ATE200511T1 - METHOD AND DEVICE FOR CONVERSING A HYDROCARBON FEED USING TWO HYDROGEN TREATMENT REACTORS AND A SINGLE FRACTIONATION PLANT - Google Patents

METHOD AND DEVICE FOR CONVERSING A HYDROCARBON FEED USING TWO HYDROGEN TREATMENT REACTORS AND A SINGLE FRACTIONATION PLANT

Info

Publication number
ATE200511T1
ATE200511T1 AT97401730T AT97401730T ATE200511T1 AT E200511 T1 ATE200511 T1 AT E200511T1 AT 97401730 T AT97401730 T AT 97401730T AT 97401730 T AT97401730 T AT 97401730T AT E200511 T1 ATE200511 T1 AT E200511T1
Authority
AT
Austria
Prior art keywords
effluents
conversing
hydrocarbon feed
reactors
hydrogen treatment
Prior art date
Application number
AT97401730T
Other languages
German (de)
Inventor
Pierre Crespin
Laurent Mariette
Original Assignee
Total Raffinage Distribution
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 Total Raffinage Distribution filed Critical Total Raffinage Distribution
Application granted granted Critical
Publication of ATE200511T1 publication Critical patent/ATE200511T1/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
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
    • 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
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps

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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

A process for the conversion by hydrotreatment of a hydrocarbon charge is carried out in conversion reactions (10, 110, 104, 114) and a single fractionation unit (12) arranged between them, in which both effluents of the two reactors are fractionated. The effluents of both reactors (10, 14) are recovered within two separate zones (24, 26) of the fractionator. The fractions of the effluents vapourised in (12) are re-condensed and withdrawn from a common zone (34) of the unit. Two separate withdrawals (18, 28) are effected on the distillation residues from the zones (24, 26) of the fractionation unit in which the effluents from (10, 14) are treated. The effluent from the first reactor (10) is collected in a zone (24) whilst the withdrawal (18) of distillation residues from this zone are directed to the inlet of the second reactor (14). Also claimed is the installation for effecting this process.
AT97401730T 1996-07-19 1997-07-17 METHOD AND DEVICE FOR CONVERSING A HYDROCARBON FEED USING TWO HYDROGEN TREATMENT REACTORS AND A SINGLE FRACTIONATION PLANT ATE200511T1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9609090A FR2751339B1 (en) 1996-07-19 1996-07-19 PROCESS AND DEVICE FOR CONVERTING A HYDROCARBON LOAD, USING TWO HYDROTREATMENT REACTORS AND A SINGLE FRACTIONATION UNIT

Publications (1)

Publication Number Publication Date
ATE200511T1 true ATE200511T1 (en) 2001-04-15

Family

ID=9494248

Family Applications (1)

Application Number Title Priority Date Filing Date
AT97401730T ATE200511T1 (en) 1996-07-19 1997-07-17 METHOD AND DEVICE FOR CONVERSING A HYDROCARBON FEED USING TWO HYDROGEN TREATMENT REACTORS AND A SINGLE FRACTIONATION PLANT

Country Status (5)

Country Link
EP (1) EP0819752B1 (en)
AT (1) ATE200511T1 (en)
DE (1) DE69704519T2 (en)
ES (1) ES2157537T3 (en)
FR (1) FR2751339B1 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2757872B1 (en) * 1996-12-31 1999-06-25 Total Raffinage Distribution PROCESS FOR HYDROTREATING A HYDROCARBON CHARGE AND DEVICE FOR IMPLEMENTING SAME
CN102639679B (en) 2009-12-01 2016-05-11 埃克森美孚研究工程公司 Use the two stages hydrogenation processing of dividing wall column fractionator
US9290703B2 (en) 2010-04-23 2016-03-22 Exxonmobil Research And Engineering Company Low pressure production of low cloud point diesel
AU2011280067A1 (en) * 2010-06-30 2013-01-10 Exxonmobil Research And Engineering Company Integrated gas and liquid phase processing of biocomponent feedstocks
SG186733A1 (en) 2010-06-30 2013-02-28 Exxonmobil Res & Eng Co Two stage hydroprocessing with divided wall column fractionator
SG185577A1 (en) 2010-06-30 2012-12-28 Exxonmobil Res & Eng Co Gas and liquid phase hydroprocessing for biocomponent feedstocks
SG10201503121SA (en) 2010-06-30 2015-06-29 Exxonmobil Res & Eng Co Liquid phase distillate dewaxing
US9028673B2 (en) 2011-11-09 2015-05-12 Exxonmobil Research And Engineering Company Production of low cloud point distillates

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB394858A (en) * 1932-03-08 1933-07-06 Lummus Co Improvements in or relating to methods of and apparatus for dividing petroleum bottoms
US3437584A (en) * 1967-08-09 1969-04-08 Universal Oil Prod Co Method for converting heavy carbonaceous materials
US4713167A (en) * 1986-06-20 1987-12-15 Uop Inc. Multiple single-stage hydrocracking process

Also Published As

Publication number Publication date
EP0819752B1 (en) 2001-04-11
DE69704519T2 (en) 2001-08-09
EP0819752A1 (en) 1998-01-21
ES2157537T3 (en) 2001-08-16
DE69704519D1 (en) 2001-05-17
FR2751339A1 (en) 1998-01-23
FR2751339B1 (en) 2003-08-08

Similar Documents

Publication Publication Date Title
MY114664A (en) Integrated distillate recovery process
DE60045600D1 (en) METHOD AND DEVICE FOR CATALYTIC CUTTING WITH UPWARD AND DOWNWARD PARALLEL REACTORS
ES534485A0 (en) PROCEDURE FOR PREPARING LIQUID HYDROCARBONS FROM USED TIRES AND WASTE OF CABLES, POLYETHYLENE AND-OR POLYPROPYLENE
DE69100770D1 (en) Process for hydrogen treatment of petroleum residue or heavy oil for refining and conversion to lighter cuts.
ID18612A (en) PURIFICATION OF CATALYTIC DESTILATION
MX9704351A (en) Process for the removal of mercaptans and hydrogen sulfide from hydrocarbon streams.
GB2301373B (en) Process for the conversion of heavy crude oils and distillation residues to distillates
CA1320168C (en) Process for separating hydroprocessed effluent streams
ATE176799T1 (en) METHOD FOR PRODUCING HIGH QUALITY BASE OIL INSERT FROM UNREACTED OIL FROM A HYDROCRACKING PLANT USING RECIRCULATED OPERATION
RU2004103461A (en) METHOD FOR PRODUCING MIDDLE DISTILLATES BY HYDROISOMERIZATION AND HYDROCRACKING IN TWO STAGES OF RAW MATERIAL OBTAINED BY FISHERATROPSH METHOD
KR970059263A (en) Two Stage Hydroprocessing Reaction with Continuous Recirculating Gas Flow
ATE200511T1 (en) METHOD AND DEVICE FOR CONVERSING A HYDROCARBON FEED USING TWO HYDROGEN TREATMENT REACTORS AND A SINGLE FRACTIONATION PLANT
FR2817767B1 (en) PROCESS AND PLANT FOR THE RECOVERY AND PURIFICATION OF ETHYLENE PRODUCED BY PYROLYSIS OF HYDROCARBONS, AND GASES OBTAINED BY PROCESS
ZA852505B (en) Process for producing hydrocarbons from biological sludge
CA1064171A (en) Treatment of aqueous waste
CA2330308A1 (en) Three stage cocurrent liquid and vapor hydroprocessing
DE3778303D1 (en) METHOD AND DEVICE FOR CONTINUOUS TREATMENT OF ALTOEL.
ATE271114T1 (en) METHOD AND DEVICE FOR CATALYTIC CRACKING USING DOWNFLOW AND UPFLOW REACTORS
MY115342A (en) Method of operating a sequencing batch reactors
KR930702473A (en) Hydrocracking Method by Removing Polycyclic Aromatic Dimer
US4116816A (en) Parallel hydrodesulfurization of naphtha and distillate streams with passage of distillate overhead as reflux to the naphtha distillation zone
NO173386C (en) Purification of 1,1-dichloro-1-fluoroethane
CA2423533A1 (en) Two stage hydroprocessing and stripping in a single reaction vessel
EP1157081A4 (en) Staged upflow and downflow hydroprocessing with noncatalytic removal of upflow stage vapor impurities
WO1993025483B1 (en) Treatment installation and method for treating water and/or gases

Legal Events

Date Code Title Description
RER Ceased as to paragraph 5 lit. 3 law introducing patent treaties