EP1637575A1 - Wanderbettverfahren zur Produktion von Propylen mit Recycling von einer Fraktion des verwendeten Katalysators - Google Patents

Wanderbettverfahren zur Produktion von Propylen mit Recycling von einer Fraktion des verwendeten Katalysators Download PDF

Info

Publication number
EP1637575A1
EP1637575A1 EP05291650A EP05291650A EP1637575A1 EP 1637575 A1 EP1637575 A1 EP 1637575A1 EP 05291650 A EP05291650 A EP 05291650A EP 05291650 A EP05291650 A EP 05291650A EP 1637575 A1 EP1637575 A1 EP 1637575A1
Authority
EP
European Patent Office
Prior art keywords
catalyst
reactor
oligocracking
fraction
moving bed
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
EP05291650A
Other languages
English (en)
French (fr)
Other versions
EP1637575B1 (de
Inventor
Sylvain Louret
Vincent Coupard
Patrice Font
Eric Sanchez
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of EP1637575A1 publication Critical patent/EP1637575A1/de
Application granted granted Critical
Publication of EP1637575B1 publication Critical patent/EP1637575B1/de
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1088—Olefins
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4081—Recycling aspects
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/70—Catalyst aspects
    • C10G2300/708—Coking aspect, coke content and composition of deposits
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (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)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)
EP05291650A 2004-09-15 2005-08-01 Wanderbettverfahren zur Produktion von Propylen mit Recycling von einer Fraktion des verwendeten Katalysators Expired - Fee Related EP1637575B1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0409795A FR2875234B1 (fr) 2004-09-15 2004-09-15 Procede de production de propylene fonctionnant en lit mobile avec recyclage d'une fraction de catalyseur use

Publications (2)

Publication Number Publication Date
EP1637575A1 true EP1637575A1 (de) 2006-03-22
EP1637575B1 EP1637575B1 (de) 2009-04-15

Family

ID=34948357

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05291650A Expired - Fee Related EP1637575B1 (de) 2004-09-15 2005-08-01 Wanderbettverfahren zur Produktion von Propylen mit Recycling von einer Fraktion des verwendeten Katalysators

Country Status (5)

Country Link
US (1) US7566811B2 (de)
EP (1) EP1637575B1 (de)
JP (1) JP5030408B2 (de)
DE (1) DE602005013870D1 (de)
FR (1) FR2875234B1 (de)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1892229A1 (de) * 2006-08-24 2008-02-27 Ifp Verfahren zur Herstellung von Propylen in Gegenwart eines makroporösen Katalysators in Form von sphärischen Kügelchen
CN102285856A (zh) * 2010-06-18 2011-12-21 中国石油化工股份有限公司 增产丙烯和乙烯的方法

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2892126B1 (fr) 2005-10-19 2010-04-30 Inst Francais Du Petrole Procede de conversion directe d'une charge comprenant des olefines a quatre, et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d'essence desulfuree
FR2932495B1 (fr) * 2008-06-17 2011-03-25 Inst Francais Du Petrole Dispositif de controle des conditions operatoires dans une unite de craquage catalytique a deux risers.
US8007728B2 (en) * 2008-12-11 2011-08-30 Uop Llc System, apparatus, and process for cracking a hydrocarbon feed
DE102009019436A1 (de) 2009-04-29 2010-11-04 Bayer Materialscience Ag Verfahren zur Herstellung von aromatischen Aminen
DE102009031911B4 (de) * 2009-07-01 2013-02-21 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren und Reaktoranlage zur Reinigung eines Brenngases
WO2011019037A1 (ja) * 2009-08-11 2011-02-17 三菱化学株式会社 触媒の製造方法
US20120296138A1 (en) * 2011-05-22 2012-11-22 Fina Technology, Inc. Method for alkylation of toluene to form styrene and ethylbenzene utilizing a moving bed reactor
US8993824B2 (en) 2011-09-28 2015-03-31 Uop Llc Fluid catalytic cracking process
EP3620499A1 (de) * 2018-09-06 2020-03-11 INDIAN OIL CORPORATION Ltd. Verfahren zur selektiven herstellung von leichten olefinen und aromaten aus gecracktem leichtem naphtha
CN115364890B (zh) * 2022-08-29 2024-03-19 中国石油大学(北京) 一种负载型甲烷热催化裂解催化剂及其制备方法与应用

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3838039A (en) 1971-12-14 1974-09-24 Universal Oil Prod Co Continuous conversion and regeneration process
US5336829A (en) 1992-03-26 1994-08-09 Institut Francais Du Petrole Continuous process for the dehydrogenation of paraffinic to olefinic hydrocarbons
US5849976A (en) 1994-07-27 1998-12-15 Uop Llc Moving bed solid catalyst hydrocarbon alkylation process
EP0921179A1 (de) * 1997-12-05 1999-06-09 Fina Research S.A. Herstellung von Olefinen
US6284939B1 (en) 1998-07-31 2001-09-04 Institut Francais Du Petrole Process for liquid-phase conversion with a moving-bed catalyst using a stripper-lift
EP1195424A1 (de) 2000-10-05 2002-04-10 ATOFINA Research Verfahren zur Krackung von olefinreichen Kohlenwasserstoffeinsätzen
WO2003000399A2 (en) * 2001-06-22 2003-01-03 Uop Llc Reaction and regeneration system
EP1365004A1 (de) * 2002-05-23 2003-11-26 ATOFINA Research Verfahren zur Herstellung von Olefinen
US20030223918A1 (en) 2001-03-23 2003-12-04 Cammy Neal E. FCC process and apparatus with automatic catalyst recycle control

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61289049A (ja) * 1985-05-27 1986-12-19 Agency Of Ind Science & Technol プロピレンの製造方法
GB9026775D0 (en) * 1990-12-10 1991-01-30 Shell Int Research Process for the preparation of an olefins-containing mixture of hydrocarbons
EP0921181A1 (de) * 1997-12-05 1999-06-09 Fina Research S.A. Herstellung von Propen
KR100338276B1 (ko) * 1998-08-25 2002-05-27 야마모토 카즈모토 에틸렌 및 프로필렌의 제조방법
IT1318527B1 (it) * 2000-05-19 2003-08-27 Enichem Spa Procedimento per la produzione di propilene da correnti olefiniche.
US7371911B2 (en) * 2005-02-25 2008-05-13 Fina Technology, Inc. Critical phase alkylation and transalkylation process in the presence of a beta zeolite

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3838039A (en) 1971-12-14 1974-09-24 Universal Oil Prod Co Continuous conversion and regeneration process
US5336829A (en) 1992-03-26 1994-08-09 Institut Francais Du Petrole Continuous process for the dehydrogenation of paraffinic to olefinic hydrocarbons
US5849976A (en) 1994-07-27 1998-12-15 Uop Llc Moving bed solid catalyst hydrocarbon alkylation process
EP0921179A1 (de) * 1997-12-05 1999-06-09 Fina Research S.A. Herstellung von Olefinen
US6284939B1 (en) 1998-07-31 2001-09-04 Institut Francais Du Petrole Process for liquid-phase conversion with a moving-bed catalyst using a stripper-lift
EP1195424A1 (de) 2000-10-05 2002-04-10 ATOFINA Research Verfahren zur Krackung von olefinreichen Kohlenwasserstoffeinsätzen
US20030223918A1 (en) 2001-03-23 2003-12-04 Cammy Neal E. FCC process and apparatus with automatic catalyst recycle control
WO2003000399A2 (en) * 2001-06-22 2003-01-03 Uop Llc Reaction and regeneration system
EP1365004A1 (de) * 2002-05-23 2003-11-26 ATOFINA Research Verfahren zur Herstellung von Olefinen

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1892229A1 (de) * 2006-08-24 2008-02-27 Ifp Verfahren zur Herstellung von Propylen in Gegenwart eines makroporösen Katalysators in Form von sphärischen Kügelchen
FR2905122A1 (fr) * 2006-08-24 2008-02-29 Inst Francais Du Petrole Procede de production de propylene en presence d'un catalyseur macroporeux se presentant sous forme de billes spheriques
US7880048B2 (en) 2006-08-24 2011-02-01 Ifp Process for producing propylene in the presence of a macroporous catalyst in the form of spherical beads
CN102285856A (zh) * 2010-06-18 2011-12-21 中国石油化工股份有限公司 增产丙烯和乙烯的方法

Also Published As

Publication number Publication date
US20060063957A1 (en) 2006-03-23
JP2006083173A (ja) 2006-03-30
FR2875234B1 (fr) 2006-11-03
FR2875234A1 (fr) 2006-03-17
EP1637575B1 (de) 2009-04-15
US7566811B2 (en) 2009-07-28
DE602005013870D1 (de) 2009-05-28
JP5030408B2 (ja) 2012-09-19

Similar Documents

Publication Publication Date Title
EP1637575B1 (de) Wanderbettverfahren zur Produktion von Propylen mit Recycling von einer Fraktion des verwendeten Katalysators
JP5436209B2 (ja) 転換増強方法及び生成物流を生産する生産方法
EP1661617B1 (de) Festbett- oder Wanderbettreaktor mit mehreren Zonen und integriertem Wärmetauscher
EP1487768B1 (de) Mehrstufenverfahren zur umsetzung einer beschickung, die olefine mit drei, vier oder mehr kohlenstoffatomen enthält, zur herstellung von propylen
EP1814654B1 (de) Reaktionsgerät mit einigen wirbelbettzonen mit versorgung in jeder regenerierten oder neuen katalysatorzone
EP1800742B1 (de) Reaktor mit zwei fluidisierbaren Reaktionsstufen und einem integrierten Gas/Feststofftrennsystem
RU2580829C2 (ru) Способ и устройство каталитического крекинга для получения пропилена
WO2006067305A1 (fr) Procede de conversion directe d’une charge comprenant des olefines a quatre et/ou cinq atomes de carbone, pour la production de propylene avec une co-production d’essence
EP1668094B1 (de) Verfahren zur direktumwandlung eines olefine mit mindestens vier oder fünf kohlenstoffatomen enthaltenden einsatzstoffs zur herstellung von propylen
EP0191695B1 (de) Verfahren und Einrichtung für die Injektion von Katalysator in ein katalytisches Wirbelschichtkrackverfahren, insbesondere von schweren Einsätzen
FR2968010A1 (fr) Procede de conversion d'une charge lourde en distillat moyen
JPH03197591A (ja) 炭化水素の接触分解方法
KR20210006415A (ko) 다단계 촉매 반응 및 재생성을 이용한 최대 올레핀 생산
CN1912059A (zh) 一种多产丙烯的催化转化方法
FR3053355B1 (fr) Procede d'oligomerisation utilisant un catalyseur zeolithique et un catalyseur comprenant une silice alumine
JP2002241764A (ja) 重質油の流動接触分解法
JP4223690B2 (ja) 重質油の流動接触分解方法
EP0325502A1 (de) Katalytische Krackverfahren
FR2770225A1 (fr) Procede et dispositif de vaporisation selective des charges d'hydrocarbures en craquage catalytique
RU2799345C2 (ru) Максимальное производство олефинов с применением многоступенчатой реакции в присутствии катализатора и его регенерации
EP0323784B1 (de) Anwendung eines einen Zeoliten aus der Erionitfamilie enthaltenden Katalysators in einem Krackverfahren, das zumindest eine Regenerationszone enthält
RU2262527C1 (ru) Способ каталитического крекинга тяжелых нефтяных фракций
FR2868788A1 (fr) Procede de conversion d'une alimentation d'hydrocarbures
FR2621322A1 (fr) Procede de vaporisation d'une charge liquide dans un procede de craquage catalytique en lit fluide
FR3090683A1 (fr) Conversion d’un brut pétrolier en lit fluidisé compartimenté

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA HR MK YU

17P Request for examination filed

Effective date: 20060922

AKX Designation fees paid

Designated state(s): BE DE GB NL

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): BE DE GB NL

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REF Corresponds to:

Ref document number: 602005013870

Country of ref document: DE

Date of ref document: 20090528

Kind code of ref document: P

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20100118

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 602005013870

Country of ref document: DE

Owner name: IFP ENERGIES NOUVELLES, FR

Free format text: FORMER OWNER: INSTITUT FRANCAIS DU PETROLE, RUEIL-MALMAISON, HAUTS-DE-SEINE, FR

Effective date: 20110331

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20200827

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20200825

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20200825

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20201029

Year of fee payment: 16

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 602005013870

Country of ref document: DE

REG Reference to a national code

Ref country code: NL

Ref legal event code: MM

Effective date: 20210901

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20210831

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20210801

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20210901

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20210801

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220301

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20210831