DE59605560D1 - Hydrocarbon splitting method and device - Google Patents

Hydrocarbon splitting method and device

Info

Publication number
DE59605560D1
DE59605560D1 DE59605560T DE59605560T DE59605560D1 DE 59605560 D1 DE59605560 D1 DE 59605560D1 DE 59605560 T DE59605560 T DE 59605560T DE 59605560 T DE59605560 T DE 59605560T DE 59605560 D1 DE59605560 D1 DE 59605560D1
Authority
DE
Germany
Prior art keywords
splitting method
hydrocarbon
hydrocarbon splitting
splitting
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 - Fee Related
Application number
DE59605560T
Other languages
German (de)
Inventor
Dr Kaufmann
Dr Zimmermann
Michael Wyrostek
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.)
Veba Oel AG
Linde GmbH
Original Assignee
Veba Oel AG
Linde 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 Veba Oel AG, Linde GmbH filed Critical Veba Oel AG
Application granted granted Critical
Publication of DE59605560D1 publication Critical patent/DE59605560D1/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/10—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/007—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor in the presence of catalytically active bodies, e.g. porous plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation 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
    • C07C4/06—Catalytic processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00164—Controlling or regulating processes controlling the flow
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
    • C07C2521/04—Alumina
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the alkali- or alkaline earth metals or beryllium
    • C07C2523/04—Alkali metals
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/20—Vanadium, niobium or tantalum
    • C07C2523/22—Vanadium
DE59605560T 1995-02-17 1996-02-14 Hydrocarbon splitting method and device Expired - Fee Related DE59605560D1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19505455 1995-02-17
DE19600684A DE19600684A1 (en) 1995-02-17 1996-01-10 Hydrocarbon splitting method and device

Publications (1)

Publication Number Publication Date
DE59605560D1 true DE59605560D1 (en) 2000-08-17

Family

ID=7754289

Family Applications (2)

Application Number Title Priority Date Filing Date
DE19600684A Withdrawn DE19600684A1 (en) 1995-02-17 1996-01-10 Hydrocarbon splitting method and device
DE59605560T Expired - Fee Related DE59605560D1 (en) 1995-02-17 1996-02-14 Hydrocarbon splitting method and device

Family Applications Before (1)

Application Number Title Priority Date Filing Date
DE19600684A Withdrawn DE19600684A1 (en) 1995-02-17 1996-01-10 Hydrocarbon splitting method and device

Country Status (3)

Country Link
US (1) US20030070963A1 (en)
AR (1) AR000827A1 (en)
DE (2) DE19600684A1 (en)

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US7090765B2 (en) 2002-07-03 2006-08-15 Exxonmobil Chemical Patents Inc. Process for cracking hydrocarbon feed with water substitution
US7097758B2 (en) * 2002-07-03 2006-08-29 Exxonmobil Chemical Patents Inc. Converting mist flow to annular flow in thermal cracking application
US7138047B2 (en) 2002-07-03 2006-11-21 Exxonmobil Chemical Patents Inc. Process for steam cracking heavy hydrocarbon feedstocks
US20070000810A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method for producing a crude product with reduced tan
US7648625B2 (en) 2003-12-19 2010-01-19 Shell Oil Company Systems, methods, and catalysts for producing a crude product
US7416653B2 (en) * 2003-12-19 2008-08-26 Shell Oil Company Systems and methods of producing a crude product
US7745369B2 (en) * 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
US20070012595A1 (en) * 2003-12-19 2007-01-18 Brownscombe Thomas F Methods for producing a total product in the presence of sulfur
US20060289340A1 (en) * 2003-12-19 2006-12-28 Brownscombe Thomas F Methods for producing a total product in the presence of sulfur
US20070000808A1 (en) * 2003-12-19 2007-01-04 Bhan Opinder K Method and catalyst for producing a crude product having selected properties
CA2455011C (en) * 2004-01-09 2011-04-05 Suncor Energy Inc. Bituminous froth inline steam injection processing
EP1727877B1 (en) 2004-03-22 2012-04-04 ExxonMobil Chemical Patents Inc. Process for steam cracking heavy hydrocarbon feedstocks
US7193123B2 (en) * 2004-05-21 2007-03-20 Exxonmobil Chemical Patents Inc. Process and apparatus for cracking hydrocarbon feedstock containing resid to improve vapor yield from vapor/liquid separation
US7358413B2 (en) * 2004-07-14 2008-04-15 Exxonmobil Chemical Patents Inc. Process for reducing fouling from flash/separation apparatus during cracking of hydrocarbon feedstocks
US7244871B2 (en) * 2004-05-21 2007-07-17 Exxonmobil Chemical Patents, Inc. Process and apparatus for removing coke formed during steam cracking of hydrocarbon feedstocks containing resids
US7408093B2 (en) * 2004-07-14 2008-08-05 Exxonmobil Chemical Patents Inc. Process for reducing fouling from flash/separation apparatus during cracking of hydrocarbon feedstocks
US7312371B2 (en) * 2004-05-21 2007-12-25 Exxonmobil Chemical Patents Inc. Steam cracking of hydrocarbon feedstocks containing non-volatile components and/or coke precursors
US7402237B2 (en) * 2004-10-28 2008-07-22 Exxonmobil Chemical Patents Inc. Steam cracking of hydrocarbon feedstocks containing salt and/or particulate matter
US7220887B2 (en) * 2004-05-21 2007-05-22 Exxonmobil Chemical Patents Inc. Process and apparatus for cracking hydrocarbon feedstock containing resid
US7311746B2 (en) * 2004-05-21 2007-12-25 Exxonmobil Chemical Patents Inc. Vapor/liquid separation apparatus for use in cracking hydrocarbon feedstock containing resid
US7297833B2 (en) * 2004-05-21 2007-11-20 Exxonmobil Chemical Patents Inc. Steam cracking of light hydrocarbon feedstocks containing non-volatile components and/or coke precursors
US7488459B2 (en) * 2004-05-21 2009-02-10 Exxonmobil Chemical Patents Inc. Apparatus and process for controlling temperature of heated feed directed to a flash drum whose overhead provides feed for cracking
US7285697B2 (en) * 2004-07-16 2007-10-23 Exxonmobil Chemical Patents Inc. Reduction of total sulfur in crude and condensate cracking
US7351872B2 (en) * 2004-05-21 2008-04-01 Exxonmobil Chemical Patents Inc. Process and draft control system for use in cracking a heavy hydrocarbon feedstock in a pyrolysis furnace
US7481871B2 (en) * 2004-12-10 2009-01-27 Exxonmobil Chemical Patents Inc. Vapor/liquid separation apparatus
US7247765B2 (en) 2004-05-21 2007-07-24 Exxonmobil Chemical Patents Inc. Cracking hydrocarbon feedstock containing resid utilizing partial condensation of vapor phase from vapor/liquid separation to mitigate fouling in a flash/separation vessel
US7235705B2 (en) * 2004-05-21 2007-06-26 Exxonmobil Chemical Patents Inc. Process for reducing vapor condensation in flash/separation apparatus overhead during steam cracking of hydrocarbon feedstocks
TW200602591A (en) * 2004-07-08 2006-01-16 hong-yang Chen Gas supply device by gasifying burnable liquid
TWI415930B (en) * 2005-04-06 2013-11-21 Shell Int Research A process for reducing the total acid number (tan) of a liquid hydrocarbonaceous feedstock
EP1869144A1 (en) * 2005-04-11 2007-12-26 Shell International Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced nitrogen content
WO2006110660A1 (en) 2005-04-11 2006-10-19 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced mcr content
US20060231456A1 (en) * 2005-04-11 2006-10-19 Bhan Opinder K Systems, methods, and catalysts for producing a crude product
JP2008536000A (en) * 2005-04-11 2008-09-04 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ Method for producing crude product with low nitrogen content and catalyst
US8173854B2 (en) * 2005-06-30 2012-05-08 Exxonmobil Chemical Patents Inc. Steam cracking of partially desalted hydrocarbon feedstocks
CN1986505B (en) * 2005-12-23 2010-04-14 中国石油化工股份有限公司 Catalytic conversion process with increased low carbon olefine output
US7513260B2 (en) * 2006-05-10 2009-04-07 United Technologies Corporation In-situ continuous coke deposit removal by catalytic steam gasification
WO2007149923A2 (en) * 2006-06-22 2007-12-27 Shell Oil Company Method for producing a crude product with a long-life catalyst
EP2029698A1 (en) * 2006-06-22 2009-03-04 Shell Internationale Research Maatschappij B.V. Methods for producing a crude product from selected feed
RU2009101923A (en) * 2006-06-22 2010-07-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) METHODS FOR PRODUCING A TOTAL PRODUCT WITH SELECTIVE PRODUCTION OF HYDROCARBONS
US20080135449A1 (en) * 2006-10-06 2008-06-12 Opinder Kishan Bhan Methods for producing a crude product
US20080110801A1 (en) * 2006-11-09 2008-05-15 Leon Yuan Process For Heating A Hydrocarbon Stream Entering A Reaction Zone With A Heater Convection Section
US7740751B2 (en) 2006-11-09 2010-06-22 Uop Llc Process for heating a stream for a hydrocarbon conversion process
US8282814B2 (en) * 2009-03-31 2012-10-09 Uop Llc Fired heater for a hydrocarbon conversion process
CN102260519B (en) * 2010-05-31 2017-03-01 通用电气公司 Hydrocarbon cracking method and reaction unit
CN102557855B (en) * 2010-12-22 2015-11-25 通用电气公司 The coating process of hydrocarbon cracking method and reaction unit and hydrocarbon cracking reaction unit
WO2012161873A1 (en) * 2011-05-20 2012-11-29 Exxonmobil Chemical Patents Inc. Coke gasification on catalytically active surfaces
DE102011107933A1 (en) 2011-07-19 2013-01-24 Thyssenkrupp Uhde Gmbh Apparatus useful for passing gas through heatable reaction tube and carrying out endothermic reaction of gas in catalyst system, comprises heatable reaction tube comprising catalyst, an input portion and an output portion
US9187700B2 (en) * 2012-01-13 2015-11-17 United Technologies Corporation Method for reducing coke deposition
US9255746B2 (en) * 2012-10-26 2016-02-09 Modine Manufacturing Company Reactor core for use in a chemical reactor, and method of making the same

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GB2023453B (en) * 1977-11-01 1982-11-17 Atomic Energy Authority Uk Coating of substrates
DE2854061A1 (en) * 1978-12-14 1980-07-03 Linde Ag METHOD FOR PREHEATING HYDROCARBONS BEFORE THERMAL CLEAVING
US4599480A (en) * 1985-07-12 1986-07-08 Shell Oil Company Sequential cracking of hydrocarbons
US5658452A (en) * 1994-01-04 1997-08-19 Chevron Chemical Company Increasing production in hydrocarbon conversion processes

Also Published As

Publication number Publication date
US20030070963A1 (en) 2003-04-17
AR000827A1 (en) 1997-08-06
DE19600684A1 (en) 1996-08-22

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Legal Events

Date Code Title Description
8339 Ceased/non-payment of the annual fee