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FR2984916B1 - IMPROVED METHOD OF CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE USING UP-TO-THE-END PRETREATMENT OF THE CATALYTIC CRACKING UNIT - Google Patents

IMPROVED METHOD OF CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE USING UP-TO-THE-END PRETREATMENT OF THE CATALYTIC CRACKING UNIT

Info

Publication number
FR2984916B1
FR2984916B1 FR1104082A FR1104082A FR2984916B1 FR 2984916 B1 FR2984916 B1 FR 2984916B1 FR 1104082 A FR1104082 A FR 1104082A FR 1104082 A FR1104082 A FR 1104082A FR 2984916 B1 FR2984916 B1 FR 2984916B1
Authority
FR
France
Prior art keywords
catalytic cracking
cracking unit
converting
improved method
heavy load
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.)
Active
Application number
FR1104082A
Other languages
French (fr)
Other versions
FR2984916A1 (en
Inventor
Frederic Feugnet
Francois Hugues
Natacha Touchais
Hugues Dulot
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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
Priority to FR1104082A priority Critical patent/FR2984916B1/en
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Priority to PCT/FR2012/000483 priority patent/WO2013093227A1/en
Priority to CN201280063808.3A priority patent/CN103998575B/en
Priority to BR112014014892-9A priority patent/BR112014014892B1/en
Priority to MYPI2014701483A priority patent/MY170286A/en
Priority to KR1020147020595A priority patent/KR101958512B1/en
Priority to RU2014130209/04A priority patent/RU2601414C2/en
Priority to TW101149151A priority patent/TWI575063B/en
Publication of FR2984916A1 publication Critical patent/FR2984916A1/en
Application granted granted Critical
Publication of FR2984916B1 publication Critical patent/FR2984916B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking in the absence of hydrogen
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • 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
    • C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
    • 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
    • C10G67/06—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 a sorption process as the refining step in the absence of hydrogen
    • 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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
    • C10G69/126—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step polymerisation, e.g. oligomerisation

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)

Abstract

The present invention describes an improved process for converting a heavy feedstock that makes it possible to improve the selectivity for middle distillates. The invention consists in the implementation of a hydrotreatment or hydroconversion process, referred to as pretreatment process, of the heavy feedstock upstream of the assembly of a catalytic cracking unit followed by an oligomerization unit which makes it possible to increase the net production of C3, C4 and light petrol cuts at the end of the catalytic cracking unit and consequently to very significantly increase the production of middle distillates after the oligomerization step, and also the selectivity of middle distillates over petrol.
FR1104082A 2011-12-23 2011-12-23 IMPROVED METHOD OF CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE USING UP-TO-THE-END PRETREATMENT OF THE CATALYTIC CRACKING UNIT Active FR2984916B1 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
FR1104082A FR2984916B1 (en) 2011-12-23 2011-12-23 IMPROVED METHOD OF CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE USING UP-TO-THE-END PRETREATMENT OF THE CATALYTIC CRACKING UNIT
CN201280063808.3A CN103998575B (en) 2011-12-23 2012-11-23 Use pretreatment that heavy charge is converted into the improved method of intermediate oil in catalytic cracking unit upstream
BR112014014892-9A BR112014014892B1 (en) 2011-12-23 2012-11-23 IMPROVED PROCESS OF CONVERSION OF A HEAVY LOAD IN MEDIUM DISTILLATE, APPEALING FOR A PRE-TREATMENT AMOUNT OF THE CATALYTIC CRACKING UNIT
MYPI2014701483A MY170286A (en) 2011-12-23 2012-11-23 Improved process for converting a heavy feedstock into middle distillates using a pretreatment upstream of the catalytic cracking unit
PCT/FR2012/000483 WO2013093227A1 (en) 2011-12-23 2012-11-23 Improved process for converting a heavy feedstock into middle distillates using a pretreatment upstream of the catalytic cracking unit
KR1020147020595A KR101958512B1 (en) 2011-12-23 2012-11-23 Improved process for converting a heavy feedstock into middle distillates using a pretreatment upstream of the catalytic cracking unit
RU2014130209/04A RU2601414C2 (en) 2011-12-23 2012-11-23 Improved method of heavy raw material converting into middle distillates with preliminary treatment before supply to catalytic cracking plant
TW101149151A TWI575063B (en) 2011-12-23 2012-12-21 Improved process for converting a heavy feed into middle distillate using a pre-treatment upstream of the catalytic cracking unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR1104082A FR2984916B1 (en) 2011-12-23 2011-12-23 IMPROVED METHOD OF CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE USING UP-TO-THE-END PRETREATMENT OF THE CATALYTIC CRACKING UNIT

Publications (2)

Publication Number Publication Date
FR2984916A1 FR2984916A1 (en) 2013-06-28
FR2984916B1 true FR2984916B1 (en) 2014-01-17

Family

ID=47553244

Family Applications (1)

Application Number Title Priority Date Filing Date
FR1104082A Active FR2984916B1 (en) 2011-12-23 2011-12-23 IMPROVED METHOD OF CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE USING UP-TO-THE-END PRETREATMENT OF THE CATALYTIC CRACKING UNIT

Country Status (8)

Country Link
KR (1) KR101958512B1 (en)
CN (1) CN103998575B (en)
BR (1) BR112014014892B1 (en)
FR (1) FR2984916B1 (en)
MY (1) MY170286A (en)
RU (1) RU2601414C2 (en)
TW (1) TWI575063B (en)
WO (1) WO2013093227A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018001920A1 (en) 2016-06-30 2018-01-04 IFP Energies Nouvelles Oligomerisation method using a zeolite catalyst and a catalyst comprising a silica-alumina

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EA039642B1 (en) * 2017-01-13 2022-02-21 Михайло Барильчук Method for oligomerization of c2-c10 olefins and complex unit for producing high-octane gasolines, diesel fractions or aromatic hydrocarbons from c1-c10 hydrocarbon fractions of various composition and oxygen-containing c1-c6 compounds using it
EP3360535A1 (en) 2017-02-13 2018-08-15 Total Marketing Services Novel emollient composition
EP3360947A1 (en) 2017-02-13 2018-08-15 Total Marketing Services Process for the production of isoparaffinic fluids with low aromatics content
RU2673558C1 (en) * 2018-08-15 2018-11-28 Федеральное автономное учреждение "25 Государственный научно-исследовательский институт химмотологии Министерства обороны Российской Федерации" Method of obtaining multigrade standardized diesel fuel
FR3089518B1 (en) 2018-12-10 2020-11-20 Ifp Energies Now IMPROVED PROCESS FOR CONVERTING A HEAVY LOAD INTO MEDIUM DISTILLATES USING A CHAIN OF HYDROCRACKING, VAPOCRAQUAGE AND OLIGOMERIZATION UNITS
FR3089519B1 (en) 2018-12-10 2020-11-20 Ifp Energies Now Improved process for converting a heavy feed to middle distillates using a chain of hydrocracking, catalytic cracking naphtha and oligomerization units
FR3091535B1 (en) * 2019-01-09 2021-01-08 Ifp Energies Now TWO-STAGE HYDROCRACKING PROCESS INCLUDING A HYDROGENATION STAGE DOWNSTREAM OF THE SECOND HYDROCRACKING STAGE FOR THE PRODUCTION OF MEDIUM DISTILLATES
CN111718754B (en) * 2019-03-22 2021-11-16 中国石油化工股份有限公司 Method and system for producing gasoline and propylene
RU2736084C1 (en) * 2019-10-10 2020-11-11 Публичное акционерное общество "Славнефть-Ярославнефтеоргсинтез", (ПАО "Славнефть-ЯНОС") Method for production of all-year unified diesel fuel

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2837213B1 (en) * 2002-03-15 2004-08-20 Inst Francais Du Petrole PROCESS FOR THE JOINT PRODUCTION OF PROPYLENE AND GASOLINE FROM A RELATIVELY HEAVY LOAD
US20040267070A1 (en) * 2003-06-30 2004-12-30 Chevron U.S.A. Inc. Hydrotreating of Fischer-Tropsch derived feeds prior to oligomerization using an ionic liquid catalyst
FR2871167B1 (en) * 2004-06-04 2006-08-04 Inst Francais Du Petrole METHOD FOR IMPROVING ESSENTIAL CUPS AND GAS PROCESSING
FR2879620B1 (en) * 2004-12-21 2007-02-23 Inst Francais Du Petrole PROCESS FOR THE DIRECT CONVERSION OF A CHARGE COMPRISING FOUR AND / OR FIVE ATOMIC CARBON OLEFINS FOR THE PRODUCTION OF PROPYLENE WITH CO-PRODUCTION OF GASOLINE
FR2886941B1 (en) * 2005-06-09 2010-02-12 Inst Francais Du Petrole SOFT HYDROCRACKING PROCESS INCLUDING DILUTION OF THE LOAD
CN101506334B (en) * 2006-07-19 2012-10-03 环球油品公司 A hydrocarbon desulfurization process
WO2008144782A2 (en) * 2007-05-21 2008-11-27 Sasol Technology (Pty) Ltd Fischer-tropsch gasoline process
FR2935377B1 (en) * 2008-08-29 2013-02-15 Inst Francais Du Petrole PROCESS FOR CONVERTING A HEAVY FUEL AND PROPYLENE LOAD HAVING A MODULATE YIELD STRUCTURE
FR2952646B1 (en) * 2009-11-13 2012-09-28 Inst Francais Du Petrole PROCESS FOR THE PRODUCTION OF HIGH QUALITY KEROSENE AND DIESEL FUELS AND COPRODUCTION OF HYDROGEN FROM LIGHT SATURATED CUTS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018001920A1 (en) 2016-06-30 2018-01-04 IFP Energies Nouvelles Oligomerisation method using a zeolite catalyst and a catalyst comprising a silica-alumina

Also Published As

Publication number Publication date
CN103998575B (en) 2016-08-17
RU2601414C2 (en) 2016-11-10
FR2984916A1 (en) 2013-06-28
BR112014014892B1 (en) 2020-09-15
RU2014130209A (en) 2016-02-10
WO2013093227A1 (en) 2013-06-27
TW201333180A (en) 2013-08-16
KR20140116138A (en) 2014-10-01
MY170286A (en) 2019-07-16
BR112014014892A2 (en) 2017-06-13
CN103998575A (en) 2014-08-20
KR101958512B1 (en) 2019-03-14
TWI575063B (en) 2017-03-21

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