FR2992874A1 - Reacteur de regeneration en continu de catalyseur avec plateau de distribution de gaz dans la zone d'oxychloration - Google Patents

Reacteur de regeneration en continu de catalyseur avec plateau de distribution de gaz dans la zone d'oxychloration Download PDF

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Publication number
FR2992874A1
FR2992874A1 FR1201888A FR1201888A FR2992874A1 FR 2992874 A1 FR2992874 A1 FR 2992874A1 FR 1201888 A FR1201888 A FR 1201888A FR 1201888 A FR1201888 A FR 1201888A FR 2992874 A1 FR2992874 A1 FR 2992874A1
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FR
France
Prior art keywords
zone
oxychlorination
oxychlorization
continuous regeneration
area
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.)
Granted
Application number
FR1201888A
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English (en)
Other versions
FR2992874B1 (fr
Inventor
Cecile Plais
Bachi Frederic Bazer
Fabian Lambert
Thierry Leflour
Xavier Decoodt
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IFP Energies Nouvelles IFPEN
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IFP Energies Nouvelles IFPEN
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Filing date
Publication date
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Priority to FR1201888A priority Critical patent/FR2992874B1/fr
Priority to US13/932,050 priority patent/US20140008269A1/en
Publication of FR2992874A1 publication Critical patent/FR2992874A1/fr
Application granted granted Critical
Publication of FR2992874B1 publication Critical patent/FR2992874B1/fr
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/42—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using halogen-containing material
    • B01J38/44—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst using halogen-containing material and adding simultaneously or subsequently free oxygen; using oxyhalogen compound
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/90—Regeneration or reactivation
    • B01J23/96—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the noble metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/085—Feeding reactive fluids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
    • B01J8/125—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections
    • 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
    • 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
    • C10G35/10—Catalytic reforming with moving catalysts
    • C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00002—Chemical plants
    • B01J2219/00018—Construction aspects
    • B01J2219/00024—Revamping, retrofitting or modernisation of existing plants
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49718—Repairing
    • Y10T29/49721—Repairing with disassembling
    • Y10T29/4973—Replacing of defective part

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Le réacteur 1 permettant la régénération en continu du catalyseur, est composé d'une enceinte 2 comportant une zone d'oxychloration superposée à une zone de calcination munie d'un conduit d'introduction de gaz de calcination 76. Une zone de mélange 74 est disposée entre la zone d'oxychloration 72 et la zone de calcination 75. La zone de mélange 74 est recouverte par un plateau 80 traversé par une pluralité de tubes 81 permettant le passage du catalyseur de la zone d'oxychloration 72 dans la zone de calcination 75. Les tubes 81 s'étendent verticalement au moins sur la hauteur H de la zone de mélange 74. Un ou plusieurs conduits 73 d'injection de gaz d'oxychloration débouche dans la zone de mélange. Le plateau 80 comporte une pluralité d'orifices pour distribuer de manière homogène le gaz de la zone de mélange 74 dans la zone d'oxychloration 72.
FR1201888A 2012-07-04 2012-07-04 Reacteur de regeneration en continu de catalyseur avec plateau de distribution de gaz dans la zone d'oxychloration Active FR2992874B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
FR1201888A FR2992874B1 (fr) 2012-07-04 2012-07-04 Reacteur de regeneration en continu de catalyseur avec plateau de distribution de gaz dans la zone d'oxychloration
US13/932,050 US20140008269A1 (en) 2012-07-04 2013-07-01 Reactor for continuous catalyst regeneration with a gas distribution tray in the oxychlorination zone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR1201888A FR2992874B1 (fr) 2012-07-04 2012-07-04 Reacteur de regeneration en continu de catalyseur avec plateau de distribution de gaz dans la zone d'oxychloration

Publications (2)

Publication Number Publication Date
FR2992874A1 true FR2992874A1 (fr) 2014-01-10
FR2992874B1 FR2992874B1 (fr) 2014-06-27

Family

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FR1201888A Active FR2992874B1 (fr) 2012-07-04 2012-07-04 Reacteur de regeneration en continu de catalyseur avec plateau de distribution de gaz dans la zone d'oxychloration

Country Status (2)

Country Link
US (1) US20140008269A1 (fr)
FR (1) FR2992874B1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2995379A1 (fr) 2014-09-10 2016-03-16 IFP Energies nouvelles Regenerateur apte a regenerer des catalyseurs dans des conditions operatoires differentes
EP2995380A1 (fr) 2014-09-10 2016-03-16 IFP Energies nouvelles Regenerateur de catalyseurs

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105309006B (zh) * 2014-03-27 2019-05-28 华为技术有限公司 数据分流的方法和基站

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3132092A (en) * 1954-02-12 1964-05-05 Union Oil Co Hydrocarbon conversion process and apparatus
EP0872277A1 (fr) * 1997-04-14 1998-10-21 Institut Français du Pétrole Procédé et dispositif à combustion étagée pour la régénération d'un catalyseur de reformage ou de production d'aromatiques en lit mobile
US7985381B2 (en) * 2009-02-06 2011-07-26 Uop Llc Utilization of baffles in chlorination zone for continuous catalyst regeneration

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3132092A (en) * 1954-02-12 1964-05-05 Union Oil Co Hydrocarbon conversion process and apparatus
EP0872277A1 (fr) * 1997-04-14 1998-10-21 Institut Français du Pétrole Procédé et dispositif à combustion étagée pour la régénération d'un catalyseur de reformage ou de production d'aromatiques en lit mobile
US7985381B2 (en) * 2009-02-06 2011-07-26 Uop Llc Utilization of baffles in chlorination zone for continuous catalyst regeneration

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2995379A1 (fr) 2014-09-10 2016-03-16 IFP Energies nouvelles Regenerateur apte a regenerer des catalyseurs dans des conditions operatoires differentes
EP2995380A1 (fr) 2014-09-10 2016-03-16 IFP Energies nouvelles Regenerateur de catalyseurs

Also Published As

Publication number Publication date
US20140008269A1 (en) 2014-01-09
FR2992874B1 (fr) 2014-06-27

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