FR2390494A1 - Procede de conversion d'hydrocarbures a stades multiples utilisant des particules de catalyseur s'ecoulant par gravite - Google Patents

Procede de conversion d'hydrocarbures a stades multiples utilisant des particules de catalyseur s'ecoulant par gravite

Info

Publication number
FR2390494A1
FR2390494A1 FR7813116A FR7813116A FR2390494A1 FR 2390494 A1 FR2390494 A1 FR 2390494A1 FR 7813116 A FR7813116 A FR 7813116A FR 7813116 A FR7813116 A FR 7813116A FR 2390494 A1 FR2390494 A1 FR 2390494A1
Authority
FR
France
Prior art keywords
reaction zone
catalyst particles
effluent
zone
conversion process
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
FR7813116A
Other languages
English (en)
Other versions
FR2390494B1 (fr
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.)
Honeywell UOP LLC
Original Assignee
UOP LLC
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
Priority claimed from US05/795,250 external-priority patent/US4119526A/en
Priority claimed from US05/795,054 external-priority patent/US4119527A/en
Application filed by UOP LLC filed Critical UOP LLC
Publication of FR2390494A1 publication Critical patent/FR2390494A1/fr
Application granted granted Critical
Publication of FR2390494B1 publication Critical patent/FR2390494B1/fr
Granted legal-status Critical Current

Links

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
    • 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
    • C10G35/10—Catalytic reforming with moving catalysts
    • C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method

Landscapes

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

Abstract

L'invention a pour objet un procédé de conversion d'une charge d'hydrocabures dans un de conversion catalytique à stades multiples avec chauffage entre les stades et déplacement par gravité des particules du catalyseur. La charge 1 et l'hydrogène 2 chauffés sont mélangés et introduits dans une première zone de réaction I maintenue dans des conditions de conversion ; on chauffe l'effluent résultant et on l'introduit dans une seconde zone de réaction II maintenue dans des conditions de conversion ; on limite en 10, 18,... l'écoulement de l'effluent d'au moins une zone de réaction et on sépare l'effluent de la dernière zone pour obtenir un produit normalement liquide et une phase vapeur riche en hydrogène; on retire au moins périodiquement le catalyseur de la dernière zone de réaction; et on introduit au moins périodiquement du catalyseur frais ou régénéré dans la première zone I. Utilisation à la conversion catalytique des hydrocarbures bouillant dans l'intervalle d'ébullition des naphtas.
FR7813116A 1977-05-09 1978-05-03 Procede de conversion d'hydrocarbures a stades multiples utilisant des particules de catalyseur s'ecoulant par gravite Granted FR2390494A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US05/795,250 US4119526A (en) 1977-05-09 1977-05-09 Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles
US05/795,054 US4119527A (en) 1977-05-09 1977-05-09 Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles

Publications (2)

Publication Number Publication Date
FR2390494A1 true FR2390494A1 (fr) 1978-12-08
FR2390494B1 FR2390494B1 (fr) 1983-12-23

Family

ID=27121582

Family Applications (1)

Application Number Title Priority Date Filing Date
FR7813116A Granted FR2390494A1 (fr) 1977-05-09 1978-05-03 Procede de conversion d'hydrocarbures a stades multiples utilisant des particules de catalyseur s'ecoulant par gravite

Country Status (14)

Country Link
JP (1) JPS5410303A (fr)
AU (1) AU516463B2 (fr)
CA (1) CA1100899A (fr)
DE (1) DE2819753A1 (fr)
ES (1) ES469583A1 (fr)
FR (1) FR2390494A1 (fr)
GB (1) GB1600928A (fr)
IT (1) IT1094599B (fr)
MX (1) MX148920A (fr)
NL (1) NL7804957A (fr)
PT (1) PT67978B (fr)
RO (1) RO75624A (fr)
TR (1) TR20185A (fr)
YU (1) YU105478A (fr)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL8600428A (nl) * 1986-02-20 1987-09-16 Shell Int Research Werkwijze en inrichting om gas, vloeistof en deeltjes met elkaar in contact te brengen.
JPH0227157U (fr) * 1989-08-18 1990-02-22
JPH0535410Y2 (fr) * 1989-08-18 1993-09-08
JPH0227156U (fr) * 1989-08-18 1990-02-22
FR2946660B1 (fr) * 2009-06-10 2011-07-22 Inst Francais Du Petrole Procede de reformage pregeneratif des essences comportant le recyclage d'au moins une partie de l'effluent de la phase de reduction du catalyseur.
FR3024460B1 (fr) 2014-07-29 2018-01-12 Ifp Energies Now Procede de reformage a repartition optimisee du catalyseur.

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3725249A (en) * 1971-12-14 1973-04-03 Universal Oil Prod Co Continuous reforming-regeneration process

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3725249A (en) * 1971-12-14 1973-04-03 Universal Oil Prod Co Continuous reforming-regeneration process

Also Published As

Publication number Publication date
RO75624A (fr) 1981-01-30
ES469583A1 (es) 1979-01-01
TR20185A (tr) 1980-11-01
CA1100899A (fr) 1981-05-12
JPS5721551B2 (fr) 1982-05-08
NL7804957A (nl) 1978-11-13
IT7823131A0 (it) 1978-05-08
GB1600928A (en) 1981-10-21
AU516463B2 (en) 1981-06-04
MX148920A (es) 1983-07-06
JPS5410303A (en) 1979-01-25
YU105478A (en) 1982-08-31
PT67978B (en) 1979-10-22
AU3588678A (en) 1979-11-15
FR2390494B1 (fr) 1983-12-23
DE2819753A1 (de) 1978-11-16
PT67978A (en) 1978-06-01
IT1094599B (it) 1985-08-02

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