GB631258A - Improvements in or relating to the utilisation of fuel gas containing low purity hydrogen in the catalytic refining of petroleum hydrocarbons - Google Patents
Improvements in or relating to the utilisation of fuel gas containing low purity hydrogen in the catalytic refining of petroleum hydrocarbonsInfo
- Publication number
- GB631258A GB631258A GB440847A GB440847A GB631258A GB 631258 A GB631258 A GB 631258A GB 440847 A GB440847 A GB 440847A GB 440847 A GB440847 A GB 440847A GB 631258 A GB631258 A GB 631258A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- gas
- carrier
- platinum
- petroleum
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/10—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing platinum group metals or compounds thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
Petroleum and like hydrocarbons are refined, to free them from sulphur, peroxides and unsaturated compounds such as diolefins, by contacting them with a fuel gas containing low purity hydrogen at 200-800 DEG F. in the presence of a catalyst comprising 0.1-10 per cent by weight of the total catalyst of platinum or palladium incorporated with a hydrous oxide carrier having ultramicroscopic pores. Hydrocarbon fractions derived from petroleum or equivalent sources such as the Fischer-Tropsch synthesis process and hydrocarbon fractions obtained by processing treatments such as thermal or catalytic cracking may be subjected to the refining treatment. The treatment is particularly suitable for application to naphtha fractions boiling in the gasoline range. Suitable fuel gases are manufactured town gas, coal gas, water gas, blue water gas, coke oven gas, carburetted water gas and natural gas. The hydrous oxide catalyst carrier may be hydrated alumina or silica gel. Pelleted catalyst may be used in a fixed bed operation or catalyst granules may be employed with a fluid or moving catalyst technique. Elevated pressures may be employed. In an example a heavy naphtha, obtained by cracking a petroleum distillate boiling in the gas oil range in the presence of a fluidized silica alumina gel catalyst, is passed together with town gas over pellets of hydrated alumina containing 2 per cent finely-divided platinum. Preparation of catalyst.-Platinum or palladium may be incorporated with the hydrous oxide carrier, (1) by impregnation of the carrier with a salt such as ammonium chloroplatinate or chloroplatinous acid, followed by slow drying and formation of the metal by heat decomposition; or (2) by mulling the carrier in powdered form with particles of the metal, for example, platinum black, followed by wet extruding or pilling and drying.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB440847A GB631258A (en) | 1947-02-14 | 1947-02-14 | Improvements in or relating to the utilisation of fuel gas containing low purity hydrogen in the catalytic refining of petroleum hydrocarbons |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB440847A GB631258A (en) | 1947-02-14 | 1947-02-14 | Improvements in or relating to the utilisation of fuel gas containing low purity hydrogen in the catalytic refining of petroleum hydrocarbons |
Publications (1)
Publication Number | Publication Date |
---|---|
GB631258A true GB631258A (en) | 1949-10-31 |
Family
ID=9776639
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB440847A Expired GB631258A (en) | 1947-02-14 | 1947-02-14 | Improvements in or relating to the utilisation of fuel gas containing low purity hydrogen in the catalytic refining of petroleum hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB631258A (en) |
-
1947
- 1947-02-14 GB GB440847A patent/GB631258A/en not_active Expired
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