EP1252262A1 - Procede de production d'olefines c 2? et c 3? a partir d'hydrocarbures - Google Patents

Procede de production d'olefines c 2? et c 3? a partir d'hydrocarbures

Info

Publication number
EP1252262A1
EP1252262A1 EP01903630A EP01903630A EP1252262A1 EP 1252262 A1 EP1252262 A1 EP 1252262A1 EP 01903630 A EP01903630 A EP 01903630A EP 01903630 A EP01903630 A EP 01903630A EP 1252262 A1 EP1252262 A1 EP 1252262A1
Authority
EP
European Patent Office
Prior art keywords
olefins
fraction
mixture
line
diolefins
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.)
Granted
Application number
EP01903630A
Other languages
German (de)
English (en)
Other versions
EP1252262B1 (fr
Inventor
Ulrich Koss
Peter König
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 EP1252262A1 publication Critical patent/EP1252262A1/fr
Application granted granted Critical
Publication of EP1252262B1 publication Critical patent/EP1252262B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C10G51/00Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/02Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
    • C10G51/04Treatment 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
    • 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins

Definitions

  • the product mixture that comes from the reactor (23) is withdrawn from the line (30) and cooled in a cooler (31) to temperatures of approximately 30 to 80 ° C., so that water and gasoline condense out.
  • the condensate mixture arrives through the line (32) to a separator (33).
  • Water is drawn off from the separator through line (34), an organic gas phase is obtained in line (35), and line (36) is withdrawn from the product gas.
  • the product gas contains the desired products ethylene and propylene.
  • the gas from line (36) can be fed to a separation device (not shown).
  • this second fraction is fed to your line (16) a partial hydrogenation (17) on a commercial Pd / Al ⁇ O catalyst arranged in a fixed bed together with hydrogen from line (18).
  • the mixture drawn off from the hydrogenation has the composition given in TabeYe II, column B, and is fed to the reactor (23) through lines (20) and (21).
  • the product stream of line (36) has the composition according to Table II, column C and column D the composition of the gas mixture of line (39) is given.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)
  • Powder Metallurgy (AREA)
EP01903630A 2000-01-12 2001-01-08 Procede de production d'olefines c2 et c3 a partir d'hydrocarbures Expired - Lifetime EP1252262B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10000889A DE10000889C2 (de) 2000-01-12 2000-01-12 Verfahren zum Erzeugen von C¶2¶- und C¶3¶-Olefinen aus Kohlenwasserstoffen
DE10000889 2000-01-12
PCT/EP2001/000129 WO2001051590A1 (fr) 2000-01-12 2001-01-08 Procede de production d'olefines c2 et c3 a partir d'hydrocarbures

Publications (2)

Publication Number Publication Date
EP1252262A1 true EP1252262A1 (fr) 2002-10-30
EP1252262B1 EP1252262B1 (fr) 2005-04-06

Family

ID=7627223

Family Applications (1)

Application Number Title Priority Date Filing Date
EP01903630A Expired - Lifetime EP1252262B1 (fr) 2000-01-12 2001-01-08 Procede de production d'olefines c2 et c3 a partir d'hydrocarbures

Country Status (17)

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

Families Citing this family (26)

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DE10000889C2 (de) * 2000-01-12 2002-12-19 Mg Technologies Ag Verfahren zum Erzeugen von C¶2¶- und C¶3¶-Olefinen aus Kohlenwasserstoffen
ES2316514T3 (es) * 2002-12-01 2009-04-16 Sud-Chemie Ag Uso de un catalizador a base de aluminosilicato cristalino.
DE102004008573A1 (de) * 2004-02-19 2005-09-08 Stockhausen Gmbh Ein Verfahren zur Entfernung kohlenstoffhaltiger Rückstände in einem Reaktor
CN1333052C (zh) * 2004-07-14 2007-08-22 中国石油化工股份有限公司 一种生产低碳烯烃和芳烃的方法和装置
RU2399648C2 (ru) * 2004-08-10 2010-09-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Способ для получения среднедистиллятного продукта и низших олефинов из углеводородного сырья и устройство для его осуществления
CN100418938C (zh) * 2005-09-07 2008-09-17 中国石油化工股份有限公司 分离含碳烯烃催化裂解产物的方法
KR20100017363A (ko) * 2007-04-30 2010-02-16 쉘 인터내셔날 리써취 마트샤피지 비.브이. 탄화수소 원료로 중질 증류 생성물 및 저급 올레핀을 산출하는 시스템 및 방법
CN101952394B (zh) * 2007-10-10 2013-09-11 国际壳牌研究有限公司 由烃原料制备中间馏分产物和低级烯烃的***和方法
WO2009070484A1 (fr) * 2007-11-29 2009-06-04 Shell Oil Company Systèmes et procédés de fabrication d'un produit de distillat intermédiaire et d'oléfines inférieures à partir d'une charge d'hydrocarbure
BRPI0918927B1 (pt) * 2008-09-17 2018-03-06 Asahi Kasei Chemicals Corporation Processo para produzir olefina, e, aparelho para produzir olefina tendo 3 ou mais átomos de carbono a partir de etano
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 (ja) * 2008-12-26 2014-03-12 Jx日鉱日石エネルギー株式会社 ジシクロペンタジエンの精製方法
US8889076B2 (en) * 2008-12-29 2014-11-18 Uop Llc Fluid catalytic cracking system and process
DE102010026880A1 (de) 2010-07-12 2012-01-12 Süd-Chemie AG Verfahren zur Herstellung von Katalysatoren auf Zeolithbasis zur Umsetzung von Oxygenaten zu niederen Olefinen
RU2518080C2 (ru) * 2011-07-08 2014-06-10 Общество с ограниченной ответственностью "Премиум Инжиниринг" Способ и устройство переработки тяжелого нефтяного сырья
ES2559612T3 (es) * 2012-08-09 2016-02-15 Linde Ag Procedimiento para la conversión de cargas de hidrocarburos a través de craqueo térmico con vapor de agua
HUE027413T2 (en) * 2012-08-09 2016-10-28 Linde Ag Process for converting hydrocarbon feedstock to olefin product stream by thermal steam steam cracking
EP2867337B1 (fr) * 2012-08-09 2015-11-04 Linde Aktiengesellschaft Procédé de fabrication d'oléfines par craquage thermique à la vapeur d'eau dans des fours de craquage
CN104540925B (zh) * 2012-08-09 2017-04-05 林德股份公司 通过热蒸汽裂化制备烯烃的方法
CN104769082B (zh) * 2012-11-08 2017-03-29 林德股份公司 通过热蒸汽裂解制备含烯烃产品的方法
JP6480726B2 (ja) * 2014-12-19 2019-03-13 千代田化工建設株式会社 低級オレフィンの製造方法、低級オレフィンの製造装置および低級オレフィンの製造設備の構築方法
WO2016098909A1 (fr) * 2014-12-19 2016-06-23 千代田化工建設株式会社 Procédé et dispositif de production d'oléfines inférieures, procédé de construction pour équipement de production d'oléfines inférieures, et catalyseur de type zéolithe
US10538711B2 (en) 2015-06-02 2020-01-21 Sabic Global Technologies B.V. Process for converting naphtha
JP6967135B2 (ja) 2017-07-18 2021-11-17 ルーマス テクノロジー エルエルシー オレフィン製造のための一体化された熱・接触分解

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DE3765324D1 (de) * 1986-06-25 1990-11-08 Naphtachimie Sa Verfahren und ofen fuer das dampfkracken von kohlenwasserstoffen fuer die zubereitung von olefinen und diolefinen.
JPH0689340B2 (ja) * 1986-08-08 1994-11-09 旭化成工業株式会社 炭化水素からオレフイン類および芳香族炭化水素を製造する方法
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 (fr) * 1995-05-11 1997-06-13 Inst Francais Du Petrole Procede et installation pour la conversion de coupes c4 et c5 olefiniques en ether et en propylene
DE19648795A1 (de) * 1996-11-26 1998-05-28 Metallgesellschaft Ag Verfahren zum Erzeugen von C¶3¶- und C¶4¶-Olefinen aus einem C¶4¶- bis C¶7¶-Olefine enthaltenden Einsatzgemisch
AU7956398A (en) * 1997-06-10 1998-12-30 Exxon Chemical Patents Inc. Multi-reactor system for enhanced light olefin make
EP0921177A1 (fr) * 1997-12-05 1999-06-09 Fina Research S.A. Production d'oléfines
EP0921179A1 (fr) * 1997-12-05 1999-06-09 Fina Research S.A. Production d'oléfines
DE19813720A1 (de) * 1998-03-27 1999-09-30 Basf Ag Verfahren zur Herstellung von Olefinen
WO2000010948A1 (fr) * 1998-08-25 2000-03-02 Asahi Kasei Kogyo Kabushiki Kaisha Procede de production d'ethylene et de propylene
DE10000889C2 (de) * 2000-01-12 2002-12-19 Mg Technologies Ag Verfahren zum Erzeugen von C¶2¶- und C¶3¶-Olefinen aus Kohlenwasserstoffen

Non-Patent Citations (1)

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Title
See references of WO0151590A1 *

Also Published As

Publication number Publication date
BR0107573A (pt) 2003-01-14
RU2002121483A (ru) 2004-01-10
TW538036B (en) 2003-06-21
CZ302128B6 (cs) 2010-11-03
RU2256692C2 (ru) 2005-07-20
SK9972002A3 (en) 2003-09-11
JP2003525971A (ja) 2003-09-02
US20030149322A1 (en) 2003-08-07
AU2001231667A1 (en) 2001-07-24
DE10000889A1 (de) 2001-07-26
DE10000889C2 (de) 2002-12-19
PL196066B1 (pl) 2007-11-30
CA2396986A1 (fr) 2001-07-19
SK286459B6 (sk) 2008-10-07
DE50105830D1 (de) 2005-05-12
JP4637434B2 (ja) 2011-02-23
WO2001051590A1 (fr) 2001-07-19
CN1395609A (zh) 2003-02-05
ZA200205192B (en) 2003-09-29
CN1263831C (zh) 2006-07-12
BR0107573B1 (pt) 2011-05-03
PL357673A1 (en) 2004-07-26
CZ20022357A3 (cs) 2003-08-13
ATE292663T1 (de) 2005-04-15
MXPA02006800A (es) 2002-10-17
EP1252262B1 (fr) 2005-04-06

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