[go: up one dir, main page]

GB1132865A - Catalytic cracking of hydrocarbons containing two to thirty carbon atoms - Google Patents

Catalytic cracking of hydrocarbons containing two to thirty carbon atoms

Info

Publication number
GB1132865A
GB1132865A GB1050866A GB1050866A GB1132865A GB 1132865 A GB1132865 A GB 1132865A GB 1050866 A GB1050866 A GB 1050866A GB 1050866 A GB1050866 A GB 1050866A GB 1132865 A GB1132865 A GB 1132865A
Authority
GB
United Kingdom
Prior art keywords
catalyst
gas
content
steam
cracked gas
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
Application number
GB1050866A
Inventor
Leopold Hupfer
Wolfgang Rall
Bruno Triebskorn
Gerhard Baron
Hans Werner Gross
Erwin Ehrhardt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
GEA Group AG
Original Assignee
BASF SE
Metallgesellschaft AG
Badische Anilin and Sodafabrik AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by BASF SE, Metallgesellschaft AG, Badische Anilin and Sodafabrik AG filed Critical BASF SE
Publication of GB1132865A publication Critical patent/GB1132865A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/06Catalytic processes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C9/00Aliphatic saturated hydrocarbons
    • C07C9/02Aliphatic saturated hydrocarbons with one to four carbon atoms
    • C07C9/04Methane
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

1,132,865. Making combustible gas. BADISCHE ANILIN - & SODA - FABRIK A.G., and METALLGESELLSCHAFT A.G. 10 March, 1966 [11 March, 1965], No. 10508/66. Heading C5E. A cracked gas of high CH 4 content is made by cracking C 2 to C 30 hydrocarbons with steam at atmospheric or superatmospheric pressure at a temperature of from 350‹ to 550‹ C. The catalyst comprises 35 to 50% b.w. Ni, a carrier material, e.g. alumina, magnesia, zirconium dioxide or titanium dioxide, and an hydraulic binder, e.g. calcium aluminate, and the inner surface area of the catalyst must be at least 15 m<SP>2</SP>/gm. An alkali metal compound or a chromium compound may be added to the carrier. Pressures up to 100 atmos. are mentioned, but 20 to 60 atmos. are preferred, and catalyst surface areas up to 200 m<SP>2</SP>/gm are mentioned, with 15 to 40 preferred. The cracked gas may be further catalytically cracked at above 550‹ C. to increase the H 2 content, or at below 350‹ C. to increase the CH 4 content, and the initial cracked gas may be mixed with a cracked gas rich in H 2 and CO to provide town's gas. Three specific examples are described, in one of which, see Fig. (not shown), steam at 500‹ C. enters at (4) a reactor (1) to heat catalyst-filled tubes (2) externally, the steam leaving at (5) for delivery to a line (6) through which a mixture of desulphurized gasoline and hydrogen is delivered to the tubes (2). Examples of feedstocks are given.
GB1050866A 1965-03-11 1966-03-10 Catalytic cracking of hydrocarbons containing two to thirty carbon atoms Expired GB1132865A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEB0080928 1965-03-11

Publications (1)

Publication Number Publication Date
GB1132865A true GB1132865A (en) 1968-11-06

Family

ID=6980896

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1050866A Expired GB1132865A (en) 1965-03-11 1966-03-10 Catalytic cracking of hydrocarbons containing two to thirty carbon atoms

Country Status (6)

Country Link
AT (1) AT263989B (en)
BE (1) BE677760A (en)
CH (1) CH443243A (en)
DE (1) DE1545430A1 (en)
GB (1) GB1132865A (en)
NL (1) NL6603221A (en)

Also Published As

Publication number Publication date
CH443243A (en) 1967-09-15
AT263989B (en) 1968-08-12
NL6603221A (en) 1966-09-12
BE677760A (en) 1966-08-01
DE1545430A1 (en) 1970-01-22

Similar Documents

Publication Publication Date Title
GB1033764A (en) Improvements in or relating to the production of methane gases
US3387942A (en) Production of hydrogen
US2346754A (en) Fuel oil gasification
GB1442172A (en) Catalyst and thue use thereof for the production of gas containing methane
GB1120258A (en) Improvements in or relating to a process for catalytic high-pressure reforming of petroleum hydrocarbons with steam
GB1462059A (en) Catalyst and its use for the manufacture of gases containing methane manufacture of methane from gases containing carbon monoxide and dioxide and hydrogen
GB1132865A (en) Catalytic cracking of hydrocarbons containing two to thirty carbon atoms
GB1379498A (en) Steam reforming of hydrocarbons
US2593584A (en) Reforming hydrocarbon gases in the presence of a magnesia catalyst
GB1270756A (en) A process for producing synthesis gas for use in the production of ammonia
GB1354073A (en) Process and apparatus for the oxygenative cracking of hydrocarbons
GB1159247A (en) Steam Reforming of Hydrocarbons
ES295725A1 (en) A hydrocracking procedure for preparing oven oil, diesel oil, reactor fuel or mixing (Machine-translation by Google Translate, not legally binding)
GB1187676A (en) Hydrocarbon Conversion Process
US1931492A (en) Production of hydrogen
GB1342027A (en) Production of reducing gas
GB1223695A (en) Improvements in and relating to the catalytic high pressure reforming of petroleum hydrocarbons
ES305331A1 (en) Improvements in the preparation of nickel-based catalysts (Machine-translation by Google Translate, not legally binding)
US3953356A (en) Method of producing gaseous mixture rich in hydrogen
ES317574A1 (en) Improvements introduced in the preparation of catalytic compositions. (Machine-translation by Google Translate, not legally binding)
GB288662A (en) Improvements in the manufacture and production of hydrogen or gas mixtures containing hydrogen from hydrocarbons
GB1059957A (en) Improvements in and relating to the steam reformation of light hydrocarbon feeds
ES389035A1 (en) Catalytic hydrocracking process
GB1064481A (en) Improvements in or relating to catalysts useful in the steam reforming of hydrocarbons
GB1129114A (en) Flameless cracking of gaseous and/or liquid vaporisable hydrocarbons having from twoto thirty carbon atoms