AU2001231667A1 - Method for producing c2 and c3 olefins of hydrocarbons - Google Patents

Method for producing c2 and c3 olefins of hydrocarbons

Info

Publication number
AU2001231667A1
AU2001231667A1 AU2001231667A AU3166701A AU2001231667A1 AU 2001231667 A1 AU2001231667 A1 AU 2001231667A1 AU 2001231667 A AU2001231667 A AU 2001231667A AU 3166701 A AU3166701 A AU 3166701A AU 2001231667 A1 AU2001231667 A1 AU 2001231667A1
Authority
AU
Australia
Prior art keywords
olefins
diolefins
fraction
cracking
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.)
Abandoned
Application number
AU2001231667A
Inventor
Peter Konig
Ulrich Koss
Martin Rothaemel
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.)
MG Technologies AG
Original Assignee
MG Technologies 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 MG Technologies AG filed Critical MG Technologies AG
Publication of AU2001231667A1 publication Critical patent/AU2001231667A1/en
Abandoned 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
    • C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
    • C10G51/04—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only including only thermal and catalytic cracking steps
    • 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

Abstract

The feed hydrocarbon together with steam is passed as vapor through a thermal steam cracking in which it is heated to temperatures in the range from 700 to 1000° C., where a cracking mixture is produced which contains C2- to C6-olefins and C4- to C6-diolefins. From the cracking mixture a first fraction, which contains C2- and C3-olefins, and a second fraction, which contains olefins and diolefins of the range C4 to C6, are separated. The diolefins are at least partly removed from the second fraction, and an intermediate product is produced which consists of C4- to C6-olefins for at least 30 wt-%. A feed mixture containing C4- to C6-olefins and steam is introduced into a reactor with an inlet temperature of 300 to 700° C., which reactor contains a bed of granular, form-selective catalyst, where a product mixture containing C2- to C4-olefins is withdrawn from the bed and C2- and C3-olefins are separated from the product mixture.
AU2001231667A 2000-01-12 2001-01-08 Method for producing c2 and c3 olefins of hydrocarbons Abandoned AU2001231667A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10000889 2000-01-12
DE10000889A DE10000889C2 (en) 2000-01-12 2000-01-12 Process for the production of C¶2¶ and C¶3¶ olefins from hydrocarbons
PCT/EP2001/000129 WO2001051590A1 (en) 2000-01-12 2001-01-08 Method for producing c2 and c3 olefins of hydrocarbons

Publications (1)

Publication Number Publication Date
AU2001231667A1 true AU2001231667A1 (en) 2001-07-24

Family

ID=7627223

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2001231667A Abandoned AU2001231667A1 (en) 2000-01-12 2001-01-08 Method for producing c2 and c3 olefins of hydrocarbons

Country Status (17)

Country Link
US (1) US20030149322A1 (en)
EP (1) EP1252262B1 (en)
JP (1) JP4637434B2 (en)
CN (1) CN1263831C (en)
AT (1) ATE292663T1 (en)
AU (1) AU2001231667A1 (en)
BR (1) BR0107573B1 (en)
CA (1) CA2396986A1 (en)
CZ (1) CZ302128B6 (en)
DE (2) DE10000889C2 (en)
MX (1) MXPA02006800A (en)
PL (1) PL196066B1 (en)
RU (1) RU2256692C2 (en)
SK (1) SK286459B6 (en)
TW (1) TW538036B (en)
WO (1) WO2001051590A1 (en)
ZA (1) ZA200205192B (en)

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DE10000889C2 (en) * 2000-01-12 2002-12-19 Mg Technologies Ag Process for the production of C¶2¶ and C¶3¶ olefins from hydrocarbons
EP1424128B1 (en) * 2002-12-01 2008-12-31 Süd-Chemie Ag Use of a catalyst based on crystalline aluminosilicate
DE102004008573A1 (en) * 2004-02-19 2005-09-08 Stockhausen Gmbh A process for removing carbonaceous residues in a reactor
CN1333052C (en) * 2004-07-14 2007-08-22 中国石油化工股份有限公司 Method and device for preparing low carbon olefine and arene
RU2399648C2 (en) * 2004-08-10 2010-09-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Method for obtaining middle-distillate product and low molecular weight olefins from hydrocarbon raw material and device for its implementation
CN100418938C (en) * 2005-09-07 2008-09-17 中国石油化工股份有限公司 Method for separating product of carbonaceous olefin catalytic cracking
CA2685541A1 (en) * 2007-04-30 2008-11-06 Shell Oil Company Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
DE112008002718T5 (en) * 2007-10-10 2010-09-09 Shell Internationale Research Maatschappij B.V. Systems and processes for producing a middle distillate product and lower olefins from a hydrocarbon feedstock
US20110034647A1 (en) * 2007-11-29 2011-02-10 Weijian Mo Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
BRPI0918927B1 (en) * 2008-09-17 2018-03-06 Asahi Kasei Chemicals Corporation Process for producing olefin, and apparatus for producing olefin having 3 or more carbon atoms from ethane
US8137631B2 (en) * 2008-12-11 2012-03-20 Uop Llc Unit, system and process for catalytic cracking
US8246914B2 (en) * 2008-12-22 2012-08-21 Uop Llc Fluid catalytic cracking system
US9242909B2 (en) 2008-12-26 2016-01-26 Jx Nippon Oil & Energy Corporation Method for refining dicyclopentadiene
JP5441025B2 (en) * 2008-12-26 2014-03-12 Ｊｘ日鉱日石エネルギー株式会社 Method for purifying dicyclopentadiene
US8889076B2 (en) * 2008-12-29 2014-11-18 Uop Llc Fluid catalytic cracking system and process
DE102010026880A1 (en) 2010-07-12 2012-01-12 Süd-Chemie AG Process for preparing zeolite-based catalysts for converting oxygenates to lower olefins
RU2518080C2 (en) * 2011-07-08 2014-06-10 Общество с ограниченной ответственностью "Премиум Инжиниринг" Heavy oil stock processing method and device
ES2558205T3 (en) * 2012-08-09 2016-02-02 Linde Ag Procedure for the conversion of hydrocarbon feedstocks into olefin-containing product streams by thermal dissociation with steam
CN104583371B (en) * 2012-08-09 2017-04-05 林德股份公司 The method that hydrocarbon feed is converted by vapours cracking
IN2014DN11048A (en) * 2012-08-09 2015-09-25 Linde Ag
EP2867339B1 (en) * 2012-08-09 2015-10-28 Linde Aktiengesellschaft Method for producing olefins through thermal water splitting
AU2013343861B2 (en) * 2012-11-08 2017-12-21 Linde Aktiengesellschaft Process for producing olefin-containing products by thermal steam cracking
WO2016098909A1 (en) * 2014-12-19 2016-06-23 千代田化工建設株式会社 Production method for lower olefin, production device for lower olefin, construction method for lower olefin production equipment, and zeolite catalyst
JP6480726B2 (en) * 2014-12-19 2019-03-13 千代田化工建設株式会社 Lower olefin production method, lower olefin production apparatus, and lower olefin production facility construction method
WO2016192041A1 (en) * 2015-06-02 2016-12-08 中国科学院大连化学物理研究所 Process for converting naphtha
EA202090313A1 (en) * 2017-07-18 2020-05-14 ЛАММУС ТЕКНОЛОДЖИ ЭлЭлСи UNITED THERMAL AND CATALYTIC CRACKING FOR PRODUCING OLEFINS

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US3565970A (en) * 1969-05-26 1971-02-23 Phillips Petroleum Co Hydrocarbon cracking
DE3765324D1 (en) * 1986-06-25 1990-11-08 Naphtachimie Sa METHOD AND OVEN FOR STEAM CRACKING HYDROCARBONS FOR THE PREPARATION OF OLEFINS AND DIOLEFINS.
JPH0689340B2 (en) * 1986-08-08 1994-11-09 旭化成工業株式会社 Process for producing olefins and aromatic hydrocarbons from hydrocarbons
DE4208907C1 (en) * 1992-03-17 1993-04-29 Mannesmann Ag, 4000 Duesseldorf, De Prodn. of lower alkene(s) for chemical intermediates and fuels - comprises thermal cracking of hydrocarbon feedstocks and sepn. into streams for compression and condensing into fractions
FR2733978B1 (en) * 1995-05-11 1997-06-13 Inst Francais Du Petrole PROCESS AND INSTALLATION FOR THE CONVERSION OF OLEFINIC C4 AND C5 CUPS INTO ETHER AND PROPYLENE
DE19648795A1 (en) * 1996-11-26 1998-05-28 Metallgesellschaft Ag Process for producing C¶3¶ and C¶4¶ olefins from a feed mixture containing C¶4¶ to C¶7¶ olefins
WO1998056740A1 (en) * 1997-06-10 1998-12-17 Exxon Chemical Patents Inc. Multi-reactor system for enhanced light olefin make
EP0921179A1 (en) * 1997-12-05 1999-06-09 Fina Research S.A. Production of olefins
EP0921177A1 (en) * 1997-12-05 1999-06-09 Fina Research S.A. Production of olefins
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DE10000889C2 (en) * 2000-01-12 2002-12-19 Mg Technologies Ag Process for the production of C¶2¶ and C¶3¶ olefins from hydrocarbons

Also Published As

Publication number Publication date
SK9972002A3 (en) 2003-09-11
ZA200205192B (en) 2003-09-29
JP4637434B2 (en) 2011-02-23
JP2003525971A (en) 2003-09-02
CN1263831C (en) 2006-07-12
SK286459B6 (en) 2008-10-07
MXPA02006800A (en) 2002-10-17
EP1252262A1 (en) 2002-10-30
DE10000889C2 (en) 2002-12-19
PL196066B1 (en) 2007-11-30
CN1395609A (en) 2003-02-05
DE50105830D1 (en) 2005-05-12
EP1252262B1 (en) 2005-04-06
TW538036B (en) 2003-06-21
DE10000889A1 (en) 2001-07-26
WO2001051590A1 (en) 2001-07-19
CZ302128B6 (en) 2010-11-03
CZ20022357A3 (en) 2003-08-13
US20030149322A1 (en) 2003-08-07
RU2002121483A (en) 2004-01-10
CA2396986A1 (en) 2001-07-19
RU2256692C2 (en) 2005-07-20
BR0107573A (en) 2003-01-14
BR0107573B1 (en) 2011-05-03
ATE292663T1 (en) 2005-04-15
PL357673A1 (en) 2004-07-26

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