DK3020788T3 - Fremgangsmåde for hvirvelpartikellagsreaktor til råmateriale der indeholder opløst hydrogen - Google Patents

Fremgangsmåde for hvirvelpartikellagsreaktor til råmateriale der indeholder opløst hydrogen Download PDF

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DK3020788T3
DK3020788T3 DK15192102.0T DK15192102T DK3020788T3 DK 3020788 T3 DK3020788 T3 DK 3020788T3 DK 15192102 T DK15192102 T DK 15192102T DK 3020788 T3 DK3020788 T3 DK 3020788T3
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hydrogen
reactor
feedstock
liquid
particle layer
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DK15192102.0T
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Omer Refa Koseoglu
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Saudi Arabian Oil Co
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    • 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
    • C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
    • C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
    • C10G67/14—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including at least two different refining steps in the absence of hydrogen
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/14—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles
    • C10G45/16—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles suspended in the oil, e.g. slurries
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/14—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles
    • C10G45/20—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with moving solid particles according to the "fluidised-bed" technique
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/22—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with hydrogen dissolved or suspended in the oil
    • 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
    • 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
    • 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
    • C10G47/30—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles according to the "fluidised-bed" technique
    • 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
    • B01J2208/00539—Pressure
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline
    • 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
    • C10G2400/04—Diesel oil

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Claims (12)

1. Fremgangsmåde til at omdanne et flydende råmateriale af carbonhydrider til carbonhydridforbindelser med lavere molekylvægt i en reaktor til katalytisk hydrogenbehandling i et hvirveldannende partikellag, hvilken reaktor med hvirvelpartikellaget indbefatter en ledning til internt at recirkulere nedstrømning, der er i fluidkommunikation med et i det væsentlige katalysatorfrit område over katalysatorpartikellaget for at lade flydende recirkuleret afløb passere fra hvirvelpartikellaget, hvilken fremgangsmåde omfatter: a) at blande det flydende råmateriale af carbonhydrider med et overskud af hydrogengas i en blandingszone for at opløse en del af hydrogengassen i det flydende råmateriale af carbonhydrider for at fremstille et hydrogenberiget flydende råmateriale af carbonhydrider; b) at transportere det hydrogenberigede flydende råmateriale af carbonhydrider og uopløst hydrogen til en flashzone, i hvilken mindst en del uopløst hydrogengas fordampes; c) at lade det hydrogenberigede flydende råmateriale af carbonhydrider passere fra flashzonen til indgangen af en pumpe til hvirvelpartikellaget; d) at lade det hydrogenberigede flydende råmateriale af carbonhydrider passerer fra pumpen til indløbet af hvirvelpartikellagsreaktoren for at blive omsat, hvilken omsætning indbefatter omdannelse af råmaterialet til carbonhydrider med lavere molekylvægt; e) at udvinde de omdannede carbonhyd rid produkter med lavere molekylvægt fra et i det væsentlige katalysatorfrit område af hvirvelpartikellagsreaktoren, og f) at lade det flydende recirkulerede afløb passere fra den interne recirkulationsledning i hvirvelpartikellagsreaktoren til blandingszonen for hydrogengas i trin (a) for at blande med det flydende råmateriale af carbonhydrider.
2. Fremgangsmåden ifølge krav 1, hvor gasindholdet i hvirvelpartikellagsreaktoren ligger i området på fra mindre end 40 vol.-% til 10 vol.-% af det totale væskevolumen.
3. Fremgangsmåden ifølge krav 1, hvor gasindholdet i hvirvelpartikellagsreaktoren er mindre end 1 vol.-%.
4. Fremgangsmåden ifølge krav 1, hvor recirkulationsstrømmen til hvirvelpartikellaget indeholder et volumen afdampe, der ligger i området på fra mindre end 10 vol.-% til mindre end 1 vol.-% af det totale væskevolumen.
5. Fremgangsmåden ifølge krav 1, hvor recirkulationsstrømmen til hvirvelpartikellaget indeholder et volumen afdampe, der er mindre end 1 vol.-% af det totale væskevolumen.
6. Fremgangsmåden ifølge krav 1, hvor hvirvelpartikellagsreaktoren drives ved en temperatur i området på fra 350 °C til 500 °C.
7. Fremgangsmåden ifølge krav 1, hvor hvirvelpartikellagsreaktoren drives ved en temperatur i området på fra 400 °C til 450 °C.
8. Fremgangsmåden ifølge krav 1, hvor hvirvelpartikellagsreaktoren drives ved et tryk i området på fra 50 til 300 kg/m2.
9. Fremgangsmåden ifølge krav 1, hvor hvirvelpartikellagsreaktoren drives ved et tryk i området på fra 100 til 250 kg/m2.
10. Fremgangsmåden ifølge krav 1, hvor hvirvelpartikellagsreaktoren drives ved et tryk i området på fra 150 til 200 kg/m2.
11. Fremgangsmåden ifølge krav 1, hvor blandings- og mætningszonen for hydrogen og råmateriale drives ved en hydrogenfødehastighed i området på fra 500 til 10.000 standard kubikfod pr. tønde (SCFB) (89 til 1780 m3/m3) råmateriale.
12. Fremgangsmåden ifølge krav 1, hvor blandings- og mætningszonen for hydrogen og råmateriale drives ved en hydrogenfødehastighed i området på fra 1.500 til 5.000 SCFB (267 til 890 m3/m3).
DK15192102.0T 2011-07-29 2012-07-24 Fremgangsmåde for hvirvelpartikellagsreaktor til råmateriale der indeholder opløst hydrogen DK3020788T3 (da)

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US201161513055P 2011-07-29 2011-07-29
EP12744152.5A EP2737023B1 (en) 2011-07-29 2012-07-24 Ebullated-bed process for feedstock containing dissolved hydrogen

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DK12744152.5T DK2737023T3 (da) 2011-07-29 2012-07-24 Fluid bed-fremgangsmåde for udgangsmateriale indeholdende opløst hydrogen
DK15192102.0T DK3020788T3 (da) 2011-07-29 2012-07-24 Fremgangsmåde for hvirvelpartikellagsreaktor til råmateriale der indeholder opløst hydrogen

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US (2) US8940155B2 (da)
EP (3) EP3020788B1 (da)
JP (2) JP6046136B2 (da)
KR (1) KR101885409B1 (da)
CN (1) CN103857771B (da)
DK (2) DK2737023T3 (da)
ES (2) ES2568004T3 (da)
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WO (1) WO2013019464A1 (da)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102016100341A1 (de) 2016-01-11 2017-07-13 Wincor Nixdorf International Gmbh Verfahren und Vorrichtung zur Depassivierung einer Batterie eines Wertbehälters
US9738839B1 (en) * 2016-04-29 2017-08-22 IFP Energies Nouvelles Generation ebullated-bed reactor system
RU2698815C1 (ru) 2016-10-18 2019-08-30 Маветал Ллс Очищенное турбинное топливо
CN114292666A (zh) 2016-10-18 2022-04-08 马威特尔有限责任公司 一种燃料以及减少排放的工艺过程
EP3529336A4 (en) 2016-10-18 2020-04-15 Mawetal LLC FUEL COMPOSITIONS OF LIGHT-TIGHT OILS AND FUEL OILS WITH A HIGH SULFUR CONTENT
CN106701160B (zh) * 2017-01-19 2019-04-30 上海竣铭化工工程设计有限公司 沸腾床加氢装置中循环泵的设置方法
US20180215683A1 (en) * 2017-01-27 2018-08-02 Saudi Arabian Oil Company Isomerization process using feedstock containing dissolved hydrogen
US11155757B2 (en) 2017-01-27 2021-10-26 Saudi Arabian Oil Company Isomerization process using feedstock containing dissolved hydrogen
CN108696842A (zh) * 2017-03-02 2018-10-23 北京小鸟听听科技有限公司 一种设备及其组网方法、输出方法
CN110756119A (zh) * 2018-07-27 2020-02-07 上海凯鑫分离技术股份有限公司 一种带有氢气分布器的连续加氢反应装置及工艺
US11084991B2 (en) * 2019-06-25 2021-08-10 Saudi Arabian Oil Company Two-phase moving bed reactor utilizing hydrogen-enriched feed
US11549069B1 (en) 2022-01-20 2023-01-10 Saudi Arabian Oil Company Two-phase hydroprocessing utilizing soluble hydrogen from the high pressure separator
US11965135B1 (en) 2023-04-12 2024-04-23 Saudi Arabian Oil Company Methods for reactivity based hydroprocessing

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2987465A (en) 1958-06-20 1961-06-06 Hydrocarbon Research Inc Gas-liquid contacting process
US3197288A (en) 1961-05-29 1965-07-27 Hydrocarbon Research Inc Catalytic reactor
DE1950640A1 (de) * 1968-10-10 1970-04-23 Chevron Res Verfahren zur Entfernung von Eisen aus Kohlenwasserstoffbeschickungen
US4670132A (en) * 1982-06-29 1987-06-02 Intevep, S.A. Method of hydrocracking and method of preparing a catalyst therefor
US4684456A (en) * 1985-12-20 1987-08-04 Lummus Crest Inc. Control of bed expansion in expanded bed reactor
US5219532A (en) * 1987-08-20 1993-06-15 Amoco Corporation Reduced gas holdup in catalytic reactor
US4971678A (en) * 1988-06-27 1990-11-20 Texaco Inc. Liquid inventory control in an ebullated bed process
US6270654B1 (en) * 1993-08-18 2001-08-07 Ifp North America, Inc. Catalytic hydrogenation process utilizing multi-stage ebullated bed reactors
US5624642A (en) * 1994-10-14 1997-04-29 Amoco Corporation Hydrocarbon processing apparatus
ZA961830B (en) * 1995-03-16 1997-10-31 Inst Francais Du Petrole Catalytic hydroconversion process for heavy petroleum feedstocks.
US7569136B2 (en) * 1997-06-24 2009-08-04 Ackerson Michael D Control system method and apparatus for two phase hydroprocessing
EP1299507B1 (en) * 2000-06-19 2006-01-04 Institut Francais Du Petrole Catalytic hydrogenation process utilizing multi-stage ebullated bed reactors
US6436279B1 (en) * 2000-11-08 2002-08-20 Axens North America, Inc. Simplified ebullated-bed process with enhanced reactor kinetics
US9669381B2 (en) * 2007-06-27 2017-06-06 Hrd Corporation System and process for hydrocracking
US8252169B2 (en) * 2008-12-16 2012-08-28 Macarthur James B Process for upgrading coal pyrolysis oils
CN102051207A (zh) 2009-10-27 2011-05-11 中国石油化工股份有限公司 一种悬浮床加氢技术的强化传质方法

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EP2737023B1 (en) 2016-03-02
ES2568004T3 (es) 2016-04-27
EP3147342A1 (en) 2017-03-29
EP3147342B1 (en) 2019-05-01
PL2737023T3 (pl) 2016-11-30
EP3020788B1 (en) 2017-09-13
US9315745B2 (en) 2016-04-19
WO2013019464A1 (en) 2013-02-07
KR101885409B1 (ko) 2018-08-03
US20150191663A1 (en) 2015-07-09
EP2737023A1 (en) 2014-06-04
JP6336538B2 (ja) 2018-06-06
US8940155B2 (en) 2015-01-27
JP2017052951A (ja) 2017-03-16
EP3020788A1 (en) 2016-05-18
US20130026068A1 (en) 2013-01-31
CN103857771A (zh) 2014-06-11
JP6046136B2 (ja) 2016-12-14
CN103857771B (zh) 2016-06-01
JP2014521774A (ja) 2014-08-28
PL3020788T3 (pl) 2018-02-28
DK2737023T3 (da) 2016-06-13
ES2650872T3 (es) 2018-01-22
KR20140064791A (ko) 2014-05-28

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