MY174627A - A process for the utilisation of naphtha for the production of high octane gasoline - Google Patents

A process for the utilisation of naphtha for the production of high octane gasoline

Info

Publication number
MY174627A
MY174627A MYPI2014703781A MYPI2014703781A MY174627A MY 174627 A MY174627 A MY 174627A MY PI2014703781 A MYPI2014703781 A MY PI2014703781A MY PI2014703781 A MYPI2014703781 A MY PI2014703781A MY 174627 A MY174627 A MY 174627A
Authority
MY
Malaysia
Prior art keywords
sending
paraffins
catalytic reforming
cut
naphtha
Prior art date
Application number
MYPI2014703781A
Inventor
Heloise Dreux
Joana Fernandes
Eric Lemaire
Eric Sanchez
Original Assignee
Ifp Energies Now
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 Ifp Energies Now filed Critical Ifp Energies Now
Publication of MY174627A publication Critical patent/MY174627A/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
    • C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
    • 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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/06—Catalytic reforming characterised by the catalyst used
    • C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
    • C10G35/09—Bimetallic catalysts in which at least one of the metals is a platinum group metal
    • 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
    • C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • 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
    • C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • C10G59/06—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural parallel stages only
    • 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
    • C10G63/00—Treatment of naphtha by at least one reforming process and at least one other conversion process
    • 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
    • C10G63/00—Treatment of naphtha by at least one reforming process and at least one other conversion process
    • C10G63/02—Treatment of naphtha by at least one reforming process and at least one other conversion process plural serial stages only
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2400/30—Aromatics

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 concerns a process for the production of gasoline with an octane number of more than 95, starting form a naphtha cut (1) comprising paraffins and naphthenes, the process comprising the following steps: a) sending the naphtha cut (1) to a first catalytic reforming unit (2) in order to convert at least a portion of the paraffins and/or naphthenes into aromatic compounds and to produce hydrogen; b) withdrawing a first effluent (3) and a stream ofhydrogen (4) from the first catalytic reforming unit (2); c) sending the first effluent (3) to a separation unit (5) so as to separate a light hydrocarbon cut containing straight chain paraffins and a heavy hydrocarbon cut (7) containing unconverted paraffins and/or naphthenes; d) sending the light hydrocarbon cut to an isomerization unit (11) in order to produce an isomerate (12); e) sending the heavy hydrocarbon cut to a second catalytic reforming unit (8); f) withdrawing a reformate (10) containing aromatic compounds from the second catalytic reforming unit (8); Figure 1
MYPI2014703781A 2013-12-17 2014-12-12 A process for the utilisation of naphtha for the production of high octane gasoline MY174627A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR1362774A FR3014895B1 (en) 2013-12-17 2013-12-17 CATALYTIC REFORMING PROCESS

Publications (1)

Publication Number Publication Date
MY174627A true MY174627A (en) 2020-05-03

Family

ID=50029139

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2014703781A MY174627A (en) 2013-12-17 2014-12-12 A process for the utilisation of naphtha for the production of high octane gasoline

Country Status (5)

Country Link
KR (1) KR102366093B1 (en)
CN (1) CN104711017B (en)
FR (1) FR3014895B1 (en)
MY (1) MY174627A (en)
TW (1) TWI653329B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111925822A (en) * 2020-07-17 2020-11-13 中科合成油工程有限公司 Method for preparing high-octane gasoline and device for implementing method

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2935459A (en) * 1956-05-01 1960-05-03 Texaco Inc Hydrocarbon conversion process
GB823320A (en) * 1957-05-31 1959-11-11 Exxon Research Engineering Co Improvements in or relating to the reforming of petroleum naphthas
US5294328A (en) * 1990-05-24 1994-03-15 Uop Production of reformulated gasoline
US5135639A (en) * 1990-05-24 1992-08-04 Uop Production of reformulated gasoline
BE1006675A3 (en) * 1993-02-02 1994-11-16 Fina Research Method for producing species high octane.
FR2925065B1 (en) * 2007-12-17 2012-11-30 Inst Francais Du Petrole NEW DIAGRAM FOR OPTIMIZING HIGH OCTANE INDEX PRODUCTION AND COPRODUCTION OF AROMATIC BASES
CN101759513B (en) 2008-12-25 2012-08-22 中国石油化工股份有限公司 Method for utilizing naphtha
US8604262B2 (en) * 2011-04-29 2013-12-10 Uop Llc Process for increasing aromatics production
TWI544067B (en) * 2011-05-27 2016-08-01 China Petrochemical Technology Co Ltd A Method for Catalytic Recombination of Naphtha
CN102796553B (en) 2011-05-27 2015-07-29 中国石油化工股份有限公司 A kind of Benzin naphtha catalytic reforming method
US8808534B2 (en) * 2011-07-27 2014-08-19 Saudi Arabian Oil Company Process development by parallel operation of paraffin isomerization unit with reformer
CN103396833B (en) * 2013-08-21 2016-03-23 中国寰球工程公司辽宁分公司 A kind of synthetic naphtha produces the method for motor spirit

Also Published As

Publication number Publication date
FR3014895B1 (en) 2017-02-10
CN104711017A (en) 2015-06-17
KR102366093B1 (en) 2022-02-21
FR3014895A1 (en) 2015-06-19
TW201538708A (en) 2015-10-16
CN104711017B (en) 2018-10-19
KR20150070968A (en) 2015-06-25
TWI653329B (en) 2019-03-11

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