GB1150437A - Catalytic Cracking of Hydrocarbons containing Two to Thirty Carbon Atoms - Google Patents
Catalytic Cracking of Hydrocarbons containing Two to Thirty Carbon AtomsInfo
- Publication number
- GB1150437A GB1150437A GB1918466A GB1918466A GB1150437A GB 1150437 A GB1150437 A GB 1150437A GB 1918466 A GB1918466 A GB 1918466A GB 1918466 A GB1918466 A GB 1918466A GB 1150437 A GB1150437 A GB 1150437A
- Authority
- GB
- United Kingdom
- Prior art keywords
- alkali metal
- catalyst
- oxide
- weight
- steam
- 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
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
1,150,437. Making combustible gas. BADI. SCHE ANILIN- & SODA-FABRIK A.G. 2 May, 1966 [3 May, 1965; 31 Dec., 1965], No. 19184/66. Heading C5E. Hydrogen-rich gas is produced by cracking vaporizable hydrocarbon mixtures with steam at elevated temperature and at atmospheric or super-atmospheric pressure in two catalytic stages in series. The first catalyst comprises Ni or Co, a carrier material, and at least 0À5% by weight (calculated as oxide) of an alkali metal compound; the second catalyst comprises Ni which contains less than 0À5% by weight (oxide basis) alkali metal compound. Temperatures are 350‹ to 650‹ C. for the first stage and 550‹ to 950‹ C. for the second. Pt or Pd may be included in the first catalyst, and the carrier for both catalysts is magnesium oxide with or without alumina to which zirconium dioxide may be added. Suitable alkali metal compounds are the oxides, hydroxides, nitrates and carbonates and preferred percentages of all catalyst components are given, along with preferred temperatures, pressures, steam ratios and space velocities. The first catalyst may include an hydraulic binder or be calcined. The feed may be gasolines (boiling range 30‹ to 200‹ C,) or higher boiling fractions (up to C 30 ) if desulphurized. Three specific examples are described, in which the second stage follows immediately after the first in a common tube, and the alkali metal is potassium.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB81706A DE1245026B (en) | 1965-05-03 | 1965-05-03 | Process for the production of fission gases by catalytic cracking of hydrocarbons with a C number from C to C. |
DE1965B0085224 DE1244328C2 (en) | 1965-12-31 | 1965-12-31 | PROCESS FOR THE RECOVERY OF FASCULAR GASES BY CATALYTIC FITTING OF HYDROCARBONS WITH A C NUMBER FROM C LOW 2 TO C LOW 30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1150437A true GB1150437A (en) | 1969-04-30 |
Family
ID=25967498
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1918466A Expired GB1150437A (en) | 1965-05-03 | 1966-05-02 | Catalytic Cracking of Hydrocarbons containing Two to Thirty Carbon Atoms |
Country Status (7)
Country | Link |
---|---|
AT (1) | AT260871B (en) |
BE (1) | BE680438A (en) |
CH (1) | CH483991A (en) |
DE (1) | DE1245026B (en) |
ES (1) | ES326261A1 (en) |
GB (1) | GB1150437A (en) |
NL (1) | NL6605912A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3963642A (en) * | 1971-08-20 | 1976-06-15 | Metallgesellschaft Aktiengesellschaft | Process for producing a reducing gas |
-
1965
- 1965-05-03 DE DEB81706A patent/DE1245026B/en active Pending
-
1966
- 1966-05-02 GB GB1918466A patent/GB1150437A/en not_active Expired
- 1966-05-02 CH CH633666A patent/CH483991A/en not_active IP Right Cessation
- 1966-05-02 NL NL6605912A patent/NL6605912A/xx unknown
- 1966-05-03 BE BE680438D patent/BE680438A/xx not_active IP Right Cessation
- 1966-05-03 AT AT416766A patent/AT260871B/en active
- 1966-05-03 ES ES0326261A patent/ES326261A1/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3963642A (en) * | 1971-08-20 | 1976-06-15 | Metallgesellschaft Aktiengesellschaft | Process for producing a reducing gas |
Also Published As
Publication number | Publication date |
---|---|
CH483991A (en) | 1970-01-15 |
NL6605912A (en) | 1966-11-04 |
ES326261A1 (en) | 1967-03-01 |
AT260871B (en) | 1968-03-25 |
DE1245026B (en) | 1967-07-20 |
BE680438A (en) | 1966-11-03 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
416 | Proceeding under section 16 patents act 1949 | ||
PS | Patent sealed | ||
PE | Patent expired |