ES464566A1 - Compact multi-tube catalytic reaction apparatus - Google Patents

Compact multi-tube catalytic reaction apparatus

Info

Publication number
ES464566A1
ES464566A1 ES464566A ES464566A ES464566A1 ES 464566 A1 ES464566 A1 ES 464566A1 ES 464566 A ES464566 A ES 464566A ES 464566 A ES464566 A ES 464566A ES 464566 A1 ES464566 A1 ES 464566A1
Authority
ES
Spain
Prior art keywords
combustion chamber
furnace
reactors
wall arrangement
adjacent
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
ES464566A
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.)
Raytheon Technologies Corp
Original Assignee
United Technologies Corp
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 US05/827,803 external-priority patent/US4098587A/en
Application filed by United Technologies Corp filed Critical United Technologies Corp
Publication of ES464566A1 publication Critical patent/ES464566A1/en
Expired 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
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/062—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes being installed in a furnace
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
    • 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
    • B01J2208/00477—Controlling the temperature by thermal insulation means
    • B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories

Abstract

The reactor installation (10) has a furnace (12) which delivers heat for an endothermic reaction. This furnace (12) has a part having elevated heating output and a wall arrangement (89) which delimits a combustion chamber (60). The furnace (12) has an outlet device (103). Means (16, 18) are assigned to the combustion chamber (60) which introduce the fuel (16) and an oxidant (18) into the combustion chamber (60). The installation (10) has a plurality of tubular reactors (20) which are arranged at least almost in the tightest packing and which are arranged within the furnace (12) and each of which has a first part (56) arranged within the combustion chamber (60) and a second part (58). The latter is arranged within the furnace part having elevated heating output, this oven part being provided with an inlet apparatus (104), which is in gas connection to the combustion chamber (60), and an outlet apparatus (67), which is in gas connection with the outlet device (103). Shield devices (90) arranged within the combustion chamber (60) are provided for reducing the temperature differences among the reactors (20). These shield devices (90) are arranged between the combustion chamber wall arrangement (89) and the reactors (20) adjacent to this wall arrangement (89), in order to reduce the radiant heating of the first parts (56) of the reactors (20) which are adjacent to the wall arrangement (89). This compact catalytic reactor installation simultaneously has a higher life expectancy and operates extremely efficiently.
ES464566A 1976-12-22 1977-11-29 Compact multi-tube catalytic reaction apparatus Expired ES464566A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US75333576A 1976-12-22 1976-12-22
US05/827,803 US4098587A (en) 1976-12-22 1977-08-25 Compact multi-tube catalytic reaction apparatus

Publications (1)

Publication Number Publication Date
ES464566A1 true ES464566A1 (en) 1978-09-01

Family

ID=27115728

Family Applications (1)

Application Number Title Priority Date Filing Date
ES464566A Expired ES464566A1 (en) 1976-12-22 1977-11-29 Compact multi-tube catalytic reaction apparatus

Country Status (13)

Country Link
JP (1) JPS5379768A (en)
AU (1) AU509038B2 (en)
BR (1) BR7707896A (en)
CH (1) CH625827A5 (en)
DE (1) DE2751308A1 (en)
DK (1) DK514377A (en)
ES (1) ES464566A1 (en)
FR (1) FR2374947A1 (en)
GB (1) GB1564995A (en)
IL (1) IL53404A (en)
IT (1) IT1089105B (en)
NL (1) NL7712715A (en)
SE (1) SE423895B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5735935A (en) * 1980-08-11 1982-02-26 Mitsui Toatsu Chem Inc Heat-absorptive reactor
JPS63162503A (en) * 1986-12-25 1988-07-06 Toyo Eng Corp Gas producer
US5164163A (en) * 1988-09-19 1992-11-17 Kabushiki Kaisha Kobe Seiko Sho Hydrocarbon reforming apparatus
JPH03232703A (en) * 1989-12-26 1991-10-16 Tokyo Electric Power Co Inc:The Reformer of hydrocarbon
JP2513485Y2 (en) * 1991-08-06 1996-10-09 北越消雪機械工業株式会社 Watering nozzle
JP3442167B2 (en) * 1993-12-28 2003-09-02 千代田化工建設株式会社 Heat transfer method in reformer
DE10119083C1 (en) * 2001-04-19 2002-11-28 Joachim Alfred Wuenning Compact steam reformer
US20070104641A1 (en) * 2005-11-08 2007-05-10 Ahmed M M Method of controlling oxygen addition to a steam methane reformer

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1580740A (en) * 1923-02-20 1926-04-13 Commercial Solvents Corp Catalyzing apparatus
US2173844A (en) * 1935-07-19 1939-09-26 Houdry Process Corp Heat exchange
US3144312A (en) * 1961-06-06 1964-08-11 Mertens Carl Catalytic conversion plant for the continuous generation of gases of any kind out of ydrocarbons
US3645701A (en) * 1967-06-19 1972-02-29 Lummus Co Reformer furnace
US3541729A (en) * 1968-05-09 1970-11-24 Gen Electric Compact reactor-boiler combination
US3909299A (en) * 1973-10-01 1975-09-30 United Technologies Corp Fuel cell system including reform reactor
DE2521710A1 (en) * 1975-05-15 1976-11-18 Siemens Ag REACTOR FOR THE CATALYTIC REVISION OF HYDROCARBONS WITH AN OXYGEN-CONTAINING GAS

Also Published As

Publication number Publication date
AU509038B2 (en) 1980-04-17
CH625827A5 (en) 1981-10-15
IL53404A (en) 1981-03-31
JPS577539B2 (en) 1982-02-10
IL53404A0 (en) 1978-01-31
IT1089105B (en) 1985-06-18
DE2751308C2 (en) 1987-05-14
FR2374947A1 (en) 1978-07-21
BR7707896A (en) 1978-08-01
FR2374947B1 (en) 1983-08-19
SE7713225L (en) 1978-06-23
NL7712715A (en) 1978-06-26
DE2751308A1 (en) 1978-07-06
SE423895B (en) 1982-06-14
AU3072577A (en) 1979-05-24
DK514377A (en) 1978-06-23
JPS5379768A (en) 1978-07-14
GB1564995A (en) 1980-04-16

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