GB1135877A – Improvements in or relating to fluid heaters of the tubular type
– Google Patents
GB1135877A – Improvements in or relating to fluid heaters of the tubular type
– Google Patents
Improvements in or relating to fluid heaters of the tubular type
Info
Publication number
GB1135877A
GB1135877A
GB14368/67A
GB1436867A
GB1135877A
GB 1135877 A
GB1135877 A
GB 1135877A
GB 14368/67 A
GB14368/67 A
GB 14368/67A
GB 1436867 A
GB1436867 A
GB 1436867A
GB 1135877 A
GB1135877 A
GB 1135877A
Authority
GB
United Kingdom
Prior art keywords
tubes
manifolds
closed
manifold
pipes
Prior art date
1966-04-08
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
GB14368/67A
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.)
Selas Corp of America
Original Assignee
Selas Corp of America
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.)
1966-04-08
Filing date
1967-03-29
Publication date
1968-12-04
1967-03-29
Application filed by Selas Corp of America
filed
Critical
Selas Corp of America
1968-12-04
Publication of GB1135877A
publication
Critical
patent/GB1135877A/en
Status
Expired
legal-status
Critical
Current
Links
Espacenet
Global Dossier
Discuss
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
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
B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J19/24—Stationary reactors without moving elements inside
B01J19/2415—Tubular reactors
B01J19/2425—Tubular reactors in parallel
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
C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
C10G9/18—Apparatus
C10G9/20—Tube furnaces
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00049—Controlling or regulating processes
B01J2219/00051—Controlling the temperature
B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
B01J2219/00085—Plates; Jackets; Cylinders
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00049—Controlling or regulating processes
B01J2219/00051—Controlling the temperature
B01J2219/0015—Controlling the temperature by thermal insulation means
B01J2219/00155—Controlling the temperature by thermal insulation means using insulating materials or refractories
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
B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
B01J2219/00049—Controlling or regulating processes
B01J2219/00051—Controlling the temperature
B01J2219/00157—Controlling the temperature by means of a burner
Abstract
1,135,877. Heaters for fluids. SELAS CORP. OF AMERICA. 29 March, 1967 [8 April, 1966], No. 14368/67. Heading F4A. In a fluid heater of the tubular type, e.g. for hydrocarbon pyrolysis, the vertical tubes 12 are supported by saddle-shaped supports 18, 19, on manifolds 15 situated inside the furnace 4 and the upper end of each tube is connected to a counterweight mechanism 26, 28, 31. The oil supply manifold 33 is connected by flexible inlet pipes 35 to the upper ends of the tubes 12 which are closed by plates 13 with yokes 14 which are connected to the counterweight mechanism. The tubes 12 are arranged in two rows in staggered formation, the tubes above one manifold 15 being connected by pipes 16 to the other manifold. Pipes 21 connect the manifolds 15 to a discharge pipe 22. The manifolds 15 are arranged in a removable trough 5. In Fig. 4, wherein the tubes 41 contain a catalyst, the lower ends of the tube project through the furnace wall and are closed by removable caps 42 for removal of the catalyst. The holes in sleeves 47 through which the tubes pass are slightly elongated to allow for expansion of the manifolds 15 and are closed by plates 48 carried by the tubes 41.
GB14368/67A
1966-04-08
1967-03-29
Improvements in or relating to fluid heaters of the tubular type
Expired
GB1135877A
(en)
Applications Claiming Priority (1)
Application Number
Priority Date
Filing Date
Title
US541305A
US3361118A
(en)
1966-04-08
1966-04-08
Tube heater
Publications (1)
Publication Number
Publication Date
GB1135877A
true
GB1135877A
(en)
1968-12-04
Family
ID=24159017
Family Applications (1)
Application Number
Title
Priority Date
Filing Date
GB14368/67A
Expired
GB1135877A
(en)
1966-04-08
1967-03-29
Improvements in or relating to fluid heaters of the tubular type
Country Status (4)
Country
Link
US
(1)
US3361118A
(en)
DE
(1)
DE1667259B2
(en)
FR
(1)
FR1517646A
(en)
GB
(1)
GB1135877A
(en)
Cited By (1)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
DE2842411A1
(en)
*
1977-10-07
1979-04-12
Hamon Sobelco Sa
HEAT EXCHANGERS, IN PARTICULAR FOR ATMOSPHERIC COOLERS
Families Citing this family (7)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
DE1751054A1
(en)
*
1967-03-29
1971-05-13
Air Reduction
Liquid cylinder system
US3573012A
(en)
*
1969-02-20
1971-03-30
Selas Corp Of America
Method for straight-through cracking of hydrocarbons
CH577117A5
(en)
*
1974-04-29
1976-06-30
Sulzer Ag
US4005681A
(en)
*
1975-07-23
1977-02-01
General Atomic Company
Vapor generator
JPS58142978A
(en)
*
1982-02-22
1983-08-25
Toyo Eng Corp
Heating furnace for treating hydrocarbon
DE102012015667A1
(en)
2012-08-09
2014-04-30
L’Air Liquide, Société Anonyme pour l’Etude et l’Exploitation des Procédés Georges Claude
Discharge system for a steam reformer and storage for this
DE102012112475A1
(en)
*
2012-12-18
2014-06-18
Thyssenkrupp Uhde Gmbh
reformer
Family Cites Families (4)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
US2898892A
(en)
*
1957-07-22
1959-08-11
Sinclair Refining Co
Heater
US3062197A
(en)
*
1959-07-23
1962-11-06
Selas Corp Of America
Tube heater
US3195989A
(en)
*
1962-07-09
1965-07-20
Foster Wheeler Corp
Integral tube furnace and oxidizer
US3267915A
(en)
*
1965-06-11
1966-08-23
Foster Wheeler Corp
Fired heater
1966
1966-04-08
US
US541305A
patent/US3361118A/en
not_active
Expired – Lifetime
1967
1967-03-29
GB
GB14368/67A
patent/GB1135877A/en
not_active
Expired
1967-04-04
DE
DE19671667259
patent/DE1667259B2/en
active
Pending
1967-04-06
FR
FR101698A
patent/FR1517646A/en
not_active
Expired
Cited By (1)
* Cited by examiner, † Cited by third party
Publication number
Priority date
Publication date
Assignee
Title
DE2842411A1
(en)
*
1977-10-07
1979-04-12
Hamon Sobelco Sa
HEAT EXCHANGERS, IN PARTICULAR FOR ATMOSPHERIC COOLERS
Also Published As
Publication number
Publication date
DE1667259B2
(en)
1970-07-23
DE1667259A1
(en)
1969-12-04
US3361118A
(en)
1968-01-02
FR1517646A
(en)
1968-03-15
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None