PL2209873T3 - Sposób hydrokonwersji ciężkich wsadów na złożu wrzącym z wtryskiem wsadu do głowicy reaktora - Google Patents

Sposób hydrokonwersji ciężkich wsadów na złożu wrzącym z wtryskiem wsadu do głowicy reaktora

Info

Publication number
PL2209873T3
PL2209873T3 PL08871299T PL08871299T PL2209873T3 PL 2209873 T3 PL2209873 T3 PL 2209873T3 PL 08871299 T PL08871299 T PL 08871299T PL 08871299 T PL08871299 T PL 08871299T PL 2209873 T3 PL2209873 T3 PL 2209873T3
Authority
PL
Poland
Prior art keywords
reactor
injection
hydroconversion
feedstock
ebullated bed
Prior art date
Application number
PL08871299T
Other languages
English (en)
Inventor
Thierry Gauthier
Jan Verstraete
Simon Maget
Original Assignee
Ifp Energies Now
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 Now filed Critical Ifp Energies Now
Publication of PL2209873T3 publication Critical patent/PL2209873T3/pl

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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
    • C10G47/26—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles suspended in the oil, e.g. slurries
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B01D19/0042—Degasification of liquids modifying the liquid flow
    • B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
    • B01D19/0057—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1872—Details of the fluidised bed reactor
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/10—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 with moving solid particles
    • C10G49/12—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 with moving solid particles suspended in the oil, e.g. slurries
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00548—Flow
    • B01J2208/00557—Flow controlling the residence time inside the reactor vessel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
PL08871299T 2007-11-12 2008-10-24 Sposób hydrokonwersji ciężkich wsadów na złożu wrzącym z wtryskiem wsadu do głowicy reaktora PL2209873T3 (pl)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR0707930A FR2923490B1 (fr) 2007-11-12 2007-11-12 Procede d'hydroconversion de charges lourdes en lit bouillonnant avec injection de la charge en tete de reacteur
EP08871299A EP2209873B1 (fr) 2007-11-12 2008-10-24 Procede d' hydroconversion de charges lourdes en lit bouillonnant avec injection de la charge en tete de reacteur
PCT/FR2008/001504 WO2009092877A1 (fr) 2007-11-12 2008-10-24 Procede dηydroconversion de charges lourdes en lit bouillonnant avec injection de la charge en tete de reacteur

Publications (1)

Publication Number Publication Date
PL2209873T3 true PL2209873T3 (pl) 2011-10-31

Family

ID=39494641

Family Applications (1)

Application Number Title Priority Date Filing Date
PL08871299T PL2209873T3 (pl) 2007-11-12 2008-10-24 Sposób hydrokonwersji ciężkich wsadów na złożu wrzącym z wtryskiem wsadu do głowicy reaktora

Country Status (11)

Country Link
US (1) US8961778B2 (pl)
EP (1) EP2209873B1 (pl)
AT (1) ATE513893T1 (pl)
CA (1) CA2702975C (pl)
FR (1) FR2923490B1 (pl)
MX (1) MX2010005038A (pl)
PL (1) PL2209873T3 (pl)
RU (1) RU2469071C2 (pl)
SA (1) SA08290719B1 (pl)
TW (1) TWI433922B (pl)
WO (1) WO2009092877A1 (pl)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2923490B1 (fr) 2007-11-12 2009-12-18 Inst Francais Du Petrole Procede d'hydroconversion de charges lourdes en lit bouillonnant avec injection de la charge en tete de reacteur
FR3000097B1 (fr) * 2012-12-20 2014-12-26 Ifp Energies Now Procede integre de traitement de charges petrolieres pour la production de fiouls a basse teneur en soufre
US20140221713A1 (en) * 2013-02-04 2014-08-07 Lummus Technology Inc. Residue hydrocracking processing
US9650312B2 (en) 2013-03-14 2017-05-16 Lummus Technology Inc. Integration of residue hydrocracking and hydrotreating
FR3027911B1 (fr) * 2014-11-04 2018-04-27 IFP Energies Nouvelles Procede de conversion de charges petrolieres comprenant une etape d'hydrocraquage en lit bouillonnant, une etape de maturation et une etape de separation des sediments pour la production de fiouls a basse teneur en sediments
FR3045649A1 (fr) * 2015-12-21 2017-06-23 Ifp Energies Now Procede de conversion de charges petrolieres comprenant une etape d'hydrocraquage en lit bouillonnant integrant un systeme de tri de catalyseur
CN109516518B (zh) * 2018-12-11 2023-09-29 华北水利水电大学 一种用于生物制氢过程含气高粘度液体的气液分离装置
US11434438B2 (en) * 2020-01-13 2022-09-06 Kellogg Brown & Root Llc Slurry phase reactor with internal vapor-liquid separator
IT202200016413A1 (it) * 2022-08-02 2024-02-02 Luigi Patron Reattore upflow ad alta capacità di idrogenazione per idroconvertire oli pesanti a idrocarburi leggeri
CN115672202A (zh) * 2022-11-16 2023-02-03 中国海洋石油集团有限公司 一种自换热式加氢反应器及其加氢方法
US20240157274A1 (en) * 2022-11-16 2024-05-16 Chevron U.S.A. Inc. Gas-liquid separation device for an ebullated bed reactor
FI131835B1 (en) * 2024-06-27 2025-12-29 Neste Oyj FEED INJECTOR AND BUBBLING FLUID BED REACTOR CONFIGURATION AND HYDROCONVERSION PROCESS USING IT

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3888761A (en) * 1970-11-12 1975-06-10 Cities Service Res & Dev Co H-oil process
RU2173696C2 (ru) * 1996-09-23 2001-09-20 Каталитик Дистиллейшн Текнолоджиз Способ гидроконверсии
US5705052A (en) * 1996-12-31 1998-01-06 Exxon Research And Engineering Company Multi-stage hydroprocessing in a single reaction vessel
FR2773814B1 (fr) * 1998-01-16 2001-04-27 Inst Francais Du Petrole Procede de conversion de fractions lourdes petrolieres en lit bouillonnant, avec ajout de catalyseur pre-conditionne
US6280606B1 (en) * 1999-03-22 2001-08-28 Institut Francais Du Petrole Process for converting heavy petroleum fractions that comprise a distillation stage, ebullated-bed hydroconversion stages of the vacuum distillate, and a vacuum residue and a catalytic cracking stage
RU2173575C1 (ru) * 2000-06-05 2001-09-20 Галимов Жамиль Файзуллович Реактор для каталитического крекинга углеводородного сырья
US6755962B2 (en) * 2001-05-09 2004-06-29 Conocophillips Company Combined thermal and catalytic treatment of heavy petroleum in a slurry phase counterflow reactor
US7247235B2 (en) * 2003-05-30 2007-07-24 Abb Lummus Global Inc, Hydrogenation of middle distillate using a counter-current reactor
MXPA06012528A (es) * 2004-04-28 2007-08-02 Headwaters Heavy Oil Llc Metodos y sistemas de hidroprocesamiento de lecho ebullente y metodos para mejorar un sistema de lecho ebullente existente.
FR2923490B1 (fr) 2007-11-12 2009-12-18 Inst Francais Du Petrole Procede d'hydroconversion de charges lourdes en lit bouillonnant avec injection de la charge en tete de reacteur

Also Published As

Publication number Publication date
RU2010123789A (ru) 2011-12-20
MX2010005038A (es) 2010-05-27
TW200932889A (en) 2009-08-01
CA2702975A1 (fr) 2009-07-30
RU2469071C2 (ru) 2012-12-10
SA08290719B1 (ar) 2012-03-24
CA2702975C (fr) 2016-05-31
EP2209873A1 (fr) 2010-07-28
US20110036752A1 (en) 2011-02-17
FR2923490A1 (fr) 2009-05-15
TWI433922B (zh) 2014-04-11
EP2209873B1 (fr) 2011-06-22
ATE513893T1 (de) 2011-07-15
FR2923490B1 (fr) 2009-12-18
US8961778B2 (en) 2015-02-24
WO2009092877A1 (fr) 2009-07-30

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