FR2129913A1 - Hydrocarbon conversion with continuous catalyst replacement - and continuous control of heat supply - Google Patents

Hydrocarbon conversion with continuous catalyst replacement - and continuous control of heat supply

Info

Publication number
FR2129913A1
FR2129913A1 FR7109901A FR7109901A FR2129913A1 FR 2129913 A1 FR2129913 A1 FR 2129913A1 FR 7109901 A FR7109901 A FR 7109901A FR 7109901 A FR7109901 A FR 7109901A FR 2129913 A1 FR2129913 A1 FR 2129913A1
Authority
FR
France
Prior art keywords
catalyst
zone
continuous
space
heat supply
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
FR7109901A
Other languages
French (fr)
Other versions
FR2129913B1 (en
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 FR7109901A priority Critical patent/FR2129913A1/en
Publication of FR2129913A1 publication Critical patent/FR2129913A1/en
Application granted granted Critical
Publication of FR2129913B1 publication Critical patent/FR2129913B1/fr
Granted legal-status Critical Current

Links

Classifications

    • 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
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/12Chemical 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
    • B01J8/125Chemical 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
    • 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
    • C10G35/10Catalytic reforming with moving catalysts
    • C10G35/12Catalytic reforming with moving catalysts according to the "moving-bed" method

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

Hydrocarbons are converted, esp. reformed, by circulating a charge of H2 and hydrocarbons through a reaction space contg. a granular catalyst, pref. supported noble metal, the space being divided into a no. of elementary catalytic zones (A) of relatively large cross-section, where the charge flows from top to bottom, connected by elementary catalytic zones (B) of relatively small cross-section, the gas stream leaving one zone (A) being subdivided into a 1st part which passes through a zone (B) to feed the next zone (A), and a 2nd part which is passed into a heat-exchange zone before being fed into the next zone (A), the catalyst being progressively drawn off at the bottom and replaced by fresh catalyst at the top so as to maintain a high and constant level of activity at each point in the catalytic space. The catalyst is pref. drawn off periodically set intervals of 0.5-20 days, the amt. being withdrawn being 3-30% of the total catalyst.
FR7109901A 1971-03-19 1971-03-19 Hydrocarbon conversion with continuous catalyst replacement - and continuous control of heat supply Granted FR2129913A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FR7109901A FR2129913A1 (en) 1971-03-19 1971-03-19 Hydrocarbon conversion with continuous catalyst replacement - and continuous control of heat supply

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7109901A FR2129913A1 (en) 1971-03-19 1971-03-19 Hydrocarbon conversion with continuous catalyst replacement - and continuous control of heat supply

Publications (2)

Publication Number Publication Date
FR2129913A1 true FR2129913A1 (en) 1972-11-03
FR2129913B1 FR2129913B1 (en) 1973-11-30

Family

ID=9073884

Family Applications (1)

Application Number Title Priority Date Filing Date
FR7109901A Granted FR2129913A1 (en) 1971-03-19 1971-03-19 Hydrocarbon conversion with continuous catalyst replacement - and continuous control of heat supply

Country Status (1)

Country Link
FR (1) FR2129913A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2821283A1 (en) * 2001-02-28 2002-08-30 Inst Francais Du Petrole LOW THICKNESS CATALYTIC MULTI-STAGE REACTOR AND PROCESS WITH INTERNAL HEAT EXCHANGER, AND USE THEREOF
FR2877589A1 (en) * 2004-11-09 2006-05-12 Inst Francais Du Petrole Fixed or mobile bed reactor comprising staged reaction zones, used for endothermic or exothermic reactions, comprises narrowed-down section between upper and lower reaction zone, containing thermal exchanger
FR2877590A1 (en) * 2004-11-09 2006-05-12 Inst Francais Du Petrole REACTIONAL DEVICE WITH SEVERAL ZONES IN A MOVABLE BED WITH APPOINTMENT IN EACH REGION OF REGENERATED OR FRESH CATALYST

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
NEANT *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2821283A1 (en) * 2001-02-28 2002-08-30 Inst Francais Du Petrole LOW THICKNESS CATALYTIC MULTI-STAGE REACTOR AND PROCESS WITH INTERNAL HEAT EXCHANGER, AND USE THEREOF
EP1236506A1 (en) * 2001-02-28 2002-09-04 Institut Francais Du Petrole Multi-stage low bed-depth catalytic reactor having internal heat exchange, and use thereof
US6919048B2 (en) 2001-02-28 2005-07-19 Institut Francais Du Petrole Thin multi-stage catalytic reactor with internal heat exchanger, and use thereof
FR2877589A1 (en) * 2004-11-09 2006-05-12 Inst Francais Du Petrole Fixed or mobile bed reactor comprising staged reaction zones, used for endothermic or exothermic reactions, comprises narrowed-down section between upper and lower reaction zone, containing thermal exchanger
FR2877590A1 (en) * 2004-11-09 2006-05-12 Inst Francais Du Petrole REACTIONAL DEVICE WITH SEVERAL ZONES IN A MOVABLE BED WITH APPOINTMENT IN EACH REGION OF REGENERATED OR FRESH CATALYST
WO2006051185A1 (en) * 2004-11-09 2006-05-18 Institut Francais Du Petrole Reaction device having a number of moving bed zones with supplementing in each regenerated or fresh catalyst zone
EP1661617A1 (en) 2004-11-09 2006-05-31 Institut Français du Pétrole Reactor having a plurality of fixed bed or mobile bed zones with integrated heat exchanger
US7611678B2 (en) 2004-11-09 2009-11-03 Institut Francais Du Petrole Multi-zone moving-bed reaction device with an addition of regenerated or fresh catalyst in each zone
US7611677B2 (en) 2004-11-09 2009-11-03 Institut Francais Du Petrole Multi-zone fixed-bed or moving-bed reactor with an integrated heat exchanger
US8609913B2 (en) 2004-11-09 2013-12-17 IFP Energies Nouvelles Multi-zone fixed-bed or moving-bed reactor with an integrated heat exchanger

Also Published As

Publication number Publication date
FR2129913B1 (en) 1973-11-30

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