GB996231A - Method of and apparatus for continuous catalytic cracking of readily volatile hydrocarbons - Google Patents

Method of and apparatus for continuous catalytic cracking of readily volatile hydrocarbons

Info

Publication number
GB996231A
GB996231A GB2496563A GB2496563A GB996231A GB 996231 A GB996231 A GB 996231A GB 2496563 A GB2496563 A GB 2496563A GB 2496563 A GB2496563 A GB 2496563A GB 996231 A GB996231 A GB 996231A
Authority
GB
United Kingdom
Prior art keywords
steam
heated
hydrocarbons
air
separately
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
GB2496563A
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.)
Heinrich Koppers GmbH
Original Assignee
Heinrich Koppers GmbH
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 Heinrich Koppers GmbH filed Critical Heinrich Koppers GmbH
Publication of GB996231A publication Critical patent/GB996231A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/38Production 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
    • C01B3/382Multi-step processes
    • 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
    • C10G11/10Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
    • 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
    • C10G11/20Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert heated gases or vapours
    • C10G11/22Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert heated gases or vapours produced by partial combustion of the material to be cracked

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

<PICT:0996231/C4-C5/1> In a process for the catalytic cracking with steam of volatile hydrocarbons to make a fuel gas, some at least of the steam, and the or some of any air in the reaction mixture, are heated separately of the hydrocarbon vapours to 800 DEG to 850 DEG C. in a catalyst-free zone 2 of an externally heated tube 1, the hydrocarbon vapours being separately heated only to a degree first short of thermal decomposition, the heated reaction mixture constituents being quickly mixed in a zone 9 before entering the catalyst zone 3. Steam enters at 6 and hydrocarbons, preheated e.g. to 300 DEG C., at 7, and air, if any, enters at 5. Some steam, e.g. 20% to 40% of the total, may be delivered with the hydrocarbons at 7 to control the heating thereof. The exothermic reaction in the region 10, 9 causes a rapid temperature rise there and militates against the formation of polymerizates, even at pressures of 3 to 15 atmospheres. Instead of being delivered separately, the air may be mixed with steam for delivery at 6.
GB2496563A 1962-07-12 1963-06-24 Method of and apparatus for continuous catalytic cracking of readily volatile hydrocarbons Expired GB996231A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEK47216A DE1199428B (en) 1962-07-12 1962-07-12 Device for the continuous catalytic splitting of volatile hydrocarbons

Publications (1)

Publication Number Publication Date
GB996231A true GB996231A (en) 1965-06-23

Family

ID=7224480

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2496563A Expired GB996231A (en) 1962-07-12 1963-06-24 Method of and apparatus for continuous catalytic cracking of readily volatile hydrocarbons

Country Status (4)

Country Link
AT (1) AT240508B (en)
CH (1) CH472490A (en)
DE (1) DE1199428B (en)
GB (1) GB996231A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0036268A1 (en) * 1980-03-18 1981-09-23 British Gas Corporation Vaporisation and gasification of hydrocarbon feedstocks

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2371147A (en) * 1945-03-13 Preparation op unsaturated ali
FR1019972A (en) * 1950-06-03 1953-01-30 Cie Pan Europ D Installations Improvements in the means for the production of gas used for synthesis purposes, in particular for the synthesis of ammonia
GB680874A (en) * 1950-06-03 1952-10-15 Cie Pan Europ D Installations Improvements in plants for the gasifying of liquid fuels, in particular oils
DE1003910B (en) * 1953-02-16 1957-03-07 Didier Werke Ag Process for the thermal transformation of gases containing hydrocarbons, of gaseous hydrocarbons and for oil gasification
DE1003911B (en) * 1954-02-08 1957-03-07 Didier Werke Ag Method and device for the thermal transformation of hydrocarbons and gases containing hydrocarbons
DE1035309B (en) * 1957-08-29 1958-07-31 Didier Werke Ag Method and device for the thermal transformation of hydrocarbons into fuel gas free from or low in hydrocarbons

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0036268A1 (en) * 1980-03-18 1981-09-23 British Gas Corporation Vaporisation and gasification of hydrocarbon feedstocks

Also Published As

Publication number Publication date
AT240508B (en) 1965-06-10
DE1199428B (en) 1965-08-26
CH472490A (en) 1969-05-15

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