EP0392590B1 - Verfahren zur Umwandlung einer Kohlenwasserstoffbeschickung - Google Patents

Verfahren zur Umwandlung einer Kohlenwasserstoffbeschickung Download PDF

Info

Publication number
EP0392590B1
EP0392590B1 EP19900200788 EP90200788A EP0392590B1 EP 0392590 B1 EP0392590 B1 EP 0392590B1 EP 19900200788 EP19900200788 EP 19900200788 EP 90200788 A EP90200788 A EP 90200788A EP 0392590 B1 EP0392590 B1 EP 0392590B1
Authority
EP
European Patent Office
Prior art keywords
catalyst
feedstock
process according
olefins
metal
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 - Lifetime
Application number
EP19900200788
Other languages
English (en)
French (fr)
Other versions
EP0392590A1 (de
Inventor
Ian Ernest Maxwell
Jaydeep Biswas
Johannes Petrus Van Den Berg
Jaap Erik Naber
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.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
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 Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of EP0392590A1 publication Critical patent/EP0392590A1/de
Application granted granted Critical
Publication of EP0392590B1 publication Critical patent/EP0392590B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • C10G57/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
    • C10G57/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process with polymerisation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Claims (9)

  1. Ein Verfahren zur Umwandlung eines kohlenwasserstoffhaltigen Ausgangsmaterials, umfassend die folgenden Stufen:
    (i) Kontaktieren des Ausgangsmaterials bei einer Temperatur von mindestens 400°C und während weniger als 10 Sekunden mit einem festen Crackkatalysator,
    (ii) Abtrennen einer Fraktion aus dem Abstrom der Stufe (i), welche ein oder mehrere C₂- bis C₆-Olefine enthält,
    (iii) Kontaktieren mindestens einer Teilmenge besagter C₂- bis C₆-Olefine enthaltenden Fraktion mit einem Oligomerisierungskatalysator unter Oligomerisierungsbedingungen bei einer Temperatur von 150 bis 330°C, einem Druck von 1 bis 100 bar und einer Raumgeschwindigkeit von 0,1 bis 10 kg Olefinzuspeisung/kg Katalysator je Stunde und
    (iv) Rückführung mindestens einer Teilmenge des Abstromes von Stufe (iii) in die Stufe (i).
  2. Ein Verfahren nach Anspruch 1, in welchem der in Stufe (i) eingesetzte feste Crackkatalysator mindestens einen Zeolith mit einem Porendurchmesser von 0,3 bis 0,7 nm umfaßt.
  3. Ein Verfahren nach Anspruch 2, in welchem der mindestens eine Zeolith ausgewählt ist aus kristallinen Metallsilikaten mit einer ZSM-5-Struktur, Ferrierit, Erionit und Mischungen davon.
  4. Ein Verfahren nach irgendeinem der vorhergehenden Ansprüche, in welchem das Ausgangsmaterial in Stufe (i) mit einem Fließbett des festen Crackkatalysators kontaktiert wird.
  5. Ein Verfahren nach irgendeinem der vorhergehenden Ansprüche, in welchem das Ausgangsmaterial in Stufe (i) während 0,2 bis 6 Sekunden mit dem festen Crackkatalysator kontaktiert wird.
  6. Ein Verfahren nach irgendeinem der vorhergehenden Ansprüche, in welchem die Kontakttemperatur in Stufe (i) im Bereich von 500 bis 750°C liegt.
  7. Ein Verfahren nach irgendeinem der vorhergehenden Ansprüche, in welchem das Gewichtsverhältnis von Katalysator zu Ausgangsmaterial in Stufe (i) im Bereich von 20:1 bis 100:1 liegt.
  8. Ein Verfahren nach irgendeinem der vorhergehenden Ansprüche, bei welchem es sich bei dem in der Stufe (iii) eingesetzten Oligomerisierungskatalysator um einen festen Oligomerisierungskatalysator handelt, welcher mindestens ein Metall ausgewählt aus den Gruppen 1b, 2a, 2b, 3a, 4b, 5b, 6b und 8, sowie ein kristallines Silikat eines dreiwertigen Metalls enthält.
  9. Ein Verfahren nach Anspruch 8, wobei das Metall Nickel ist und das kristalline Silikat ein Mordenit ist.
EP19900200788 1989-04-11 1990-03-30 Verfahren zur Umwandlung einer Kohlenwasserstoffbeschickung Expired - Lifetime EP0392590B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB898908081A GB8908081D0 (en) 1989-04-11 1989-04-11 Process for the conversion of a hydrocarbonaceous feedstock
GB8908081 1989-04-11

Publications (2)

Publication Number Publication Date
EP0392590A1 EP0392590A1 (de) 1990-10-17
EP0392590B1 true EP0392590B1 (de) 1993-03-10

Family

ID=10654770

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19900200788 Expired - Lifetime EP0392590B1 (de) 1989-04-11 1990-03-30 Verfahren zur Umwandlung einer Kohlenwasserstoffbeschickung

Country Status (7)

Country Link
EP (1) EP0392590B1 (de)
JP (1) JPH02298585A (de)
AU (1) AU618464B2 (de)
CA (1) CA2014153A1 (de)
DE (1) DE69001035T2 (de)
ES (1) ES2054214T3 (de)
GB (1) GB8908081D0 (de)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9114390D0 (en) * 1991-07-03 1991-08-21 Shell Int Research Hydrocarbon conversion process and catalyst composition
JPH06220461A (ja) * 1993-01-22 1994-08-09 Mazda Motor Corp 廃プラスチック又はゴム材から炭化水素油を得る方法及びその実施に使用される装置
FR2968010B1 (fr) * 2010-11-25 2014-03-14 Ifp Energies Now Procede de conversion d'une charge lourde en distillat moyen
US9914884B2 (en) 2013-12-17 2018-03-13 Uop Llc Process and apparatus for recovering oligomerate
US9732285B2 (en) 2013-12-17 2017-08-15 Uop Llc Process for oligomerization of gasoline to make diesel
US9670425B2 (en) 2013-12-17 2017-06-06 Uop Llc Process for oligomerizing and cracking to make propylene and aromatics
US9387413B2 (en) 2013-12-17 2016-07-12 Uop Llc Process and apparatus for recovering oligomerate
CN112654690A (zh) * 2018-09-06 2021-04-13 沙特基础全球技术有限公司 使用多级径向流移动床反应器系统催化裂化石脑油的方法

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB513545A (en) * 1938-04-12 1939-10-16 Standard Oil Co Indiana Improvements relating to the conversion of mineral oils into gasoline
CN1021913C (zh) * 1988-06-16 1993-08-25 国际壳牌研究有限公司 使烃类原料转化的方法
GB8814292D0 (en) * 1988-06-16 1988-07-20 Shell Int Research Process for conversion of hydrocarbonaceous feedstock

Also Published As

Publication number Publication date
DE69001035T2 (de) 1993-07-01
AU5306490A (en) 1990-10-18
JPH02298585A (ja) 1990-12-10
CA2014153A1 (en) 1990-10-11
GB8908081D0 (en) 1989-05-24
DE69001035D1 (de) 1993-04-15
EP0392590A1 (de) 1990-10-17
AU618464B2 (en) 1991-12-19
ES2054214T3 (es) 1994-08-01

Similar Documents

Publication Publication Date Title
EP0418370B1 (de) Verfahren zur herstellung von alkylaromatischen kohlenwasserstoffen
EP0372632B1 (de) Kohlenwasserstoffumwandlungsverfahren
US5702589A (en) Process for converting olefinic hydrocarbons using spent FCC catalyst
US4966680A (en) Integrated catalytic cracking process with light olefin upgrading
AU620840B2 (en) Two-stage process for conversion of alkanes to gasoline
EP0426400B1 (de) Qualitätserhöhung von leichtem olefinischen Heizgas in einem Reaktor mit fluidisiertem Katalysator sowie Regenerierung des Katalysators
EP0259156A1 (de) Verfahren zur katalytischen Wirbelschichtspaltung mit reaktiven Bruchstücken
EP0347003B1 (de) Verfahren zur Umwandlung einer Kohlenwasserstoffhaltigen Fraktion
US5049360A (en) Multi-stage conversion of alkanes to gasoline
US5152883A (en) Process for the production of improved octane numbers gasolines
US5069776A (en) Process for the conversion of a hydrocarbonaceous feedstock
US4956075A (en) Catalytic cracking
US5009851A (en) Integrated catalytic reactor system with light olefin upgrading
US5000837A (en) Multistage integrated process for upgrading olefins
US3993556A (en) Method of catalytic cracking of hydrocarbons
US4032432A (en) Conversions of hydrocarbons
KR20050115873A (ko) 프로필렌을 생성하기 위한 유체 접촉 분해 유니트에서ｃ6의 재순환
EP0490435B1 (de) Verfahren zur Herstellung eines Olefine enthaltenden Kohlenwasserstoffgemisches
EP0392590B1 (de) Verfahren zur Umwandlung einer Kohlenwasserstoffbeschickung
EP0349036B1 (de) Verfahren zur Umwandlung eines kohlenwasserstoffartigen Ausgangsmaterials
US5234575A (en) Catalytic cracking process utilizing an iso-olefin enhancer catalyst additive
EP0385538B1 (de) Verfahren zur Umwandlung von Kohlenwasserstoffen
CA1300541C (en) Integrated process for gasoline production
EP0436253A1 (de) Verfahren zur Aufbereitung von leichten Kohlenwasserstofföldestillaten
RU2039790C1 (ru) Способ получения высокооктановых бензиновых фракций и ароматических углеводородов

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): BE DE ES FR GB IT NL

17P Request for examination filed

Effective date: 19901220

17Q First examination report despatched

Effective date: 19910808

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): BE DE ES FR GB IT NL

ITF It: translation for a ep patent filed

Owner name: ING. C. GREGORJ S.P.A.

REF Corresponds to:

Ref document number: 69001035

Country of ref document: DE

Date of ref document: 19930415

ET Fr: translation filed
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
REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2054214

Country of ref document: ES

Kind code of ref document: T3

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

Ref country code: FR

Payment date: 19970124

Year of fee payment: 8

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

Ref country code: GB

Payment date: 19970211

Year of fee payment: 8

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

Ref country code: BE

Payment date: 19970305

Year of fee payment: 8

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

Ref country code: ES

Payment date: 19970321

Year of fee payment: 8

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

Ref country code: NL

Payment date: 19970331

Year of fee payment: 8

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

Ref country code: DE

Payment date: 19970408

Year of fee payment: 8

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: 19980330

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

Ref country code: FR

Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY

Effective date: 19980331

Ref country code: ES

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 19980331

Ref country code: BE

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

Effective date: 19980331

BERE Be: lapsed

Owner name: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.

Effective date: 19980331

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: 19981001

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

Effective date: 19980330

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19981001

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

Ref country code: DE

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

Effective date: 19981201

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20000301

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

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 20050330