[go: up one dir, main page]

US1962262A - Tubular heater - Google Patents

Tubular heater Download PDF

Info

Publication number
US1962262A
US1962262A US574234A US57423431A US1962262A US 1962262 A US1962262 A US 1962262A US 574234 A US574234 A US 574234A US 57423431 A US57423431 A US 57423431A US 1962262 A US1962262 A US 1962262A
Authority
US
United States
Prior art keywords
zone
tubes
radiation
convection
combustion
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 - Lifetime
Application number
US574234A
Inventor
Thompson Nelson Wamsley
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.)
Shell Development Co
Original Assignee
Shell Development Co
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 Shell Development Co filed Critical Shell Development Co
Priority to US574234A priority Critical patent/US1962262A/en
Application granted granted Critical
Publication of US1962262A publication Critical patent/US1962262A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

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
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/14Thermal 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
    • C10G9/18Apparatus
    • C10G9/20Tube furnaces

Definitions

  • My invention relates to the tubular heaters having a radiant heat zone vand a convection zone and although'not limited thereto is more particularly intended for tubular heaters used for heating or cracking of hydrocarbon oils.
  • One object of my invention is to provide efficient and economical means for applying intense heat under easy control to hydrocarbon oils for the purpose of altering their physical and/or chemical character, while preventing the combustion gases, on their path to the convection zone from dangerously approaching and overheating the bank of tubes in the radiant heat zone.
  • Another object of my invention is to provide 5 the heater with simple arched crosswalls in the radiant heat zone to support the tubes and to strengthen the long walls of the heater.
  • FIG. 1 a sectional view of my tubular heater.
  • 1 is the front wall of the heater; 2 is a crossarch; an air preheater 3, having a vertical partition 4, is built in in the furnace; air is admitted in front through an opening 5 and passed back and forth through the preheater and via the metal enclosure 6 to the burner 'l.
  • the combustion gases are conducted horizontally through the radiant heat zone 8, towards the back wall 9 of the furnace, where the downdraft causes them to pass between the air-preheater 3 and the backwall 9 away from the radiant heat tubes.
  • the combustion gases then pass through the arch 10 into the convection zone 11, where they come in direct contact with the bank of tubes 12, and from where they flow into the flue 13 and to the stack 14.
  • the radiant heat tubes 15 are supported at their ends by the side walls of the heater of which the drawing shows the one sidewall 16 in the background.
  • the radiant tubes 15 are further supported at one or more intermediate points by rollers 1'1 positioned upon the crossarches 2, which crossarches at the same time brace the front and rear wall of the heater.
  • Buckstays 18 connected at the top by cross beams 19 prevent the front and rear walls from bulging.
  • the radiant heat tubes are covered at the top by a roof of tile 20 suspended from the cross beams 19.
  • the radiant tubes are at a safe distance from the combustion gases at 8, which are led horizontally across the furnace, and further in a downward direction to the convection zone away from ,the radiant tubes.
  • Another advantage resides in the method of supporting the radiant tubes at. intermediate points between the ends by crossarches. This eliminates the difficult, expensive, and unsatisfactory method of suspending these tubes from the roof or of supporting them by special expensive heat resistant beams across the furnace. It further allows the use of long tubes in the radiant zone, keeping the span between two supporting points well within the limits of safety. The use of extra long tubes decreases the number of return bends which in turn decreases the pressure loss through the coil, which results in a more economical operation. Furthermore, by supporting the bank of tubes on rollers positioned in troughs placed on top of the supporting crossarches the whole bank of radiant heat tubes is made of the full-floating type and is able to freely expand lengthwise.
  • Fluid heating apparatus comprising: in combination, a horizontal radiation combustion zone, means for effecting combustion within said zone, a downward gas passage from the radiation zone to a convection zone for deflecting combustion gases from the top of the radiation zone, an air conduit interposed between said zones and delivering air directly to the burners, said radiation zone being positioned directly above the convection zone, a multiplicity of tubular elements within said zones providing flow paths for the fluid to be heated, a number of said elements being positioned within the radiation zone off the general direction of flow of the burning gases, the other portion of said elements being placed in the convection zone and in the path of the combustion gases.
  • Fluid heating apparatus comprising: incombination, a radiation combustion zone, means for effecting combustion within said zone, a downward gas passage from the radiation zone to a convection zone for deflecting combustion gases from the top of the radiation zone, an air conduit interposed between said zones and delivering air to the burners, said radiation zone being positioned directly above the convection zone, a multiplicity of tubular elements within said zones providing flow paths for the fluid to be heated, a number of said elements being positioned within the radiation zone off the general direction of flow of the burning gases, and freely supported by arched cross-walls substantially not obstructing said flow and which reinforces two walls of the apparatus, the other portion of said elements being placed in the convection zone and in the path of the combustion gases.
  • Fluid heating apparatus comprising: in combination, a radiation combustion zone, means for effecting combustion within said zone, a downward gas passage from the radiation zone to a convection zone for deflecting combustion gases from the top of the radiation zone, an air conduit interposed between said zones and delivering air to the burners, a multiplicity of tubular elements within said zones providing flow paths for the fluid to be heated, a number of said elements being positioned within the radiation zone off the general direction of flow of the burning gases and resting upon roller-like members, supported by arched cross-walls substantially not obstructing said flow, the other portion of said elements being placed in the convection zone and in the path of the combustion gases.
  • Fluid heating apparatus comprising: in combination, a horizontal radiation combustion zone and separated therefrom a convection heating zone positioned directly below said radiation zone, an air conduit interposed between said zones, a downward gas passage from the radiation zone to the convection zone for deflecting combustion gases from the top of the radiation zone, a means for eifecting combustion within the radiation zone, a series of heating tubes within the radiation zone disposed substantially without the path of the combustion gases and another series of heating tubes within the convection zone.
  • Fluid heating apparatus comprising: in combination, a horizontal radiation combustion zone and a horizontal convection heating zone positioned directly below said radiation zone, an air conduit interposed between said zones, a downward gas passage from the radiation zone to the convection zone for deflecting combustion gases from the top of the radiation zone, a means for effecting combustion within the radiation zone, a series of heating tubes within the radiation zone disposed substantially without the path of the combustion gases and another series of heating tubes within the convection zone.
  • Fluid heating apparatus comprising: in combination, a radiation combustion zone, a convection zone and a gas passage from the radiation zone to said convection zone, said radiation zone being positioned directly above said convection zone, an air conduit interposed between said zones, a series of heating tubes in said zones and one or more arched cross-walls in the radiation zone for freely supporting the tubes while reinforcing two walls of the apparatus.
  • Fluid heating apparatus comprising: in combination, a radiation combustion zone having a series of heating tubes arranged along one side thereof, a burner, acombustion gas exit passage at the side of the zone opposite to the tubes and away from the burner, allowing to divert the combustion gases away from the tubes and to direct them to a convection zone positioned directly below said radiation zone and an air conduit interposed between said zones.
  • a tube-supporting means which comprise rollers supported by the cross-wall in direct supporting contact with the tubes, said cross-wall reinforcing two walls of the furnace.
  • Fluid heating apparatus comprising in combination, a radiation combustion zone, aconvection zone and a gas passage from the radiation zone to said convection zone, said radiation zone being positioned directly above the convection zone, an air conduit interposed between said zones, a series of heating tubes in said zones and one or more arched cross-walls in the radiation zone for supporting side walls of the apparatus and provided with rollers for slidably supporting tubes within the radiation zone.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Combustion Of Fluid Fuel (AREA)

Description

June 12, 1934.
N. W. THOMPSON TUBULAR HEATER Filed Nov. 10, 1951 Invenjo r: Nelson W. Thom By his Attqrngy Patented June 12, 1934 PATENT OFFICE TUBULAR HEATER Nelson Wamsley Thompson, Oakland, Calif., as-
signor to Shell Development Company, San Francisco, Calif., a corporation of Delaware Application November 10, 1931, Serial No. 574,234
9 Claims. (01. 122-356) My invention relates to the tubular heaters having a radiant heat zone vand a convection zone and although'not limited thereto is more particularly intended for tubular heaters used for heating or cracking of hydrocarbon oils.
One object of my invention is to provide efficient and economical means for applying intense heat under easy control to hydrocarbon oils for the purpose of altering their physical and/or chemical character, while preventing the combustion gases, on their path to the convection zone from dangerously approaching and overheating the bank of tubes in the radiant heat zone.
Another object of my invention is to provide 5 the heater with simple arched crosswalls in the radiant heat zone to support the tubes and to strengthen the long walls of the heater.
This invention accordingly consists in the features of construction and the arrangement and 29 design of the parts, which will be more fully indicated in the following description and claims.
In order to disclose more completely this in- .vention reference is had to the accompanying drawing showing in Fig. 1 a sectional view of my tubular heater. 1 In the drawing, 1 is the front wall of the heater; 2 is a crossarch; an air preheater 3, having a vertical partition 4, is built in in the furnace; air is admitted in front through an opening 5 and passed back and forth through the preheater and via the metal enclosure 6 to the burner 'l. The combustion gases are conducted horizontally through the radiant heat zone 8, towards the back wall 9 of the furnace, where the downdraft causes them to pass between the air-preheater 3 and the backwall 9 away from the radiant heat tubes. The combustion gases then pass through the arch 10 into the convection zone 11, where they come in direct contact with the bank of tubes 12, and from where they flow into the flue 13 and to the stack 14. The radiant heat tubes 15 are supported at their ends by the side walls of the heater of which the drawing shows the one sidewall 16 in the background. The radiant tubes 15 are further supported at one or more intermediate points by rollers 1'1 positioned upon the crossarches 2, which crossarches at the same time brace the front and rear wall of the heater.
Buckstays 18 connected at the top by cross beams 19 prevent the front and rear walls from bulging. The radiant heat tubes are covered at the top by a roof of tile 20 suspended from the cross beams 19.
One of the advantages of my invention resides in protecting the radiant tubes from being-impinged by flame, locally overheated and bumed out with disastrous consequences. The radiant tubes are at a safe distance from the combustion gases at 8, which are led horizontally across the furnace, and further in a downward direction to the convection zone away from ,the radiant tubes.
Another advantage resides in the method of supporting the radiant tubes at. intermediate points between the ends by crossarches. This eliminates the difficult, expensive, and unsatisfactory method of suspending these tubes from the roof or of supporting them by special expensive heat resistant beams across the furnace. It further allows the use of long tubes in the radiant zone, keeping the span between two supporting points well within the limits of safety. The use of extra long tubes decreases the number of return bends which in turn decreases the pressure loss through the coil, which results in a more economical operation. Furthermore, by supporting the bank of tubes on rollers positioned in troughs placed on top of the supporting crossarches the whole bank of radiant heat tubes is made of the full-floating type and is able to freely expand lengthwise. This will prevent the buildso ing up of stresses across the supporting walls in the axial direction of the tubes, which might be disastrous. Asecond function of the crossarches is the reinforcement obtained for the front and back walls, by balancing the action of the buck- 5 stays, which will prevent the walls from caving in and bulging with the unavoidable consequence of weakening and leakage due to formation of cracks.
I claim as my invention:
1. Fluid heating apparatus comprising: in combination, a horizontal radiation combustion zone, means for effecting combustion within said zone, a downward gas passage from the radiation zone to a convection zone for deflecting combustion gases from the top of the radiation zone, an air conduit interposed between said zones and delivering air directly to the burners, said radiation zone being positioned directly above the convection zone, a multiplicity of tubular elements within said zones providing flow paths for the fluid to be heated, a number of said elements being positioned within the radiation zone off the general direction of flow of the burning gases, the other portion of said elements being placed in the convection zone and in the path of the combustion gases.
2. Fluid heating apparatus comprising: incombination, a radiation combustion zone, means for effecting combustion within said zone, a downward gas passage from the radiation zone to a convection zone for deflecting combustion gases from the top of the radiation zone, an air conduit interposed between said zones and delivering air to the burners, said radiation zone being positioned directly above the convection zone, a multiplicity of tubular elements within said zones providing flow paths for the fluid to be heated, a number of said elements being positioned within the radiation zone off the general direction of flow of the burning gases, and freely supported by arched cross-walls substantially not obstructing said flow and which reinforces two walls of the apparatus, the other portion of said elements being placed in the convection zone and in the path of the combustion gases.
3. Fluid heating apparatus comprising: in combination, a radiation combustion zone, means for effecting combustion within said zone, a downward gas passage from the radiation zone to a convection zone for deflecting combustion gases from the top of the radiation zone, an air conduit interposed between said zones and delivering air to the burners, a multiplicity of tubular elements within said zones providing flow paths for the fluid to be heated, a number of said elements being positioned within the radiation zone off the general direction of flow of the burning gases and resting upon roller-like members, supported by arched cross-walls substantially not obstructing said flow, the other portion of said elements being placed in the convection zone and in the path of the combustion gases.
4. Fluid heating apparatus comprising: in combination, a horizontal radiation combustion zone and separated therefrom a convection heating zone positioned directly below said radiation zone, an air conduit interposed between said zones, a downward gas passage from the radiation zone to the convection zone for deflecting combustion gases from the top of the radiation zone, a means for eifecting combustion within the radiation zone, a series of heating tubes within the radiation zone disposed substantially without the path of the combustion gases and another series of heating tubes within the convection zone.
5. Fluid heating apparatus comprising: in combination, a horizontal radiation combustion zone and a horizontal convection heating zone positioned directly below said radiation zone, an air conduit interposed between said zones, a downward gas passage from the radiation zone to the convection zone for deflecting combustion gases from the top of the radiation zone, a means for effecting combustion within the radiation zone, a series of heating tubes within the radiation zone disposed substantially without the path of the combustion gases and another series of heating tubes within the convection zone.
6. Fluid heating apparatus comprising: in combination, a radiation combustion zone, a convection zone and a gas passage from the radiation zone to said convection zone, said radiation zone being positioned directly above said convection zone, an air conduit interposed between said zones, a series of heating tubes in said zones and one or more arched cross-walls in the radiation zone for freely supporting the tubes while reinforcing two walls of the apparatus.
7. Fluid heating apparatus comprising: in combination, a radiation combustion zone having a series of heating tubes arranged along one side thereof, a burner, acombustion gas exit passage at the side of the zone opposite to the tubes and away from the burner, allowing to divert the combustion gases away from the tubes and to direct them to a convection zone positioned directly below said radiation zone and an air conduit interposed between said zones.
8. In a furnace provided with heating tubes and a cross-wall, a tube-supporting means which comprise rollers supported by the cross-wall in direct supporting contact with the tubes, said cross-wall reinforcing two walls of the furnace.
9. Fluid heating apparatus comprising in combination, a radiation combustion zone, aconvection zone and a gas passage from the radiation zone to said convection zone, said radiation zone being positioned directly above the convection zone, an air conduit interposed between said zones, a series of heating tubes in said zones and one or more arched cross-walls in the radiation zone for supporting side walls of the apparatus and provided with rollers for slidably supporting tubes within the radiation zone.
NELSON WAMSLEY THOMPSON.
US574234A 1931-11-10 1931-11-10 Tubular heater Expired - Lifetime US1962262A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US574234A US1962262A (en) 1931-11-10 1931-11-10 Tubular heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US574234A US1962262A (en) 1931-11-10 1931-11-10 Tubular heater

Publications (1)

Publication Number Publication Date
US1962262A true US1962262A (en) 1934-06-12

Family

ID=24295248

Family Applications (1)

Application Number Title Priority Date Filing Date
US574234A Expired - Lifetime US1962262A (en) 1931-11-10 1931-11-10 Tubular heater

Country Status (1)

Country Link
US (1) US1962262A (en)

Similar Documents

Publication Publication Date Title
US2276527A (en) Apparatus for heating fluids
EP0197212A1 (en) Radiation shield, furnace and method for shielding a furnace convection section
US2993479A (en) Fluid heaters
US2151386A (en) Furnace
US1962262A (en) Tubular heater
US2898892A (en) Heater
US2603195A (en) Tubular heater and method of controlling radiation effects therein
US1853684A (en) Air heater
US2333077A (en) Furnace construction
US2105821A (en) Furnace
US2625140A (en) Furnace construction
US2332534A (en) Steam generator
US2479544A (en) Tubular heater
US2902981A (en) Vertical tube furnace
US2129589A (en) Method of and apparatus for heating oil or petroleum to elevated temperatures
US2294977A (en) Heater
US2385749A (en) Heater
US2375505A (en) Boiler construction
US3361538A (en) Tube heater
US2994307A (en) Vertical tube heater
US2498717A (en) Heater
US2296390A (en) Process furnace
CN210602781U (en) Waste heat recovery energy-saving tubular heating furnace
US2579350A (en) Furnace
US2129900A (en) Heating of fluids