ES472233A1 - Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles - Google Patents

Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles

Info

Publication number
ES472233A1
ES472233A1 ES472233A ES472233A ES472233A1 ES 472233 A1 ES472233 A1 ES 472233A1 ES 472233 A ES472233 A ES 472233A ES 472233 A ES472233 A ES 472233A ES 472233 A1 ES472233 A1 ES 472233A1
Authority
ES
Spain
Prior art keywords
bed
hydrocarbon conversion
gravity
catalyst particles
flowing catalyst
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.)
Expired
Application number
ES472233A
Other languages
Spanish (es)
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 US05/828,803 external-priority patent/US4104149A/en
Application filed by UOP LLC filed Critical UOP LLC
Publication of ES472233A1 publication Critical patent/ES472233A1/en
Expired legal-status Critical Current

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

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

In a hydrocarbon conversion process (such as reforming) in which regenerated catalyst 2 is passed in sequence through a series of at least three beds I-IV, (a) the admixed vaporous charge stock and hydrogen feed is divided into a portion 9 which is introduced into the first bed I and a portion 10 which is introduced into the second bed II and the effluents 12 and 14 from these two beds are combined, heated, and introduced into the third bed III, and (b) the flow of effluent 12 from.the first bed is restricted at 13 to increase the density of the vapours (thereby reducing their volume and reducing lodgement of catalyst in the bed I) whilst the amount of the feed passing into the second bed is controlled by a restriction 11.
ES472233A 1977-08-29 1978-07-31 Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles Expired ES472233A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US05/828,803 US4104149A (en) 1977-05-09 1977-08-29 Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles

Publications (1)

Publication Number Publication Date
ES472233A1 true ES472233A1 (en) 1979-03-16

Family

ID=25252792

Family Applications (1)

Application Number Title Priority Date Filing Date
ES472233A Expired ES472233A1 (en) 1977-08-29 1978-07-31 Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles

Country Status (13)

Country Link
JP (1) JPS6039111B2 (en)
AU (1) AU526654B2 (en)
CA (1) CA1104965A (en)
DE (1) DE2832971A1 (en)
ES (1) ES472233A1 (en)
FR (1) FR2401981A1 (en)
GB (1) GB2003914B (en)
IT (1) IT1097997B (en)
MX (1) MX150595A (en)
PT (1) PT68376A (en)
RO (1) RO76038A (en)
SU (1) SU1248530A3 (en)
YU (1) YU40719B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4325807A (en) * 1981-01-05 1982-04-20 Uop Inc. Multiple stage hydrocarbon conversion with gravity flowing catalyst particles
CA2137310C (en) * 1993-12-20 2004-02-17 John C. Jubin Jr. Catalytic converter and method for highly exothermic reactions
US8282814B2 (en) * 2009-03-31 2012-10-09 Uop Llc Fired heater for a hydrocarbon conversion process
RU2518080C2 (en) * 2011-07-08 2014-06-10 Общество с ограниченной ответственностью "Премиум Инжиниринг" Heavy oil stock processing method and device
CN117023513B (en) * 2023-04-20 2025-08-08 武汉氢能与燃料电池产业技术研究院有限公司 Methanol reforming hydrogen production reactor based on multi-stage catalytic heating

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3470090A (en) * 1967-09-25 1969-09-30 Universal Oil Prod Co Method for operating a non-regenerative fixed bed reforming process
US3725248A (en) * 1969-09-25 1973-04-03 Universal Oil Prod Co Method of operating a reforming process
US3647680A (en) * 1969-09-25 1972-03-07 Universal Oil Prod Co Continuous reforming-regeneration process
US3706536A (en) * 1971-05-10 1972-12-19 Universal Oil Prod Co Multiple-stage stacked reactor system for moving bed catalyst particles
US3864240A (en) * 1973-03-09 1975-02-04 Universal Oil Prod Co Integration of a reaction system having gravity-flowing catalyst particles with a fixed-bed system
US3839197A (en) * 1973-08-09 1974-10-01 Universal Oil Prod Co Controlled inter-reactor catalyst transport method
IL51237A (en) * 1976-01-19 1979-11-30 Uop Inc Hydrocarbon conversion with gravity-flowing catalyst particles

Also Published As

Publication number Publication date
GB2003914B (en) 1982-02-24
RO76038A (en) 1981-03-10
IT7826318A0 (en) 1978-07-31
DE2832971A1 (en) 1979-03-22
MX150595A (en) 1984-06-06
IT1097997B (en) 1985-08-31
YU40719B (en) 1986-04-30
JPS5446204A (en) 1979-04-12
CA1104965A (en) 1981-07-14
SU1248530A3 (en) 1986-07-30
JPS6039111B2 (en) 1985-09-04
GB2003914A (en) 1979-03-21
AU3835178A (en) 1980-01-31
DE2832971C2 (en) 1989-03-09
FR2401981B1 (en) 1980-07-04
AU526654B2 (en) 1983-01-27
FR2401981A1 (en) 1979-03-30
PT68376A (en) 1978-09-01
YU184578A (en) 1983-02-28

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Legal Events

Date Code Title Description
FD1A Patent lapsed

Effective date: 19971103