US2454943A - Heater for hydrocarbon fluids - Google Patents

Heater for hydrocarbon fluids Download PDF

Info

Publication number
US2454943A
US2454943A US605612A US60561245A US2454943A US 2454943 A US2454943 A US 2454943A US 605612 A US605612 A US 605612A US 60561245 A US60561245 A US 60561245A US 2454943 A US2454943 A US 2454943A
Authority
US
United States
Prior art keywords
tubes
heater
wall
deflector
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
US605612A
Inventor
Carl S Reed
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.)
CB&I Technology Inc
Original Assignee
Lummus 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 Lummus Co filed Critical Lummus Co
Priority to US605612A priority Critical patent/US2454943A/en
Application granted granted Critical
Publication of US2454943A publication Critical patent/US2454943A/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

  • Thisinvention relatesl to improvements. in heaters of the type having heating tubes disposed within a furnace chamber and wherein provision is made for conducting combustion within the chamber in a manner to raise the temperature of a hydrocarbon fluid, as it is passed through the tubes, to a desired distillation point, or to. a cracking point, predominantly by radiant heat received from such combustion.
  • An important object of the invention is to pro,- vide such a heater with improved means for efiecting heating of the tubes by convection as well as by radiant heat, within a singlechamber.
  • Another object of the invention is. to provide a highly eicient convection heating feature of improved design within a heater of the vertical tube type wherein an annular series of heating tubes surrounds a combustion region within the lower portion of an upright furnace. chamber and wherein the products of combustion escape from the upper end of the chamber.
  • Another object of the invention is toy provide such a convection heating feature designed for long service without repair or replacement of parts.
  • Fig. 1 is a vertical sectional View of a heater embodying one form of the convection heating feature
  • Fig. 2 is a horizontal section on the line 2--2 of Fig. 1, upon a larger scale and partly broken away;
  • Fig. 3 is a vertical sectional view of a portion of the heater, showing a modiied form ofv the central deflector which forms part of the con vection heating feature; j
  • Fig. 4 is a view, partly in elevation and partly in section, of the upper portion of a heater embodying a further modification of the convection heating feature
  • Fig. 5. is a section on the line 5-5 of Fig. 4, partly broken away;
  • Fig. 6 isa sectional perspective view of a portion of the heater shown in Fig. 4, disclosing details of construction of the convection heating feature;
  • Fig. 7 is a development of the periphery of a portion of the central deflector, indicated in Fig. 4, showing the arrangement of the baffles borne by said deector.
  • Figs. l, 2 and 3 show my invention embodied in a heater of the vertical tube type.
  • the struc- 2 ture. oi the heater includesv a vertical cylindrical shell Il lined with heat insulation 2.
  • a refractory wall 3 formed, in the present instance, of blocks or bricks of ceramic or other suitable refractory material.
  • rings 4y are secured to the inner side of the shell in vertically spaced positions. These rings have inwardly projecting anges forming ledges bearing the weight of the bricks.
  • the lower end of the shell is closed by a hearth 5 of refractory material and formed with a depressed central portion within which burners t are located.
  • a flat ring T of reiractory material is4 tted within the brick wall, and the, Wall, the hearth and the ring 'l define the furnace chamber ci the heater.
  • annular series of vertical heating tubes 8 Within said chamber there is an annular series of vertical heating tubes 8.
  • the tubes are disposed near the brick wall and are equidistant from the axis of the shell'.
  • the upper end portions of the tubes project through holes in the ring 'l and through holes in an annular tubey sheet la, overlyingv the ring.
  • the lower end portions of the tubes project through holes in the margin of the hearth 5 and through holes in an annular tube sheet 5a underlying said margin.
  • the tubes 3 are all serially interconnected by return bends 9 and lll at the upper and lower ends respectively, of the tubes, and the series has an inlet ll and an adjacent outlet l2, both located at the lower end of the heater.
  • different groups of tubes of the series may be connected into different flow circuits, if; desired.
  • An annular housing I3 encloses the return bends at the upper ends of the tubes, and an annular housing it encloses the return bends at the lower ends of the tubes, for heat ⁇ conservation.
  • the burners 6 are gas burn ers and they are preferably of a directional type.
  • a collar i6 of refractory material extends upwardly from the aperture of the ring 'i and defines the outlet for gaseous products oi combustion from the furnace chamber.
  • Said collar is connected to an exhaust stack il through a hood I8 at the base of the stack.
  • the stack and the hood are supported by beams I9 which form part of a frame structure 20 borne by the shell, and the collar It and the ring 'I are supported by the shell.
  • Legs 2l at the lower end of the shell support the entire heater structure.
  • the lower portions of the tubes 8 are heated predominantly by radiant heat from the combustion within the lower portion of the furnace chamber, and the present invention provides for increased transmission of radiant heat to said portions of the tubes and also provides for efficient transmission of heat of convection to the upper portions of the tubes.
  • a drum-like deilector 22 is supported centrally within the upper portion of the furnace chamber, within the space surrounded by the tubes.
  • the deflector comprises a cylindrical body of substantial vertical length and of an external diameter materially less than ⁇ the internal diameter of the series of tubes, to afford a surrounding space of material width between the deflector and the tubes.
  • the lower end of the deflector is in the form of an inverted cone 22a and tapers downwardly from the periphery of the cylindrical body of the deector.
  • the deiiector is supported suspended in a position coaxial with the shell l by links 23 whose upper ends are pivotally attached to ears borne by the hood I8 and whose lower ends are pivotally attached to ears borne by the deflector and located within the cone 22a.
  • the vertical position of the deflector is such as to dispose its upper edge spaced from the outlet of the furnace chamber.
  • the deflector is made of a heat resistant metal alloy such as stainless steel, for example.
  • the deflector bears a series of flat annular baffles 24 surrounding the cylindrical body of the deflector and vertically spaced therealong. The inner edges of these baffles are upturned and secured by welding, or otherwise, to the dellector.
  • the baflles extend radially outward toward the tubes and have notches 25 receiving the inner portion of the periphery of the tubes.
  • the shell I bears a series of vertically spaced flat annular baffles 26 having upturned outer edges welded, or otherwise secured, to the shell, and these baliles extend radially inward, between the bricks of the refractory wall 3 and across the space between said wall and the tubes.
  • the baliles At their inner edges the baliles have notches 21 receiving the outer portion of the periphery of the tubes, and the baflies are disposed at levels intermediate the levels of the inner battles 24.
  • the baffles 24 are all of the same external diameter and the baffles 2B are all of the same internal diameter.
  • the external diameter of the bailles 24 is also less than the internal diameter of the ballles 26 so that the former can pass the latter baffles in assembly and disassembly of the parts.
  • the notches 25 and 2l of the bailles are large enough to afford substantial clearance between the edges of the baffles and the tubes. Thereby, the necessity for accurate shaping and fitting of the baffles is avoided and removal of the tubes is also facilitated. l
  • the hydrocarbon fluid is admitted through the inlet I I and passed through the tubes in succession to the outlet I2.
  • the fluid is heated predominantly by radiant heat transmitted from the combustion within the lower region of the furnace chamber directly to the lower portion of the tubes. This direct radiant heat is supplemented by reflection of radiant heat from the conical lower end of thedeector, located directly over ⁇ the combustionregion.
  • the cone 22a is provided with a good re'- flecting surface disposed to reflect the radiant heat outwardly and downwardly upon the lower portion of the tubes.
  • the gaseous products of combustion ascending from the combustion region are deflected by the deflector 22 and are compelled to flow into the space surrounding the deector and containing the upper portion of the tubes.
  • the staggered baflles cause turbulence and circuitous flow of the hot combustion gases for efficient transfer of heat of convection therefrom to the tubes.
  • the gases, materially cooled by such heat transfer now past the upper edge of the defiector and through the furnace chamber outlet to the stack Il.
  • Fig. 3 shows a convection heating feature precisely like that just described, and shown in Figs. l and 2, except that the periphery of the cylindrical body of the deector is faced with a refractory brick wall 28.
  • the provision of this wall enables the body of the dellector to be made of a less expensive metal.
  • the baffles 24 project outwardly between the bricks of the wall 28.
  • the cylindrical body of the deflector consists entirely of a refractory wall 29.
  • the hood I8@ at the base of the stack also extends downwardly to the refractory shell wall 3a, and the annular upper edge of the defleotor wall 29 abuts an annular flange at the base of the hood.
  • the hood also has a refractory lining 30.
  • the deflector wall has, at its upper edge, a series of notches 3I of liberal size through which the gases flow to the hood and the stack.
  • the stack, the hood and the deector are all supported by the shell.
  • the defiector wall 29 is integrally formed with a series of helical baffles -32 projecting radially therefrom toward the tubes. These balles are of steep pitch and they make materially less than a complete turn around the deflector.
  • the surrounding wall 3a is also integrally formed with a series of similar helical bales 33 projecting inwardly toward the tubes and in direct edgewise opposition to the bales 32. Like the walls which bear them, the bailles 32 and 33 are formed of refractory material.
  • the wall 3a is shown as a continuous piece of refractory but it may be formed of bricks with ribs suitably arranged to form the baflies 33.
  • the baffles 33 have, at their inner edges, notches 34 receiving the outer portion of the periphery of the tubes, and the baliles 32 have similar notches 35 at their outer edges receiving the inner portion of the periphery of the tubes. ⁇ The notches are large enough to afford a desired clearance around the tubes, and the outside radius of bafes 32 is substantially less than the inside radius of baffles 33, for the purposes previously stated in the description of the form of the invention shown in Figs. 1 and 2.
  • the baffles 32 and 33 combine to dene a series of concurrent or parallel helical channels around the deflector. These channels are all open at their lower ends to the combustion region for ow of the combustion gases into the channels.
  • the notches 3l in the upper edge of the defleetor are located so that one of said notches occurs at the upper end of each channel so that the gases can flow from each channel to the stack.
  • the tubes extend across all of the channels directly in the path of the hot gases so that highly eicient transfer of heat to the tubes is obtained.
  • a heater for a hydrocarbon iluid comprising a furnace chamber, substantially parallel heating tubes arranged over the inner surface of a wall of said chamber, burner means disposed to conduct combustion within a region of the chamber adjacent one portion of the length of said tubes for radiant heating thereof, a deflector disposed inwardly of the tubing and having a wall in opposed face-to-face relation to said chamber wall and overlying another length portion of the tubes, said deflector being constructed and arranged to direct the products of combustion between said walls for convection heating of the portion of the tubes therebetween, a set of transversely spaced concurrent ballles oblique with respect to the tubes extending laterally outward from said deflector wall and having notches at their outer edges receiving the inner portion of the periphery of the respective tubes, .a set of baliles spaced similarly to the first-mentioned ballies and similarly oblique extending laterallyv inward from said chamber wall and having notches at their inner edges receiving the outer portion of the periphery of the respective tubes
  • a heater for a hydrocarbon fluid comprising an upright furnace chamber having at the upper end thereof lan outlet for combustion products, an annular series of substantially vertical heating tubes within said chamber and adjacent to and surrounded by a side wall of the chamber,
  • burner means disposed to conduct combustion within a region surrounded by a lower portion of said tubes for radiant heating thereof, a deflector within a region surrounded by an upper portion of the tubes and constructed and arranged to deflect ascending products of cornbustion outwardly against the tubes for convection heating thereof, a set of spaced concurrent helical baffles borne by and extending around and along the said delector and extending laterally outward therefrom, and a set of spaced concurrent helical balles borne by and extending lateral- 1y inward from said surrounding Wall and forming, together with the first-mentioned baiiies, a plurality of concurrent helical channels to conduct the products of combustion to said outlet, the tubes extending lacross said channels in the path of the combustion products therein.
  • a heater for a hydrocarbon fluid as claimed in claim 2, wherein the outer edges of the bailles borne by the deliector are respectively in opposed relation to the inner edges of the bailles borne by the surrounding wall and have notches receiving the inner portion of the periphery of the tubes, and said edges of the wall-borne bailles have notches receiving the outer portion of the periphery of the tubes.
  • a heater for a hydrocarbon fluid as claimed in claim 2, wherein the bales of both of said sets are formed of non-metallic refractory material.

Description

2 Sheets-Sheet 1 IN V EN TOR.
ATToRNEY Nav. 30, 948. c. s. REED HEATER FOR -HYDROCRBON FLUIDS Filed July y17, 1945 Nov. 30, 1948. c. s. REED y HEATER FOR HYDROCARBON FLUIDS 2 Shee'ts-Sheet 2 v Filed July 1'7, 1,945
.--1121A Il Patented Nov. 30, 1948 UNITED STATES PATENT 2,454,943 HEATER Foa Himnos-Annen FLUi-Ds Carli S. Reed'L New York, N.l Y., assigner tel The Lummus Company, New York,` N. Y., ay corpera tion of Delaware.
4 Claims.
Thisinvention relatesl to improvements. in heaters of the type having heating tubes disposed within a furnace chamber and wherein provision is made for conducting combustion within the chamber in a manner to raise the temperature of a hydrocarbon fluid, as it is passed through the tubes, to a desired distillation point, or to. a cracking point, predominantly by radiant heat received from such combustion.
An important object of the invention is to pro,- vide such a heater with improved means for efiecting heating of the tubes by convection as well as by radiant heat, within a singlechamber.
Another object of the invention is. to provide a highly eicient convection heating feature of improved design within a heater of the vertical tube type wherein an annular series of heating tubes surrounds a combustion region within the lower portion of an upright furnace. chamber and wherein the products of combustion escape from the upper end of the chamber.
Another object of the invention is toy provide such a convection heating feature designed for long service without repair or replacement of parts.
These and other objects and advantages of the invention will appear from the following description and from the accompanying drawings.
In the drawings:
Fig. 1 is a vertical sectional View of a heater embodying one form of the convection heating feature;
Fig. 2 is a horizontal section on the line 2--2 of Fig. 1, upon a larger scale and partly broken away;
Fig. 3 is a vertical sectional view of a portion of the heater, showing a modiied form ofv the central deflector which forms part of the con vection heating feature; j
Fig. 4 is a view, partly in elevation and partly in section, of the upper portion of a heater embodying a further modification of the convection heating feature;
Fig. 5. is a section on the line 5-5 of Fig. 4, partly broken away;
Fig. 6 isa sectional perspective view of a portion of the heater shown in Fig. 4, disclosing details of construction of the convection heating feature; and
Fig. 7 is a development of the periphery of a portion of the central deflector, indicated in Fig. 4, showing the arrangement of the baffles borne by said deector.
Figs. l, 2 and 3 show my invention embodied in a heater of the vertical tube type. The struc- 2 ture. oi the heater includesv a vertical cylindrical shell Il lined with heat insulation 2. Inwardly of theheat insulation, there is a refractory wall 3 formed, in the present instance, of blocks or bricks of ceramic or other suitable refractory material. For supporting the bricks, a number of rings 4y are secured to the inner side of the shell in vertically spaced positions. These rings have inwardly projecting anges forming ledges bearing the weight of the bricks. The lower end of the shell is closed by a hearth 5 of refractory material and formed with a depressed central portion within which burners t are located. At the upper end of theshell a flat ring T of reiractory material is4 tted within the brick wall, and the, Wall, the hearth and the ring 'l define the furnace chamber ci the heater. Within said chamber there is an annular series of vertical heating tubes 8. The tubes are disposed near the brick wall and are equidistant from the axis of the shell'. The upper end portions of the tubes project through holes in the ring 'l and through holes in an annular tubey sheet la, overlyingv the ring. The lower end portions of the tubes project through holes in the margin of the hearth 5 and through holes in an annular tube sheet 5a underlying said margin.
In the present instance, the tubes 3 are all serially interconnected by return bends 9 and lll at the upper and lower ends respectively, of the tubes, and the series has an inlet ll and an adjacent outlet l2, both located at the lower end of the heater. However, different groups of tubes of the series may be connected into different flow circuits, if; desired. An annular housing I3 encloses the return bends at the upper ends of the tubes, and an annular housing it encloses the return bends at the lower ends of the tubes, for heat` conservation. The burners 6 are gas burn ers and they are preferably of a directional type. Their upper ends are inclined and they are mounted for individual rotative adjustment on vertical axes so that the flame from any one of the burners may be directed toward a selected groupv of the tubes. An oil burner l5 is also provided at the center of the hearth. At the upper end of the. furnace chamber a collar i6 of refractory material extends upwardly from the aperture of the ring 'i and defines the outlet for gaseous products oi combustion from the furnace chamber. Said collar is connected to an exhaust stack il through a hood I8 at the base of the stack. The stack and the hood are supported by beams I9 which form part of a frame structure 20 borne by the shell, and the collar It and the ring 'I are supported by the shell. Legs 2l at the lower end of the shell support the entire heater structure.
The lower portions of the tubes 8 are heated predominantly by radiant heat from the combustion within the lower portion of the furnace chamber, and the present invention provides for increased transmission of radiant heat to said portions of the tubes and also provides for efficient transmission of heat of convection to the upper portions of the tubes. For these purposes, a drum-like deilector 22 is supported centrally within the upper portion of the furnace chamber, within the space surrounded by the tubes. The deflector comprises a cylindrical body of substantial vertical length and of an external diameter materially less than `the internal diameter of the series of tubes, to afford a surrounding space of material width between the deflector and the tubes. The lower end of the deflector is in the form of an inverted cone 22a and tapers downwardly from the periphery of the cylindrical body of the deector. The deiiector is supported suspended in a position coaxial with the shell l by links 23 whose upper ends are pivotally attached to ears borne by the hood I8 and whose lower ends are pivotally attached to ears borne by the deflector and located within the cone 22a.. The vertical position of the deflector is such as to dispose its upper edge spaced from the outlet of the furnace chamber. Preferably, the deflector is made of a heat resistant metal alloy such as stainless steel, for example.
The deflector bears a series of flat annular baffles 24 surrounding the cylindrical body of the deflector and vertically spaced therealong. The inner edges of these baffles are upturned and secured by welding, or otherwise, to the dellector. The baflles extend radially outward toward the tubes and have notches 25 receiving the inner portion of the periphery of the tubes. The shell I bears a series of vertically spaced flat annular baffles 26 having upturned outer edges welded, or otherwise secured, to the shell, and these baliles extend radially inward, between the bricks of the refractory wall 3 and across the space between said wall and the tubes. At their inner edges the baliles have notches 21 receiving the outer portion of the periphery of the tubes, and the baflies are disposed at levels intermediate the levels of the inner baiiles 24. The baffles 24 are all of the same external diameter and the baffles 2B are all of the same internal diameter. The external diameter of the bailles 24 is also less than the internal diameter of the ballles 26 so that the former can pass the latter baffles in assembly and disassembly of the parts. Preferably the notches 25 and 2l of the bailles are large enough to afford substantial clearance between the edges of the baffles and the tubes. Thereby, the necessity for accurate shaping and fitting of the baffles is avoided and removal of the tubes is also facilitated. l
In the operation of the heater the hydrocarbon fluid is admitted through the inlet I I and passed through the tubes in succession to the outlet I2. In the course of its passage through the tubes the fluid is heated predominantly by radiant heat transmitted from the combustion within the lower region of the furnace chamber directly to the lower portion of the tubes. This direct radiant heat is supplemented by reflection of radiant heat from the conical lower end of thedeector, located directly over` the combustionregion. The cone 22a is provided with a good re'- flecting surface disposed to reflect the radiant heat outwardly and downwardly upon the lower portion of the tubes.
The gaseous products of combustion ascending from the combustion region are deflected by the deflector 22 and are compelled to flow into the space surrounding the deector and containing the upper portion of the tubes. Within said space the staggered baflles cause turbulence and circuitous flow of the hot combustion gases for efficient transfer of heat of convection therefrom to the tubes. From said space the gases, materially cooled by such heat transfer, now past the upper edge of the defiector and through the furnace chamber outlet to the stack Il. Thus, elficient radiant heating of the tubes is obtained within one zone of`the furnace chamber and eflcient convection heating of the fluid is obtained within another zone of the chamber.
Fig. 3 shows a convection heating feature precisely like that just described, and shown in Figs. l and 2, except that the periphery of the cylindrical body of the deector is faced with a refractory brick wall 28. The provision of this wall enables the body of the dellector to be made of a less expensive metal. The baffles 24 project outwardly between the bricks of the wall 28.
In the further modification shown in Figs. 4 to 7, inclusive, the cylindrical body of the deflector consists entirely of a refractory wall 29. The hood I8@ at the base of the stack also extends downwardly to the refractory shell wall 3a, and the annular upper edge of the defleotor wall 29 abuts an annular flange at the base of the hood.
. The hood also has a refractory lining 30. For
escape of the combustion gases from the space between the deflector and the surrounding wall 3a, the deflector wall has, at its upper edge, a series of notches 3I of liberal size through which the gases flow to the hood and the stack. The stack, the hood and the deector are all supported by the shell.
The defiector wall 29 is integrally formed with a series of helical baffles -32 projecting radially therefrom toward the tubes. These balles are of steep pitch and they make materially less than a complete turn around the deflector. The surrounding wall 3a is also integrally formed with a series of similar helical bales 33 projecting inwardly toward the tubes and in direct edgewise opposition to the bales 32. Like the walls which bear them, the bailles 32 and 33 are formed of refractory material. The wall 3a is shown as a continuous piece of refractory but it may be formed of bricks with ribs suitably arranged to form the baflies 33. The baffles 33 have, at their inner edges, notches 34 receiving the outer portion of the periphery of the tubes, and the baliles 32 have similar notches 35 at their outer edges receiving the inner portion of the periphery of the tubes.` The notches are large enough to afford a desired clearance around the tubes, and the outside radius of bafes 32 is substantially less than the inside radius of baffles 33, for the purposes previously stated in the description of the form of the invention shown in Figs. 1 and 2.
The baffles 32 and 33 combine to dene a series of concurrent or parallel helical channels around the deflector. These channels are all open at their lower ends to the combustion region for ow of the combustion gases into the channels. The notches 3l in the upper edge of the defleetor are located so that one of said notches occurs at the upper end of each channel so that the gases can flow from each channel to the stack. The tubes extend across all of the channels directly in the path of the hot gases so that highly eicient transfer of heat to the tubes is obtained.
It is, of course, to be understood that the foregoing description is merely illustrative and `in no Wise limiting and that I desire to comprehend within my invention such modifications as are included within the scope of the appended claims.
Having thus clearly described my invention, What I claim as new and desire to secure by Letters Patent is:
1. A heater for a hydrocarbon iluid comprising a furnace chamber, substantially parallel heating tubes arranged over the inner surface of a wall of said chamber, burner means disposed to conduct combustion within a region of the chamber adjacent one portion of the length of said tubes for radiant heating thereof, a deflector disposed inwardly of the tubing and having a wall in opposed face-to-face relation to said chamber wall and overlying another length portion of the tubes, said deflector being constructed and arranged to direct the products of combustion between said walls for convection heating of the portion of the tubes therebetween, a set of transversely spaced concurrent ballles oblique with respect to the tubes extending laterally outward from said deflector wall and having notches at their outer edges receiving the inner portion of the periphery of the respective tubes, .a set of baliles spaced similarly to the first-mentioned ballies and similarly oblique extending laterallyv inward from said chamber wall and having notches at their inner edges receiving the outer portion of the periphery of the respective tubes, said sets of bailles together defining a plurality of oblique concurrent channels for ilow of the combustion products therethrough, and the tubes extending across said channels in the paths of the combustion products therein.
2. A heater for a hydrocarbon fluid, comprising an upright furnace chamber having at the upper end thereof lan outlet for combustion products, an annular series of substantially vertical heating tubes within said chamber and adjacent to and surrounded by a side wall of the chamber,
burner means disposed to conduct combustion within a region surrounded by a lower portion of said tubes for radiant heating thereof, a deflector within a region surrounded by an upper portion of the tubes and constructed and arranged to deflect ascending products of cornbustion outwardly against the tubes for convection heating thereof, a set of spaced concurrent helical baffles borne by and extending around and along the said delector and extending laterally outward therefrom, and a set of spaced concurrent helical balles borne by and extending lateral- 1y inward from said surrounding Wall and forming, together with the first-mentioned baiiies, a plurality of concurrent helical channels to conduct the products of combustion to said outlet, the tubes extending lacross said channels in the path of the combustion products therein.
3. A heater for a hydrocarbon fluid, as claimed in claim 2, wherein the outer edges of the bailles borne by the deliector are respectively in opposed relation to the inner edges of the bailles borne by the surrounding wall and have notches receiving the inner portion of the periphery of the tubes, and said edges of the wall-borne bailles have notches receiving the outer portion of the periphery of the tubes.
4. A heater for a hydrocarbon fluid, as claimed in claim 2, wherein the bales of both of said sets are formed of non-metallic refractory material.
CARL S. REED.
REFERENCES CITED The following references are of record in the le of this patent:
UNITED STATES PATENTS Number Name Date 1,871,937 Wilson Aug. 16, 1932 1,881,275 Huff Oct. 4, 1932 2,152,905 Mekler Apr. 4, 1939 2,173,844 Houdry Sept. 26, 1939 2,276,529 Throckmorton et al. Mar. 17, 1942 2,333,077 Wallis et al Oct. 26, 1943 2,340,289 Wallis et al. Feb. 1, 1944 2,340,878 Holt et al Feb. 8, 1944 2,362,107 Wallis et al. Nov. 7, 1944
US605612A 1945-07-17 1945-07-17 Heater for hydrocarbon fluids Expired - Lifetime US2454943A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US605612A US2454943A (en) 1945-07-17 1945-07-17 Heater for hydrocarbon fluids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US605612A US2454943A (en) 1945-07-17 1945-07-17 Heater for hydrocarbon fluids

Publications (1)

Publication Number Publication Date
US2454943A true US2454943A (en) 1948-11-30

Family

ID=24424437

Family Applications (1)

Application Number Title Priority Date Filing Date
US605612A Expired - Lifetime US2454943A (en) 1945-07-17 1945-07-17 Heater for hydrocarbon fluids

Country Status (1)

Country Link
US (1) US2454943A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2555552A (en) * 1949-01-04 1951-06-05 Petro Chem Process Company Inc Furnace header box
US2634712A (en) * 1951-08-17 1953-04-14 Ind Engineers Inc Fluid heating unit
US2672850A (en) * 1950-02-01 1954-03-23 Babcock & Wilcox Co Convection fluid heat exchange system
US2712303A (en) * 1948-04-23 1955-07-05 Chemical Construction Corp Fluid heater
US2733692A (en) * 1956-02-07 sherman
US3181508A (en) * 1961-06-26 1965-05-04 Shell Oil Co Industrial furnaces

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1871937A (en) * 1930-03-28 1932-08-16 Standard Oil Co Furnace structure
US1881275A (en) * 1928-08-22 1932-10-04 Lyman C Huff Heater
US2152905A (en) * 1935-06-13 1939-04-04 Universal Oil Prod Co Conversion of hydrocarbon oils
US2173844A (en) * 1935-07-19 1939-09-26 Houdry Process Corp Heat exchange
US2276529A (en) * 1941-07-09 1942-03-17 Petro Chem Dev Company Furnace construction
US2333077A (en) * 1942-10-19 1943-10-26 Petro Chem Dev Company Furnace construction
US2340289A (en) * 1942-09-11 1944-02-01 Petro Chem Dev Company Furnace construction
US2340878A (en) * 1939-12-23 1944-02-08 Shell Dev Method for executing vapor phase reactions
US2362107A (en) * 1943-01-18 1944-11-07 Petro Chem Process Company Inc Apparatus for heating fluids

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1881275A (en) * 1928-08-22 1932-10-04 Lyman C Huff Heater
US1871937A (en) * 1930-03-28 1932-08-16 Standard Oil Co Furnace structure
US2152905A (en) * 1935-06-13 1939-04-04 Universal Oil Prod Co Conversion of hydrocarbon oils
US2173844A (en) * 1935-07-19 1939-09-26 Houdry Process Corp Heat exchange
US2340878A (en) * 1939-12-23 1944-02-08 Shell Dev Method for executing vapor phase reactions
US2276529A (en) * 1941-07-09 1942-03-17 Petro Chem Dev Company Furnace construction
US2340289A (en) * 1942-09-11 1944-02-01 Petro Chem Dev Company Furnace construction
US2333077A (en) * 1942-10-19 1943-10-26 Petro Chem Dev Company Furnace construction
US2362107A (en) * 1943-01-18 1944-11-07 Petro Chem Process Company Inc Apparatus for heating fluids

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2733692A (en) * 1956-02-07 sherman
US2712303A (en) * 1948-04-23 1955-07-05 Chemical Construction Corp Fluid heater
US2555552A (en) * 1949-01-04 1951-06-05 Petro Chem Process Company Inc Furnace header box
US2672850A (en) * 1950-02-01 1954-03-23 Babcock & Wilcox Co Convection fluid heat exchange system
US2634712A (en) * 1951-08-17 1953-04-14 Ind Engineers Inc Fluid heating unit
US3181508A (en) * 1961-06-26 1965-05-04 Shell Oil Co Industrial furnaces

Similar Documents

Publication Publication Date Title
US2160644A (en) Steam generating system
US2276527A (en) Apparatus for heating fluids
US2454943A (en) Heater for hydrocarbon fluids
US2151386A (en) Furnace
US2338295A (en) Heating of fluids
US2340287A (en) Furnace construction
US1989612A (en) Furnace
US2723651A (en) Fluid heaters
US2333077A (en) Furnace construction
US2625917A (en) Fluid heating apparatus
US2114269A (en) Heating apparatus and method
US2718217A (en) Water heating apparatus
GB1022804A (en) Improvements in or relating to the production of oil gas
US2348512A (en) Heating of fluids
US2276529A (en) Furnace construction
US2340289A (en) Furnace construction
US2294254A (en) Apparatus for heating fluids
US1924209A (en) Boiler
US2514279A (en) Heater for fluids
US2598840A (en) Heater for hydrocarbon fluid
US2276528A (en) Apparatus for heating fluids
US2592608A (en) Heater
US2555322A (en) Heater
US2625140A (en) Furnace construction
US3002505A (en) Tube heater