GB1421339A - Method of operating a reforming process - Google Patents

Method of operating a reforming process

Info

Publication number
GB1421339A
GB1421339A GB5742172A GB5742172A GB1421339A GB 1421339 A GB1421339 A GB 1421339A GB 5742172 A GB5742172 A GB 5742172A GB 5742172 A GB5742172 A GB 5742172A GB 1421339 A GB1421339 A GB 1421339A
Authority
GB
United Kingdom
Prior art keywords
catalyst
reactor
hydrocarbon
collector
reforming
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
GB5742172A
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
Application filed by UOP LLC filed Critical UOP LLC
Publication of GB1421339A publication Critical patent/GB1421339A/en
Expired 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
    • 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
    • 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)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

1421339 Catalyst discharge in reforming process U O P INC 13 Dec 1972 [14 Dec 1971] 57421/72 Heading B1F [Also in Divisions C4 and C5] A reforming process comprises (a) charging a hydrogen-hydrocarbon mixture to a reforming reactor containing a moving bed of platinum group metal catalyst particles at reforming conditions, (b) withdrawing a hydrocarbon stream from the reactor and separately withdrawing used catalyst particles from the reactor through a plurality of catalyst transfer conduits to a catalyst collector, (c) continuously charging a hydrogen rich gas, e.g. recycle gas, to the collector to preclude the passage of hydrocarbons from the reactor through the transfer conduits, the hydrogen-rich gas passing through the conduits into the reactor to be withdrawn therefrom in admixture with the hydrocarbon stream, (d) periodically increasing the flow of the hydrogen rich gas to the collector to preclude the passage of catalyst through the conduits, and withdrawing used catalyst from the collector and (e) adding a quantity of active platinum group metal catalyst to the reactor substantially equivalent to the quantity withdrawn from it to maintain a substantially constant catalyst inventary therein, the reactor remaining on stream at reforming conditions during the addition of said active catalyst to it and withdrawal of used catalyst from it. The process may be carried out in a series of side by side vertical reactors through which the catalyst and hydrocarbon pass generally downward, but the hydrocarbon passes laterally through an annular catalyst bed, and the catalyst and hydrocarbon may move cocurrently or countercurrently between reactors.
GB5742172A 1971-12-14 1972-12-13 Method of operating a reforming process Expired GB1421339A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US20791071A 1971-12-14 1971-12-14

Publications (1)

Publication Number Publication Date
GB1421339A true GB1421339A (en) 1976-01-14

Family

ID=22772465

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5742172A Expired GB1421339A (en) 1971-12-14 1972-12-13 Method of operating a reforming process

Country Status (14)

Country Link
JP (1) JPS5121644B2 (en)
AR (1) AR231726A1 (en)
AU (1) AU462781B2 (en)
BR (1) BR7208793D0 (en)
CA (1) CA978127A (en)
DE (1) DE2260073C3 (en)
ES (1) ES409499A1 (en)
FR (1) FR2163509B1 (en)
GB (1) GB1421339A (en)
IT (1) IT973867B (en)
NL (1) NL175316C (en)
PL (1) PL89059B1 (en)
SU (1) SU468439A3 (en)
ZA (1) ZA728416B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4837114B2 (en) 2010-03-26 2011-12-14 千代田化工建設株式会社 Aromatic hydrocarbon production method and aromatic hydrocarbon production plant
RU2727887C1 (en) * 2019-12-30 2020-07-24 Общество с ограниченной ответственностью "Институт по проектированию предприятий нефтеперерабатывающей и нефтехимической промышленности" (ООО "Ленгипронефтехим") Catalytic reforming unit with continuous regeneration of catalyst

Also Published As

Publication number Publication date
DE2260073B2 (en) 1973-10-04
FR2163509A1 (en) 1973-07-27
BR7208793D0 (en) 1973-09-25
DE2260073A1 (en) 1973-06-20
ZA728416B (en) 1974-06-26
JPS4885605A (en) 1973-11-13
NL7217030A (en) 1973-06-18
DE2260073C3 (en) 1974-05-16
CA978127A (en) 1975-11-18
AR231726A1 (en) 1985-02-28
SU468439A3 (en) 1975-04-25
AU462781B2 (en) 1975-07-10
NL175316C (en) 1984-10-16
ES409499A1 (en) 1976-01-01
PL89059B1 (en) 1976-10-30
AU4994772A (en) 1974-06-13
IT973867B (en) 1974-06-10
NL175316B (en) 1984-05-16
FR2163509B1 (en) 1975-01-03
JPS5121644B2 (en) 1976-07-03

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee