[go: up one dir, main page]

HUP0101799A2 - Integrated hydroconversion process - Google Patents

Integrated hydroconversion process

Info

Publication number
HUP0101799A2
HUP0101799A2 HU0101799A HUP0101799A HUP0101799A2 HU P0101799 A2 HUP0101799 A2 HU P0101799A2 HU 0101799 A HU0101799 A HU 0101799A HU P0101799 A HUP0101799 A HU P0101799A HU P0101799 A2 HUP0101799 A2 HU P0101799A2
Authority
HU
Hungary
Prior art keywords
stream
reaction space
raw material
hydrogen
phase
Prior art date
Application number
HU0101799A
Other languages
Hungarian (hu)
Inventor
Martin J. Armstrong
Dennis R. Cash
Arthur J. Dahlberg
Hyung-Jae Yoon
Original Assignee
Chevron U.S.A. Inc.
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=27491380&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=HUP0101799(A2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Chevron U.S.A. Inc. filed Critical Chevron U.S.A. Inc.
Publication of HUP0101799A2 publication Critical patent/HUP0101799A2/en
Publication of HUP0101799A3 publication Critical patent/HUP0101799A3/en

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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

A találmány tárgya integrált hidrogénező konverziós eljárás. Lényege,hogy (a) első finomítóáram (85) és hidrogéndús gázfázisú elsőanyagáram (170) egyesítésével első nyersanyagot (105) hoznak létre;(b) az első nyersanyagot (105) forrponttartomány-konverzióteredményező feltételek között tartott első reakciótérbe (115) vezetik,és ott normál körülmények között folyadékfázisú és gázfázisúösszetevőket tartalmazó első reakciótérből (115) kilépő terméket (120)állítanak elő; (c) a normál körülmények között gázfázisú összetevőklegalább egy részét jelentős mértékű hűtés alkalmazása nélkül másodikfinomítóárammal (5) való elegyítéshez továbbvezetik, és így másodiknyersanyagot (15) hoznak létre; (d) a második nyersanyagot (15) amásodik finomítóáramban (5) jelen lévő aromás vegyületek legalább egyrészének konverzióját eredményező feltételek között tartott másodikreakciótérbe (20) vezetik, és ott második reakciótérből (20) kilépőterméket (25) állítanak elő; (e) a második reakciótér (20) kilépőtermékét (25) legalább egy második hidrogéndús gázáramra (150),valamint második folyadékáramra (35) választják szét; és (f) a másodikhidrogéndús gázáram (150) legalább egy részét az első reakciótérhez(115) visszavezetik. ÓThe subject of the invention is an integrated hydrogenation conversion process. The essence is that (a) a first refinery stream (85) and a hydrogen-rich gas-phase first material stream (170) are combined to create a first raw material (105); (b) the first raw material (105) is led to a first reaction space (115) held under boiling point conversion producing conditions, and there, under normal conditions, a product (120) leaving the first reaction space (115) containing liquid-phase and gas-phase components is produced; (c) at least a portion of the normally gas-phase components are passed on for mixing with a second refining stream (5) without applying a significant amount of cooling, thus creating a second raw material (15); (d) the second raw material (15) is led into the second reaction space (20) kept under conditions resulting in the conversion of at least a part of the aromatic compounds present in the second refining stream (5), and there an exit product (25) is produced from the second reaction space (20); (e) the exit product (25) of the second reaction space (20) is separated into at least a second hydrogen-rich gas stream (150) as well as a second liquid stream (35); and (f) at least a portion of the second hydrogen-rich gas stream (150) is returned to the first reaction space (115). HE

HU0101799A 1998-03-14 1999-01-08 Integrated hydroconversion process HUP0101799A3 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US7801998P 1998-03-14 1998-03-14
US7801298P 1998-03-14 1998-03-14
US7801198P 1998-03-14 1998-03-14
US8335998P 1998-04-28 1998-04-28
PCT/US1999/000478 WO1999047626A1 (en) 1998-03-14 1999-01-08 Integrated hydroconversion process with reverse hydrogen flow

Publications (2)

Publication Number Publication Date
HUP0101799A2 true HUP0101799A2 (en) 2001-10-28
HUP0101799A3 HUP0101799A3 (en) 2002-03-28

Family

ID=27491380

Family Applications (1)

Application Number Title Priority Date Filing Date
HU0101799A HUP0101799A3 (en) 1998-03-14 1999-01-08 Integrated hydroconversion process

Country Status (14)

Country Link
EP (1) EP1064343B1 (en)
JP (1) JP4383659B2 (en)
AR (1) AR014713A1 (en)
AU (1) AU761961B2 (en)
BR (1) BR9908753B1 (en)
CA (1) CA2323910A1 (en)
DE (1) DE69915599T2 (en)
DK (1) DK1064343T3 (en)
EA (1) EA200000945A1 (en)
ES (1) ES2218987T3 (en)
HU (1) HUP0101799A3 (en)
PL (1) PL189544B1 (en)
PT (1) PT1064343E (en)
WO (1) WO1999047626A1 (en)

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6589415B2 (en) 2001-04-04 2003-07-08 Chevron U.S.A., Inc. Liquid or two-phase quenching fluid for multi-bed hydroprocessing reactor
US6656342B2 (en) 2001-04-04 2003-12-02 Chevron U.S.A. Inc. Graded catalyst bed for split-feed hydrocracking/hydrotreating
US6583186B2 (en) 2001-04-04 2003-06-24 Chevron U.S.A. Inc. Method for upgrading Fischer-Tropsch wax using split-feed hydrocracking/hydrotreating
US6797154B2 (en) * 2001-12-17 2004-09-28 Chevron U.S.A. Inc. Hydrocracking process for the production of high quality distillates from heavy gas oils
US6702935B2 (en) * 2001-12-19 2004-03-09 Chevron U.S.A. Inc. Hydrocracking process to maximize diesel with improved aromatic saturation
US6709569B2 (en) 2001-12-21 2004-03-23 Chevron U.S.A. Inc. Methods for pre-conditioning fischer-tropsch light products preceding upgrading
AU2003219005A1 (en) 2002-03-06 2003-09-16 Exxonmobil Chemical Patents Inc. Improved hydrocarbon fluids
EP1342774A1 (en) 2002-03-06 2003-09-10 ExxonMobil Chemical Patents Inc. A process for the production of hydrocarbon fluids
US7300567B2 (en) * 2003-06-10 2007-11-27 Haldor Topsoe A/S Hydrotreating process
US8137531B2 (en) * 2003-11-05 2012-03-20 Chevron U.S.A. Inc. Integrated process for the production of lubricating base oils and liquid fuels from Fischer-Tropsch materials using split feed hydroprocessing
US7507326B2 (en) * 2003-11-14 2009-03-24 Chevron U.S.A. Inc. Process for the upgrading of the products of Fischer-Tropsch processes
US7763218B2 (en) 2005-09-26 2010-07-27 Haldor Topsoe A/S Partial conversion hydrocracking process and apparatus
WO2008035279A2 (en) * 2006-09-20 2008-03-27 Pt. Pertamina (Persero) Non-toxic mineral oil and its preparation process as drilling mud base material
WO2011061575A1 (en) 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
WO2011061576A1 (en) 2009-11-20 2011-05-26 Total Raffinage Marketing Process for the production of hydrocarbon fluids having a low aromatic content
US8945372B2 (en) * 2011-09-15 2015-02-03 E I Du Pont De Nemours And Company Two phase hydroprocessing process as pretreatment for tree-phase hydroprocessing process
FR3013357B1 (en) 2013-11-18 2016-09-16 Total Marketing Services PROCESS FOR THE PRODUCTION OF HYDROCARBON FLUIDS WITH LOW AROMATIC CONTENT
FR3015514B1 (en) 2013-12-23 2016-10-28 Total Marketing Services IMPROVED PROCESS FOR DESAROMATIZATION OF PETROLEUM CUTTERS
FR3023298B1 (en) 2014-07-01 2017-12-29 Total Marketing Services PROCESS FOR DESAROMATISATION OF PETROLEUM CUTTERS
JP6905056B2 (en) 2016-10-18 2021-07-21 マウェタール エルエルシー Fuel and its manufacturing method
KR102243784B1 (en) 2016-10-18 2021-04-22 모에탈 엘엘씨 Use of environment-friendly marine fuel
CN110050056B (en) 2016-10-18 2022-04-08 马威特尔有限责任公司 Fuel composition of light dense oil and high sulfur fuel oil
EP3342842A1 (en) 2017-01-03 2018-07-04 Total Marketing Services Dewaxing and dearomating process of hydrocarbon in a slurry reactor
US12209223B2 (en) 2020-08-07 2025-01-28 Totalenergies Onetech Process for the production of fluids
FR3145000A1 (en) 2023-01-12 2024-07-19 Totalenergies Onetech PROCESS FOR PRODUCING FLUIDS

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3203889A (en) * 1962-11-01 1965-08-31 Universal Oil Prod Co Catalytic hydrocracking process with the preliminary hydrogenation of the aromatic containing feed oil
US3172836A (en) * 1962-12-28 1965-03-09 California Research Corp Hydrocarbon conversion process
US3328290A (en) * 1965-03-30 1967-06-27 Standard Oil Co Two-stage process for the hydrocracking of hydrocarbon oils in which the feed oil ispretreated in the first stage
US3475322A (en) * 1966-08-01 1969-10-28 Universal Oil Prod Co Hydrocracking process
US3364134A (en) * 1966-11-30 1968-01-16 Universal Oil Prod Co Black oil conversion and desulfurization process
US3494855A (en) * 1968-06-10 1970-02-10 Universal Oil Prod Co Desulfurization of high metal black oils
GB1270607A (en) * 1970-08-12 1972-04-12 Texaco Development Corp Production of motor and jet fuels
US3779897A (en) * 1971-12-29 1973-12-18 Texaco Inc Hydrotreating-hydrocracking process for manufacturing gasoline range hydrocarbons
US4011154A (en) * 1973-03-26 1977-03-08 Chevron Research Company Production of lubricating oils
US4082647A (en) * 1976-12-09 1978-04-04 Uop Inc. Simultaneous and continuous hydrocracking production of maximum distillate and optimum lube oil base stock
US5958218A (en) * 1996-01-22 1999-09-28 The M. W. Kellogg Company Two-stage hydroprocessing reaction scheme with series recycle gas flow
AU2215997A (en) * 1996-04-09 1997-10-29 Chevron U.S.A. Inc. Process for reverse staging in hydroprocessing reactor systems

Also Published As

Publication number Publication date
BR9908753A (en) 2000-12-26
JP4383659B2 (en) 2009-12-16
WO1999047626A1 (en) 1999-09-23
HUP0101799A3 (en) 2002-03-28
PT1064343E (en) 2004-07-30
PL342895A1 (en) 2001-07-16
JP2002506919A (en) 2002-03-05
AR014713A1 (en) 2001-03-28
ES2218987T3 (en) 2004-11-16
BR9908753B1 (en) 2010-07-13
DE69915599T2 (en) 2004-08-05
DE69915599D1 (en) 2004-04-22
AU2218299A (en) 1999-10-11
PL189544B1 (en) 2005-08-31
EP1064343A1 (en) 2001-01-03
CA2323910A1 (en) 1999-09-23
WO1999047626A9 (en) 1999-11-18
AU761961B2 (en) 2003-06-12
EA200000945A1 (en) 2001-04-23
DK1064343T3 (en) 2004-06-21
EP1064343B1 (en) 2004-03-17

Similar Documents

Publication Publication Date Title
HUP0101799A2 (en) Integrated hydroconversion process
DE69817653D1 (en) Processes for converting hydrocarbon inserts, catalytic emulsion and process for their production
NO994653L (en) Process for Autothermal Reform of a Hydrocarbon Raw Material Containing Higher Hydrocarbons
ZA88765B (en) Catalytic hydrogenation process
HUP9700197A1 (en) Two-stage hydroprocessing reaction scheme with series recycle gas flow
JPS61275101A (en) Manufacture of chemical substance
EP1103592A3 (en) Improved hydrocracking process
RU2010119514A (en) HYDROCRACKING METHOD
BR9907821A (en) Gas conversion process
RU99104506A (en) METHOD FOR HYDROCARBON CONVERSION
MY101222A (en) Process for the dehydrocyclodemerization of c3-c4 aliphatic hydrocarbons
AU2632902A (en) Improved hydroprocessing process and method of retrofitting existing hydroprocessing reactors
BR0207921A (en) Process for producing synthetic hydrocarbon products, and method for separating liquid from a liquid / solid mixture
JPH10245201A (en) Catalytic partial oxidation process of hydrocarbon ground substance and system for the same
BR9900758A (en) Process and installation for the combined production of a mixture of ammonia and carbon monoxide synthesis.
MX173396B (en) LIQUID PHASE HEAVY HYDROCARBON HYDROTREATMENT PROCEDURE
BR0015917A (en) Method and apparatus for manufacturing vinyl chloride and obtained vinyl chloride
ATE453607T1 (en) METHOD FOR PRODUCING OLIGOMERS OF ALKENES WITH 4 TO 8 CARBON ATOMS
BR0116914A (en) Process for the production of aldehydes
US3518166A (en) Hydrogen sulfide and ammonia recovery by degassing and plural distillation with ammonia recycle
ATE286527T1 (en) STEPPED UPFLOW AND DOWNFLOW HYDROGENATION WITH NON-CATALYTIC REMOVAL OF GAS STREAM CONTAMINANTS FROM UPFLOW HYDROGENATION
HUP9800232A2 (en) Process and plant for the production of urea with high conversion yield and low energy consumption
US6908602B1 (en) Hydrocarbon conversion process
JPS6220967B2 (en)
MX167932B (en) HYDROCONVERSION OF OIL USING PRE-ASPHALTENE ACID PRECIPITATION IN WASTE RECYCLING