, casinghead gasoline or straight-run naphtha. Olefins and water are removed with concentrated sulphuric acid or fluor- or chlor-sulphonic acids, and sulphur with caustic alkali. A plurality of reactors may be arranged in series or parallel. The catalyst is regenerated by heating to remove aluminium halide, burning at 700-1000 DEG F. with oxygen-containing gas, and re-impregnating. Examples describe the isomerization of pentane with aluminium chloride on "Porocel" at varying reaction conditions. Specifications 498,463, 535,398 and 543,085 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US587615XA | 1942-10-07 | 1942-10-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB587615A true GB587615A (en) | 1947-05-01 |
Family
ID=22018773
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7443/43A Expired GB587615A (en) | 1942-10-07 | 1943-05-11 | Improved process for the isomerization of straight chain paraffinic hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB587615A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020160467A1 (en) * | 2019-02-01 | 2020-08-06 | Uop Llc | Process for isomerizing a hydrocarbon feed stream |
-
1943
- 1943-05-11 GB GB7443/43A patent/GB587615A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020160467A1 (en) * | 2019-02-01 | 2020-08-06 | Uop Llc | Process for isomerizing a hydrocarbon feed stream |
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