FR3130833B1 - Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide - Google Patents

Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide Download PDF

Info

Publication number
FR3130833B1
FR3130833B1 FR2114150A FR2114150A FR3130833B1 FR 3130833 B1 FR3130833 B1 FR 3130833B1 FR 2114150 A FR2114150 A FR 2114150A FR 2114150 A FR2114150 A FR 2114150A FR 3130833 B1 FR3130833 B1 FR 3130833B1
Authority
FR
France
Prior art keywords
liquid
raffinate
extract
aromatics
separation unit
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
FR2114150A
Other languages
English (en)
Other versions
FR3130833A1 (fr
Inventor
Jérémy Gazarian
Thi Bich Ngoc Dang
Li Zhang
Arnaud Cotte
Anaïs Dorsey
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
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Priority to FR2114150A priority Critical patent/FR3130833B1/fr
Priority to EP22836120.0A priority patent/EP4453141A1/fr
Priority to KR1020247022939A priority patent/KR20240122819A/ko
Priority to PCT/EP2022/085676 priority patent/WO2023117594A1/fr
Priority to CN202280085321.9A priority patent/CN118451161A/zh
Priority to US18/722,049 priority patent/US20240417631A1/en
Publication of FR3130833A1 publication Critical patent/FR3130833A1/fr
Application granted granted Critical
Publication of FR3130833B1 publication Critical patent/FR3130833B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G35/00Reforming naphtha
    • C10G35/04Catalytic reforming
    • C10G35/06Catalytic reforming characterised by the catalyst used
    • C10G35/085Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof
    • C10G35/09Bimetallic catalysts in which at least one of the metals is a platinum group metal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G61/00Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
    • C10G61/02Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/143Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0492Feeding reactive fluids
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C6/00Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
    • C07C6/08Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
    • C07C6/12Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
    • C07C6/123Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of only one hydrocarbon
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/04Purification; Separation; Use of additives by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/10Purification; Separation; Use of additives by extraction, i.e. purification or separation of liquid hydrocarbons with the aid of liquids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G61/00Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
    • C10G61/02Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only
    • C10G61/04Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only the refining step being an extraction
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G61/00Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
    • C10G61/10Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen processes also including other conversion steps
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G63/00Treatment of naphtha by at least one reforming process and at least one other conversion process
    • C10G63/02Treatment of naphtha by at least one reforming process and at least one other conversion process plural serial stages only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G7/00Distillation of hydrocarbon oils
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/30Aromatics
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G57/00Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one cracking process or refining process and at least one other conversion process
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G63/00Treatment of naphtha by at least one reforming process and at least one other conversion process
    • C10G63/06Treatment of naphtha by at least one reforming process and at least one other conversion process plural parallel stages only
    • C10G63/08Treatment of naphtha by at least one reforming process and at least one other conversion process plural parallel stages only including at least one cracking step

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Dispositif et procédé de production et de séparation dans lesquels : on produit et fractionne un effluent de reformage (40) dans une unité de séparation (1) et un train de fractionnement (5-6-7) pour extraire du benzène (22), du toluène (23), des xylènes (24), et des aromatiques en C9-10 ; on extrait des aromatiques d’une charge (41) dans une unité d’extraction liquide-liquide (14) pour produire un premier raffinat (43) et un premier extrait (42), ce dernier étant envoyé vers un dispositif de fractionnement benzène-toluène (5) ; on sépare les xylènes dans une unité de séparation des xylènes (10) pour produire un deuxième extrait (31) comprenant du paraxylène, et un deuxième raffinat (32) comprenant de l’orthoxylène et du métaxylène ; on isomérise le deuxième raffinat dans une unité d’isomérisation (11), pour produire un isomérat (34) enrichi en paraxylène envoyé dans un train de fractionnement (5-6-7). Figure 2 à publier
FR2114150A 2021-12-21 2021-12-21 Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide Active FR3130833B1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
FR2114150A FR3130833B1 (fr) 2021-12-21 2021-12-21 Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide
EP22836120.0A EP4453141A1 (fr) 2021-12-21 2022-12-13 Unité de production et de séparation des aromatiques avec valorisation d'un extrait et/ou d'un raffinat provenant d'un procédé d'extraction liquide-liquide
KR1020247022939A KR20240122819A (ko) 2021-12-21 2022-12-13 액체-액체 추출 프로세스로부터 추출물 및/또는 라피네이트의 회수와 함께 방향족을 제조 및 분리하기 위한 유닛
PCT/EP2022/085676 WO2023117594A1 (fr) 2021-12-21 2022-12-13 Unité de production et de séparation des aromatiques avec valorisation d'un extrait et/ou d'un raffinat provenant d'un procédé d'extraction liquide-liquide
CN202280085321.9A CN118451161A (zh) 2021-12-21 2022-12-13 通过由液-液提取工艺回收提取物和/或提余物而生产和分离芳烃的单元
US18/722,049 US20240417631A1 (en) 2021-12-21 2022-12-13 Unit for producing and separating aromatics with recovery of an extract and/or raffinate from a liquid-liquid extraction process

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR2114150A FR3130833B1 (fr) 2021-12-21 2021-12-21 Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide
FR2114150 2021-12-21

Publications (2)

Publication Number Publication Date
FR3130833A1 FR3130833A1 (fr) 2023-06-23
FR3130833B1 true FR3130833B1 (fr) 2024-10-11

Family

ID=80735921

Family Applications (1)

Application Number Title Priority Date Filing Date
FR2114150A Active FR3130833B1 (fr) 2021-12-21 2021-12-21 Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide

Country Status (6)

Country Link
US (1) US20240417631A1 (fr)
EP (1) EP4453141A1 (fr)
KR (1) KR20240122819A (fr)
CN (1) CN118451161A (fr)
FR (1) FR3130833B1 (fr)
WO (1) WO2023117594A1 (fr)

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4962258A (en) 1988-12-15 1990-10-09 Amoco Corporation Liquid-phase xylene isomerization
US6180550B1 (en) 1998-12-22 2001-01-30 Mobile Oil Corporation Small crystal ZSM-5, its synthesis and use
FR2862638B1 (fr) 2003-11-26 2005-12-30 Inst Francais Du Petrole Procede de production de paraxylene comprenant une etape d'adsorption et deux etapes d'isomerisation
US7371913B2 (en) 2005-06-30 2008-05-13 Uop Llc Selective aromatics isomerization process
MY162584A (en) 2010-04-21 2017-06-30 Exxonmobil Chemical Patents Inc Xylene isomerization process and catalyst therefor
US20150166435A1 (en) * 2013-12-13 2015-06-18 Uop Llc Methods and apparatuses for processing hydrocarbons
FR3023841B1 (fr) 2014-07-18 2016-07-15 Ifp Energies Now Procede de production de paraxylene comprenant deux unites de separation en lit mobile simule et deux unites d'isomerisation dont l'une en phase gaz
FR3023840B1 (fr) 2014-07-18 2016-07-15 Ifp Energies Now Procede de production de paraxylene a haute purete a partir d'une coupe xylenes, utilisant deux unites de separation en lit mobile simule fonctionnant en serie et deux unites d'isomerisation.
FR3104572B1 (fr) * 2019-12-17 2021-12-31 Ifp Energies Now Conversion de composés aromatiques par alkylation de toluène par du CO et de benzène par l’éthanol pour production de paratolualdéhyde

Also Published As

Publication number Publication date
WO2023117594A1 (fr) 2023-06-29
EP4453141A1 (fr) 2024-10-30
CN118451161A (zh) 2024-08-06
FR3130833A1 (fr) 2023-06-23
KR20240122819A (ko) 2024-08-13
US20240417631A1 (en) 2024-12-19

Similar Documents

Publication Publication Date Title
DE59610939D1 (de) Verfahren zur Gewinnung von Reinaromaten aus Reformatbenzin
US7592499B2 (en) Process for co-producing para-xylene and styrene
RU2019109085A (ru) Способы и устройства для получения ароматических продуктов
FR3104571B1 (fr) Dispositif et procédé de conversion de composés aromatiques par alkylation de toluène par du CO pour production de paratolualdéhyde
JP2007512293A5 (fr)
GB1430482A (en) Process for producing aromatic hydrocarbons
TW201323404A (zh) 利用多重吸附分離單元及分隔分餾塔製造對二甲苯之方法及裝置
HRP20210834T1 (hr) Postupak i uređaj za inverzno razdvajanje aromata
AR008837A1 (es) Proceso para recuperar estireno a partir de materiales de alimentacion de varios hidrocarburos.
WO2017044137A1 (fr) Procédés et appareils pour la méthylation du toluène dans un complexe d'hydrocarbures aromatiques
GB1227510A (fr)
JP2019194187A5 (fr)
US2795635A (en) Centrifuge
FR3130833B1 (fr) Unité de production et de séparation des aromatiques avec valorisation d’un extrait et/ou d’un raffinat provenant d’un procédé d’extraction liquide-liquide
RU2016134769A (ru) Энергосберегающий способ фракционирования для разделения выходящего потока реактора процессов переалкилирования tol/a9+
US3000794A (en) Extractive distillation of vinyl acetylene in the purification of butadiene
US20160347689A1 (en) Processes and apparatuses for separating streams to provide a transalkylation feed stream in an aromatics complex
US3700566A (en) Biphenyl purification process by plural stage fractional distillation
JP2019194222A (ja) 芳香族化合物複合施設において流れを分離してトランスアルキル化供給流を与えるための方法及びシステム
US20150038755A1 (en) Processes and systems for separating streams to provide a transalkylation feed stream in an aromatics complex
US20180305277A1 (en) Process and apparatus for improved para-xylene yield in an aromatic complex
US20160346711A1 (en) Processes and apparatuses for separating streams to provide a transalkylation feed stream in an aromatics complex
ATE59835T1 (de) Verfahren zur abtrennung von reinen aromaten.
US3304341A (en) Processes for separation of olefines
FR3104573B1 (fr) Dispositif et procédé de conversion de composés aromatiques par alkylation de toluène par du méthanol

Legal Events

Date Code Title Description
PLFP Fee payment

Year of fee payment: 2

PLSC Publication of the preliminary search report

Effective date: 20230623

PLFP Fee payment

Year of fee payment: 3

PLFP Fee payment

Year of fee payment: 4