DE3677919D1 - Verfahren und vorrichtung fuer die regeneration von kohlenwasserstoff-umwandlungskatalysatoren. - Google Patents

Verfahren und vorrichtung fuer die regeneration von kohlenwasserstoff-umwandlungskatalysatoren.

Info

Publication number
DE3677919D1
DE3677919D1 DE8686117837T DE3677919T DE3677919D1 DE 3677919 D1 DE3677919 D1 DE 3677919D1 DE 8686117837 T DE8686117837 T DE 8686117837T DE 3677919 T DE3677919 T DE 3677919T DE 3677919 D1 DE3677919 D1 DE 3677919D1
Authority
DE
Germany
Prior art keywords
catalyst
zone
air stream
hydrocarbon conversion
hot
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 - Fee Related
Application number
DE8686117837T
Other languages
English (en)
Inventor
Arthur Raymond Greenwood
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
Application granted granted Critical
Publication of DE3677919D1 publication Critical patent/DE3677919D1/de
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • 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
    • B01J8/087—Heating or cooling the reactor
    • 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
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/22—Moving bed, e.g. vertically or horizontally moving bulk
    • B01J38/24—Moving bed, e.g. vertically or horizontally moving bulk having mainly transverse, i.e. lateral, flow of oxygen-containing gas and material
    • 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
    • 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
    • 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
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/0007—Pressure measurement
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00389—Controlling the temperature using electric heating or cooling elements
    • B01J2208/00415—Controlling the temperature using electric heating or cooling elements electric resistance heaters
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
DE8686117837T 1985-12-27 1986-12-20 Verfahren und vorrichtung fuer die regeneration von kohlenwasserstoff-umwandlungskatalysatoren. Expired - Fee Related DE3677919D1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US06/814,337 US4647549A (en) 1985-12-27 1985-12-27 Regeneration of hydrocarbon conversion catalyst

Publications (1)

Publication Number Publication Date
DE3677919D1 true DE3677919D1 (de) 1991-04-11

Family

ID=25214760

Family Applications (1)

Application Number Title Priority Date Filing Date
DE8686117837T Expired - Fee Related DE3677919D1 (de) 1985-12-27 1986-12-20 Verfahren und vorrichtung fuer die regeneration von kohlenwasserstoff-umwandlungskatalysatoren.

Country Status (17)

Country Link
US (1) US4647549A (de)
EP (1) EP0227080B1 (de)
JP (1) JPS62191038A (de)
KR (1) KR900000752B1 (de)
CN (1) CN1003914B (de)
AT (1) ATE61254T1 (de)
AU (1) AU581113B2 (de)
CA (1) CA1270783A (de)
DE (1) DE3677919D1 (de)
ES (1) ES2021276B3 (de)
GR (1) GR3001572T3 (de)
IN (1) IN169259B (de)
MY (1) MY101859A (de)
NO (1) NO169424C (de)
NZ (1) NZ218643A (de)
SU (1) SU1577686A3 (de)
ZA (1) ZA869479B (de)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4859643A (en) * 1988-05-11 1989-08-22 Uop Regeneration method with reduced catalyst heat exposure
JPH02298356A (ja) * 1989-05-09 1990-12-10 Sofutaade Kogyo Kk 触媒の再生方法及びその装置
US5227566A (en) * 1991-01-09 1993-07-13 Uop Process for the dehydrogenation of hydrocarbons
US5087792A (en) * 1991-01-09 1992-02-11 Uop Process for the dehydrogenation of hydrocarbons
US5824619A (en) * 1994-05-12 1998-10-20 Uop Particulate cooling process with reduced thermal channeling
AU686937B2 (en) * 1995-03-20 1998-02-12 Shell Internationale Research Maatschappij B.V. Process for catalyst regeneration
CN1089639C (zh) * 1998-07-10 2002-08-28 中国石油化工集团公司 烃转化催化剂的再生方法
US6123833A (en) * 1998-09-22 2000-09-26 Uop Llc Method for controlling moisture in a catalyst regeneration process
CN1089640C (zh) * 1999-05-19 2002-08-28 中国石油化工集团公司 一种烃转化催化剂的再生方法
CN1089641C (zh) * 1999-05-19 2002-08-28 中国石油化工集团公司 一种烃转化催化剂的再生工艺
US7282619B2 (en) * 2003-10-14 2007-10-16 Shell Oil Company Method of operating a dehydrogenation reactor system
WO2007018677A1 (en) 2005-07-26 2007-02-15 Exxonmobil Upstream Research Company Method of purifying hydrocarbons and regeneration of adsorbents used therein
FR2934963B1 (fr) * 2008-08-13 2010-11-26 Inst Francais Du Petrole Appareil de regeneration de catalyseur et procede de regeneration associe
FR2957821B1 (fr) * 2010-03-24 2014-08-29 Inst Francais Du Petrole Nouvelle zone de regeneration du catalyseur divisee en secteurs pour unites catalytiques regeneratives
US20150224464A1 (en) * 2014-02-13 2015-08-13 Uop Llc Radial flow reactor having a side inlet nozzle and methods for reacting hydrocarbons using the same

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2833726A (en) * 1952-12-03 1958-05-06 Socony Mobil Oil Co Inc Method and apparatus for cooling granular contact material
US3652231A (en) * 1969-09-25 1972-03-28 Universal Oil Prod Co Reconditioning system for moving column of reforming catalyst
US3647680A (en) * 1969-09-25 1972-03-07 Universal Oil Prod Co Continuous reforming-regeneration process
US3692496A (en) * 1971-04-19 1972-09-19 Universal Oil Prod Co Apparatus for continuous reforming-regeneration process
US3745112A (en) * 1971-11-23 1973-07-10 Universal Oil Prod Co Platinum-tin uniformly dispersed hydro-carbon conversion catalyst and process
US3838038A (en) * 1971-12-14 1974-09-24 Universal Oil Prod Co Continuous conversion and regeneration process
US3978150A (en) * 1975-03-03 1976-08-31 Universal Oil Products Company Continuous paraffin dehydrogenation process
US4094814A (en) * 1977-06-15 1978-06-13 Uop Inc. Regeneration method for gravity-flowing deactivated catalyst particles
US4094817A (en) * 1977-06-15 1978-06-13 Uop Inc. Regeneration method for gravity-flowing deactivated catalyst particles
US4438288A (en) * 1983-03-22 1984-03-20 Uop Inc. Dehydrogenation of hydrocarbons with a halogen contacting step
US4506032A (en) * 1983-03-22 1985-03-19 Uop Inc. Dehydrogenation catalyst composition

Also Published As

Publication number Publication date
JPS62191038A (ja) 1987-08-21
NO169424B (no) 1992-03-16
GR3001572T3 (en) 1992-11-23
EP0227080A3 (en) 1988-04-20
CA1270783A (en) 1990-06-26
MY101859A (en) 1992-01-31
CN86108969A (zh) 1987-07-29
EP0227080A2 (de) 1987-07-01
AU6653586A (en) 1987-07-02
SU1577686A3 (ru) 1990-07-07
ATE61254T1 (de) 1991-03-15
NZ218643A (en) 1988-08-30
JPH055536B2 (de) 1993-01-22
US4647549A (en) 1987-03-03
NO865249D0 (no) 1986-12-22
CN1003914B (zh) 1989-04-19
IN169259B (de) 1991-09-21
NO169424C (no) 1992-06-24
KR870005692A (ko) 1987-07-06
EP0227080B1 (de) 1991-03-06
AU581113B2 (en) 1989-02-09
ES2021276B3 (es) 1991-11-01
ZA869479B (en) 1988-04-27
KR900000752B1 (ko) 1990-02-15
NO865249L (no) 1987-06-29

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Legal Events

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8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee