GB1178449A - Method and Apparatus for Performing Pyrolysis Reactions. - Google Patents

Method and Apparatus for Performing Pyrolysis Reactions.

Info

Publication number
GB1178449A
GB1178449A GB46819/67A GB4681967A GB1178449A GB 1178449 A GB1178449 A GB 1178449A GB 46819/67 A GB46819/67 A GB 46819/67A GB 4681967 A GB4681967 A GB 4681967A GB 1178449 A GB1178449 A GB 1178449A
Authority
GB
United Kingdom
Prior art keywords
oxygen
hot gases
wall
reaction chamber
feed
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
GB46819/67A
Inventor
Miloslav Staud
Anatolij Lazarev
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.)
CHEPOS ZD Y CHEMICKEHO A POATR
Original Assignee
CHEPOS ZD Y CHEMICKEHO A POATR
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 CHEPOS ZD Y CHEMICKEHO A POATR filed Critical CHEPOS ZD Y CHEMICKEHO A POATR
Publication of GB1178449A publication Critical patent/GB1178449A/en
Expired legal-status Critical Current

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
    • C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
    • C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S48/00—Gas: heating and illuminating
    • Y10S48/05—Diffusion membrane for gas reaction or separation
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/909—Heat considerations
    • Y10S585/91—Exploiting or conserving heat of quenching, reaction, or regeneration
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00—Chemistry of hydrocarbon compounds
    • Y10S585/919—Apparatus considerations
    • Y10S585/921—Apparatus considerations using recited apparatus structure
    • Y10S585/922—Reactor fluid manipulating device
    • Y10S585/923—At reactor inlet

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

1,178,449. Cracking hydrocarbons. CHEPOS, ZAVODY CHEMICKEHO A POATRAVINARSKEHO STROJIRENSTVI BRNO, OBOR. OVY PODNIK. 13 Oct., 1967 [14 Oct., 1966], No. 46819/67. Heading C5E. Hydrocarbons are cracked, e.g. to produce ethylene, propylene or acetylene, by mixing the feed with hot gases formed by reacting combustible gas or vapour with an oxygen-containing gas, conducting the mixture of feed and hot gases to a reaction chamber, and introducing a further supply of oxygen-containing gas into the reaction chamber through a porous wall to react with the mixture of feed and hot gases. Further heat is thus provided during the cracking reaction, and heat loss through the reactor wall is reduced. As shown, combustible gas 9 is burned in burner 1 by oxygen 8 to form hot gases, the temperature of which may be controlled by water vapour 10. The resulting hot gases are mixed with hydrocarbon feed 11, e.g. gasoline, in mixer 2, and the mixture then enters reaction chamber 5, which is bound by a permeable wall 4 located inside a jacket 3. Oxygen 12 under pressure enters the annular space between jacket 3 and permeable wall 12, and passes through the wall into reaction chamber 5. The amount of oxygen may be adjusted to give desired temperature conditions in chamber 5. Products are cooled at 6, and leave via 7. The wall 5 may be frusto-conical in shape, the greater base being at the outlet side.
GB46819/67A 1966-10-14 1967-10-13 Method and Apparatus for Performing Pyrolysis Reactions. Expired GB1178449A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CS653566 1966-10-14

Publications (1)

Publication Number Publication Date
GB1178449A true GB1178449A (en) 1970-01-21

Family

ID=5412611

Family Applications (1)

Application Number Title Priority Date Filing Date
GB46819/67A Expired GB1178449A (en) 1966-10-14 1967-10-13 Method and Apparatus for Performing Pyrolysis Reactions.

Country Status (4)

Country Link
US (2) US3563709A (en)
DE (1) DE1643811A1 (en)
FR (1) FR1555656A (en)
GB (1) GB1178449A (en)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4038036A (en) * 1974-09-16 1977-07-26 The Ralph M. Parsons Company Apparatus for the production of sulfur from mixtures of hydrogen sulfide and fixed nitrogen compounds
US4044068A (en) * 1975-10-14 1977-08-23 Allied Chemical Corporation Process and apparatus for autothermic cracking of ethane to ethylene
US4760210A (en) * 1981-01-27 1988-07-26 Sweeney Maxwell P Partial oxidation system
EP0070304A4 (en) * 1981-01-27 1984-03-26 Maxwell P Sweeney Partial oxidation system.
US4321131A (en) * 1981-04-15 1982-03-23 Union Carbide Corporation Process for heat carrier generation
FI65275C (en) * 1982-06-14 1984-04-10 Neste Oy FOERFARANDE FOER TERMISK KRACKNING AV KOLVAETEOLJA
FR2546174B1 (en) * 1983-05-20 1986-09-19 Rhone Poulenc Chim Base PROCESS FOR VAPOCRACKING HYDROCARBONS
US4536603A (en) * 1983-12-22 1985-08-20 Rockwell International Corporation Production of acetylene from coal by contact with a combustion gas
US4724272A (en) * 1984-04-17 1988-02-09 Rockwell International Corporation Method of controlling pyrolysis temperature
US4983783A (en) * 1989-07-25 1991-01-08 Illinois Institute Of Technology Reduction in carbon oxides in oxidative pyrolysis of halogenated methanes
US5104417A (en) * 1990-07-13 1992-04-14 E. I. Du Pont De Nemours And Company Substitute coal from acetylene production by-products
GB9117216D0 (en) * 1991-08-09 1991-09-25 British Petroleum Co Plc Process for the production of mono-olefins
US5344862A (en) * 1991-10-25 1994-09-06 Kimberly-Clark Corporation Thermoplastic compositions and nonwoven webs prepared therefrom
WO1997002223A2 (en) * 1995-06-30 1997-01-23 Vitaly Lissianski Method for producing ethylene and other chemicals
GB0229497D0 (en) * 2002-12-18 2003-01-22 Bp Chem Int Ltd Process for the production of olefins
US8450552B2 (en) * 2009-05-18 2013-05-28 Exxonmobil Chemical Patents Inc. Pyrolysis reactor materials and methods
CN101920187B (en) * 2010-09-17 2012-10-24 王仲华 Equipment and method for preparing low-carbon olefins by cracking reactions
US10160697B2 (en) * 2012-08-21 2018-12-25 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9656229B2 (en) * 2012-08-21 2017-05-23 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US20140058173A1 (en) * 2012-08-21 2014-02-27 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9707530B2 (en) * 2012-08-21 2017-07-18 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US10029957B2 (en) * 2012-08-21 2018-07-24 Uop Llc Methane conversion apparatus and process using a supersonic flow reactor
US9689615B2 (en) * 2012-08-21 2017-06-27 Uop Llc Steady state high temperature reactor
KR20160147482A (en) * 2015-06-15 2016-12-23 삼성전자주식회사 Apparatus for manufacturing Semiconductor Devices Having a Gas Mixing Part
JP7079968B2 (en) * 2018-05-09 2022-06-03 株式会社パロマ Premixer and combustion device

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1808168A (en) * 1923-07-31 1931-06-02 Standard Oil Dev Co Dehydrogenating hydrocarbons
US2174288A (en) * 1935-06-07 1939-09-26 Ig Farbenindustrie Ag Production of olefins from gaseous or vaporous saturated hydrocarbons
US2387731A (en) * 1943-07-06 1945-10-30 Phillips Petroleum Co Manufacture of diolefins
US2790838A (en) * 1952-01-16 1957-04-30 Eastman Kodak Co Process for pyrolysis of hydrocarbons
US3161695A (en) * 1960-05-13 1964-12-15 Du Pont Process for making acetylene
US3361839A (en) * 1964-10-28 1968-01-02 Universal Oil Prod Co Dehydrogenation process
US3375288A (en) * 1964-10-28 1968-03-26 Universal Oil Prod Co Dehydrogenation of hydrocarbons at high conversion levels

Also Published As

Publication number Publication date
FR1555656A (en) 1969-01-31
DE1643811A1 (en) 1971-03-11
US3563709A (en) 1971-02-16
US3692862A (en) 1972-09-19

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