FR2968010B1 - Procede de conversion d'une charge lourde en distillat moyen - Google Patents
Procede de conversion d'une charge lourde en distillat moyenInfo
- Publication number
- FR2968010B1 FR2968010B1 FR1004585A FR1004585A FR2968010B1 FR 2968010 B1 FR2968010 B1 FR 2968010B1 FR 1004585 A FR1004585 A FR 1004585A FR 1004585 A FR1004585 A FR 1004585A FR 2968010 B1 FR2968010 B1 FR 2968010B1
- Authority
- FR
- France
- Prior art keywords
- middle distillate
- cut
- converting
- incorporated
- 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
Links
- 238000000034 method Methods 0.000 title abstract 3
- 150000001336 alkenes Chemical class 0.000 abstract 3
- 238000006384 oligomerization reaction Methods 0.000 abstract 2
- 125000004432 carbon atom Chemical group C* 0.000 abstract 1
- 238000004523 catalytic cracking Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 abstract 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
-
- 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
- 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
- C10G57/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
- C10G57/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process with polymerisation
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
-
- 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
- C10G2300/4006—Temperature
-
- 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
- C10G2300/4012—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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/06—Gasoil
-
- 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
- C10G2400/08—Jet fuel
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
La présente invention décrit un procédé de conversion d'une charge lourde permettant d'améliorer la sélectivité en distillat moyen. Le procédé fait appel à une unité de craquage catalytique suivie d'une ou plusieurs unités d'oligomérisation d'oléfines à nombre d'atomes de carbone allant de C2 à C9 permettant de produire préférentiellement une coupe additionnelle dite distillat moyen. La partie légère de l'oligomérat produit et non incorporable dans la coupe distillat moyen est recyclée au FCC pour être craquée en oléfines légères qui retournent aux unités d'oligomerisation en supplément des oléfines de la charge afin de former préférentiellement des oligomérats lourds incorporables à la coupe distillat moyen.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1004585A FR2968010B1 (fr) | 2010-11-25 | 2010-11-25 | Procede de conversion d'une charge lourde en distillat moyen |
PCT/FR2011/000589 WO2012069709A2 (fr) | 2010-11-25 | 2011-11-03 | Procede de conversion d'une charge lourde en distillat moyen. |
RU2013128868/04A RU2563655C2 (ru) | 2010-11-25 | 2011-11-03 | Способ конверсии тяжелой фракции в средний дистиллят |
CN201180056719.1A CN103221514B (zh) | 2010-11-25 | 2011-11-03 | 将重质原料转化成中间馏分的方法 |
US13/989,590 US10077218B2 (en) | 2010-11-25 | 2011-11-03 | Process for converting a heavy feed into middle distillate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1004585A FR2968010B1 (fr) | 2010-11-25 | 2010-11-25 | Procede de conversion d'une charge lourde en distillat moyen |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2968010A1 FR2968010A1 (fr) | 2012-06-01 |
FR2968010B1 true FR2968010B1 (fr) | 2014-03-14 |
Family
ID=44067859
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR1004585A Active FR2968010B1 (fr) | 2010-11-25 | 2010-11-25 | Procede de conversion d'une charge lourde en distillat moyen |
Country Status (5)
Country | Link |
---|---|
US (1) | US10077218B2 (fr) |
CN (1) | CN103221514B (fr) |
FR (1) | FR2968010B1 (fr) |
RU (1) | RU2563655C2 (fr) |
WO (1) | WO2012069709A2 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3089519A1 (fr) | 2018-12-10 | 2020-06-12 | IFP Energies Nouvelles | Procédé amélioré de conversion d’une charge lourde en distillats moyens faisant appel à un enchainement d’unités d’hydrocraquage, de craquage catalytique de naphta et d’oligomérisation |
FR3089518A1 (fr) | 2018-12-10 | 2020-06-12 | IFP Energies Nouvelles | Procede ameliore de conversion d’une charge lourde en distillats moyens faisant appel a un enchainement d’unites d’hydrocraquage, de vapocraquage et d’oligomerisation |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2986799B1 (fr) * | 2012-02-15 | 2015-02-06 | IFP Energies Nouvelles | Procede de conversion d'une charge lourde, mettant en oeuvre une unite de craquage catalytique et une etape d'hydrogenation selective de l'essence issue du craquage catalytique |
US10385279B2 (en) | 2014-03-25 | 2019-08-20 | Uop Llc | Process and apparatus for recycling cracked hydrocarbons |
US9181500B2 (en) | 2014-03-25 | 2015-11-10 | Uop Llc | Process and apparatus for recycling cracked hydrocarbons |
RU2692491C2 (ru) * | 2014-07-28 | 2019-06-25 | Сэсол Текнолоджи Пропрайэтери Лимитед | Получение промысловых углеводородов |
US20160137934A1 (en) * | 2014-11-19 | 2016-05-19 | Uop Llc | Flexible operation of oligomerization process |
CN106268932B (zh) * | 2015-06-09 | 2019-07-23 | 中国石油化工股份有限公司 | 一种催化裂化催化剂及其制备方法与应用 |
FR3045652B1 (fr) * | 2015-12-22 | 2018-01-12 | Axens | Procede de fractionnement pour un procede d'oligomerisation d'olefines legeres |
US20180171242A1 (en) * | 2016-12-15 | 2018-06-21 | Exxonmobil Research And Engineering Company | Efficient process for upgrading paraffins to gasoline |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3954600A (en) * | 1974-02-15 | 1976-05-04 | Exxon Research & Engineering Co. | Catalytic cracking process for producing middle distillate |
US4720600A (en) * | 1983-06-29 | 1988-01-19 | Mobil Oil Corporation | Production of middle distillate range hydrocarbons by light olefin upgrading |
US4822477A (en) * | 1987-06-11 | 1989-04-18 | Mobil Oil Corporation | Integrated process for gasoline production |
US5264115A (en) * | 1987-12-30 | 1993-11-23 | Compagnie De Raffinage Et De Distribution Total France | Process and apparatus for fluidized bed hydrocarbon conversion |
US4966680A (en) * | 1988-05-31 | 1990-10-30 | Mobil Oil Corporation | Integrated catalytic cracking process with light olefin upgrading |
GB8908081D0 (en) * | 1989-04-11 | 1989-05-24 | Shell Int Research | Process for the conversion of a hydrocarbonaceous feedstock |
FR2659346B1 (fr) * | 1990-03-09 | 1994-04-29 | Inst Francais Du Petrole | Procede de craquage avec oligomerisation ou trimerisation des olefines presentes dans les effluents. |
US5981818A (en) * | 1995-03-21 | 1999-11-09 | Stone & Webster Engineering Corp. | Integrated cracking and olefins derivative process utilizing dilute olefins |
FR2752567B1 (fr) * | 1996-08-23 | 1998-10-16 | Inst Francais Du Petrole | Zeolithe nu-88, son procede de preparation et ses applications catalytiques |
US5846403A (en) * | 1996-12-17 | 1998-12-08 | Exxon Research And Engineering Company | Recracking of cat naphtha for maximizing light olefins yields |
US20010035369A1 (en) * | 2000-03-23 | 2001-11-01 | Eduardo Mon | FCC process |
FR2837199B1 (fr) | 2002-03-15 | 2005-09-16 | Inst Francais Du Petrole | Procede de conversion en plusieurs etapes d'une charge comprenant des olefines a quatre, cinq atomes de carbone ou plus, en vue de produire du propylene |
FR2837213B1 (fr) | 2002-03-15 | 2004-08-20 | Inst Francais Du Petrole | Procede de production conjointe de propylene et d'essence a partir d'une charge relativement lourde |
AU2005274030B2 (en) * | 2004-08-10 | 2008-11-20 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for making a middle distillate product and lower olefins from a hydrocarbon feedstock |
US7582203B2 (en) * | 2004-08-10 | 2009-09-01 | Shell Oil Company | Hydrocarbon cracking process for converting gas oil preferentially to middle distillate and lower olefins |
US7902412B2 (en) * | 2007-07-23 | 2011-03-08 | Uop Llc | Use of olefin cracking to produce alkylate |
FR2935377B1 (fr) | 2008-08-29 | 2013-02-15 | Inst Francais Du Petrole | Procede de conversion d'une charge lourde en essence et en propylene presentant une structure de rendement modulable |
CN102448913B (zh) * | 2009-03-31 | 2015-01-28 | 环球油品公司 | 稀乙烯的低聚方法 |
-
2010
- 2010-11-25 FR FR1004585A patent/FR2968010B1/fr active Active
-
2011
- 2011-11-03 WO PCT/FR2011/000589 patent/WO2012069709A2/fr active Application Filing
- 2011-11-03 RU RU2013128868/04A patent/RU2563655C2/ru active
- 2011-11-03 US US13/989,590 patent/US10077218B2/en active Active
- 2011-11-03 CN CN201180056719.1A patent/CN103221514B/zh active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3089519A1 (fr) | 2018-12-10 | 2020-06-12 | IFP Energies Nouvelles | Procédé amélioré de conversion d’une charge lourde en distillats moyens faisant appel à un enchainement d’unités d’hydrocraquage, de craquage catalytique de naphta et d’oligomérisation |
FR3089518A1 (fr) | 2018-12-10 | 2020-06-12 | IFP Energies Nouvelles | Procede ameliore de conversion d’une charge lourde en distillats moyens faisant appel a un enchainement d’unites d’hydrocraquage, de vapocraquage et d’oligomerisation |
Also Published As
Publication number | Publication date |
---|---|
CN103221514A (zh) | 2013-07-24 |
FR2968010A1 (fr) | 2012-06-01 |
RU2563655C2 (ru) | 2015-09-20 |
CN103221514B (zh) | 2016-04-13 |
WO2012069709A2 (fr) | 2012-05-31 |
US10077218B2 (en) | 2018-09-18 |
RU2013128868A (ru) | 2014-12-27 |
WO2012069709A3 (fr) | 2012-12-20 |
US20130281749A1 (en) | 2013-10-24 |
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