US3572296A - Low pressure drop heater for fluids - Google Patents

Low pressure drop heater for fluids Download PDF

Info

Publication number
US3572296A
US3572296A US844837A US3572296DA US3572296A US 3572296 A US3572296 A US 3572296A US 844837 A US844837 A US 844837A US 3572296D A US3572296D A US 3572296DA US 3572296 A US3572296 A US 3572296A
Authority
US
United States
Prior art keywords
heating
heater
fluid
conduits
shaped
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
US844837A
Other languages
English (en)
Inventor
Don B Carson
Marion W Barnes
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products 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 Universal Oil Products Co filed Critical Universal Oil Products Co
Application granted granted Critical
Publication of US3572296A publication Critical patent/US3572296A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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

Definitions

  • a heater for fluids which provides a low pressure drop for fluid flow by having a plurality of spaced apart U- shaped conduits positioned across the heating zone to connect in a parallel flow manner between spaced, longitudinally extending headers.
  • long flame burners provide radiant heating to each side of each leg of the U-shaped conduits by having at least three lines of burners to introduce heating from each end of the heating chamber such that flame and hot gases will provide radiant heat to the opposing inner faces of the U-shaped conduits as well as to the sides facing the side walls of the heater.
  • the present invention relates to a heater for fluids which is particularly designed and arranged to provide a low pressure drop for the fluid flow through the radiant heating zone.
  • the present heater design eliminates extended lengths of conduit and sharp return bends in the fluid flow arrangement by utilizing a plurality of spaced apart U-shaped conduits that are positioned transversely across the entire heater chamber.
  • the lower portion of each U-shaped conduit section has a large radius U-bend that joins together vertical leg portions that in turn connect with headers that extend longitudinally along the top of the heating chamber.
  • each multiple tube heater coil inherently causes a considerable pressure drop for fluid flow therethrough.
  • a still further object of the improved design is to incorporate a spring suspension form of support for the fluid inlet and outlet headers to the heater such that expansion and contraction of such headers, as well as the expansion and contraction of the connecting process Patented Mar. 23, 1971 piping in any direction may optimumly be accommodated. This leads to further pressure drop reduction by eliminating the need for expansion loops in the piping with their attendant pressure drop.
  • the present invention provides a heater for fluids, which comprises in combination, a heating chamber with an internal heating zone having a generally rectangular form with respect to horizontal and vertical cross-sections, a fluid inlet header extending longitudinally along the top of said heating chamber, a heated fluid header parallel to and spaced from said inlet header and similarly extending along the top portion of said heating chamber, a plurality of separate and spaced apart U-shaped tubular conduits positioned transversely and depending from said fluid headers down through the top portion of said chamber tothereby be spaced longitudinally throughout said heating zone, burner means projecting into the interior of said heating chamber from each end portion thereof whereby to provide both high temperature radiant flame and hot gases to the walls of said tubular conduits for radiant heating of the fluid streams flowing therethrough and gas outlet means from an upper portion of said chamber.
  • the burners are placed in at least three vertical rows within each end of the heating zones such that long flames from each of the burners will pass along side of each side wall of the heater and, in effect behind each outer face of the plurality of leg portions of the U-shaped conduits, as well as have high temperature radiant flame and hot combustion gases within the central portion of the heating zone, whereby both the outer and inner faces of all the conduit sections will be subjected to radiant heating.
  • the length of the heater will, of course, be determined by the capabilities of the burners used through the end wall sections of the heater; however, at the present time, certain high pressure burners are capable of shooting flames and hot combustion gases laterally for a distance of the order of 20 feet.
  • long narrow flames may be obtained by the use of a steam atomizing oil burner having a narrow angular conical tip.
  • a steam atomizing oil burner having a narrow angular conical tip.
  • the elimination of tube supports in turn reduces the first-cost for the heating chamber as well as maintenance expense, particularly with respect to tube support repairs and the replacement of deformed or sagging conduits when they are in the horizontal position.
  • the U-tube sections themselves will generally be formed by bending long tubular sections with a long radius bent U-portion and there is no need to weld such U-portions to straight pipe leg sections.
  • the present simplified design permits the longitudinal headers to be placed above the heater roof or ceiling and in turn be suspended from springs or counterweight means such that all types of expansion and contraction may be readily accommodated with respect to the inlet and outlet piping that connects with the headers, as well as with respect to the headers themselves and the multiplicity of depending U-shaped conduit sections spaced throughout the radiant zone of the heating chamber.
  • FIG. 1 of the drawing is a sectional elevational view through a rectangular form heater indicating the rise of a plurality of transversely positioned U-shaped conduit sections.
  • FIG. 2 is a partial sectional view through an end portion of the heating chamber, as indicated by the line 22 in FIG. 1.
  • FIG. 3 of the drawing indicates diagrammatically one means of effecting the resilient spring supporting of the longitudinal headers above the roof portion of the heating chamber.
  • a large unobstructed radiant heating chamber 1 defined by refractory side walls 2 and 2 as well as end walls 3.
  • the heating chamber is also indicated as being supported by a foundation 4 and having a refractory lower floor section 5 as well as refractory roof sections 6 and 6.
  • the latter may be flat or may slope in a manner similar to that indicated in the present drawing toward the center of the heating chamber where a longitudinal opening 7 provides a longitudinal convection heating section 8 between spaced walls 9 and 9'.
  • Convection section 8 will in turn lead into and connect with a suitable stack means, not shown in the drawing, whereby the flue gases from the burner means may be exhausted from the entire heating chamber.
  • inlet and outlet headers are provided along the roof portions of the heating chamber such as in the manner of the inlet header 10, having fluid supplied thereto by way of line 11, and the outlet header 12 which has a heated fluid removed therefrom by way of outlet conduit 13.
  • the longitudinal headers 10 and 12 are spaced apart horizontally in a manner to provide for the connection of a plurality of long radius U-shaped conduit sections 14, which may be spaced relatively close to one another throughout the entire length of the heating zone.
  • the vertical leg portions of the U-shaped sections 14 will connect to and depend from the respective lower wall portions of each of the headers 10 and 12 so that the conduits will provide for the radiant heating of a multiplicity of fluid streams passing in a parallel manner from the inlet header 10 to the outlet header 12.
  • each of the U-shaped sections 14 has a large radius U-bend section 14' which shall be positioned in a manner to clear the floor portion 5 within the heating chamber after each U-shaped section has been subjected to heating and expansion.
  • vertical guide members 5' may project vertically upwardly from the floor portion 5 in a manner to hold or guide each side of the U-shaped sections 14 in a proper vertical alignment and maintain substantially equal spacing between the adjacent tubular sections 14 throughout the entire length of the heating zone.
  • the plurality of conduit sections 14 Will normally be spaced relatively close together, as for example, on 3 to 6" centers. The spacing between conduits in any one heater or portion of a heater will of course depend upon the diameter of the tubing being used for each conduit section.
  • the radiant heating for the U- shaped tubular conduits is provided by long flame emission from burners positioned at each end of the heating chamber in the end wall portions 3.
  • a plurality of vertically spaced burners such as 15 Will be provided along the center line of each. end wall whereby long hot flames will provide radiant heat and hot combustion gases to the inner faces of the U-shaped conduit sections.
  • additional burner means 16 will pass flame and hot combustion gases between side Wall section '2 and the outer faces of the plurality U-shaped conduit sections 14 along one portion of the heating chamber and additional burner means 17 will provide radiant heating to the opposing exterior faces of the plurality of U-shaped sections 14 and along the opposing side wall portion 2'.
  • additional burner means 16 will pass flame and hot combustion gases between side Wall section '2 and the outer faces of the plurality U-shaped conduit sections 14 along one portion of the heating chamber and additional burner means 17 will provide radiant heating to the opposing exterior faces of the plurality of U-shaped sections 14 and along the opposing side wall portion 2'.
  • FIG. '2 of the drawing there is indicated fuel supply piping means 18, with valve means 19, connecting to the plurality of vertical spaced burner means 15 which are of a type providing long lateral flames 20 to carry inwardly for approximately a full half length of the entire heating chamber.
  • long narrow flames will be provided from each of the burners 16 and 17 such that there is high temperature radiant heating to the exterior faces of each of the U-shaped conduit faces throughout the entire length of the heating zone. It is, of course, not intended to limit the heater design and arrangement to any given number of burners or to any particular spacing of burner means.
  • each of the longitudinal header sections 10 and 12 are indicated as being supported on spaced cradle members 21 which in turn are supported from the upper roof portions 6 and 6' of the heating chamber.
  • the longitudinal and vertical expansions due to temperature changes for each U- shaped section 14 will take place downwardly from support positions 21 While each of the header sections 10 and 12 will undergo a certain amount of sliding across the spaced supports 21.
  • expansion and contraction movement due to temperature changes in the conduit system may well be accommodated by the spring suspension of each of the headers 10 and 12, whereby the entire system may be freely floating and minimizing of stresses from connecting pipe runs as well as in the headers and conduit sections. As best shown in FIG.
  • the present embodiment indicates a housing 22 around header 12 as being supported from roof section 6' and the housing 22 holding longitudinal channel members 23 which in turn supports a plate member 24 and a compression spring means 25 with a superposed bearing plate 26 holding a threaded nut 27 that is attached to an adjustable length threaded rod means 28.
  • the latter connects to lug means 29 and the header 12 through pin connection means 30.
  • suitable tension springs may be connected at spaced distances to the top portion of each header and the spring means in turn hung from overhead beam means in lieu of the compression spring arrangement, as set forth in connection with FIG. 3 of the drawing.
  • a modified fluid heating system there may be more than one longitudinal header along each roof section of a single radiant heating zone.
  • a plurality of U-shaped sections such as 14, may connect between a less than full length longitudinal inlet header and accompany an opposing fluid outlet header.
  • Such shortened headers may be at one end or along a central portion of the radiant heating zone, while at the same time one or more additional longitudinal header sections may be provided to accommodate separate fluid streams through an additional plurality of U-shaped conduit sections.
  • more than one fluid stream may be introduced into a single rectangular form heating zone for low pressure drop radiant heating in such zone.
  • conduits for the different groups of transverse U-shaped conduit sections, the size of the conduits being determined by the quantity of fluid to be handled and the amount of heat input required for the particular fluid stream.
  • FIG. 1 there is indicated in FIG. 1 a flow pattern into and out of the headers and 12 such that the fluid inlet pipe 11 connects to header .10 at one end thereof and the heated fluid outlet conduit 13 connects to the end of outlet header 12 at the same end of the heater unit.
  • This flow pattern provides that fluid pressure is high at the opposing closed ends of each of the headers even though velocity head has decreased at the downstream end of the inlet header 10 and is also low at the laterally opposing upstream end of the outlet header 12.
  • it is not intended to limit fluid flow into and out of the headers to any one fixed flow pattern within the scope of the present invention.
  • the present illustrated embodiment indicates a central flue gas outlet through the convection heating section 8 such that the hot combustion gases from all of the end wall burners will flow uniformly into and upwardly through the entire central heating zone 1.
  • the convection heating section 8 and the flue gas outlet means may be positioned in an off-center manner.
  • a plurality of conduits such as shown in tube bank 31, will be provided in the convection heating zone 8, although it is not intended to limit the present improved heater design to any one type of tube bank or waste heat boiler arrangement with respect to the removal of heat in the convection heating section, or within outlet duct work from the heating chamber 1.
  • FIG. 1 still further indicates diagrammatically the use of generally rectangular, or box-like, refractory wall enclosures 32 and 33 for encompassing the fluid header means 10 and 12; however, again it is not intended to limit the present invention to any one type of header enclosure or limit the design to the exterior placement of the headers 10 and 12 above the heater roof means 6 and 6.
  • the drawing is merely diagrammatic with respect to the method of construction for the heater walls, roof and floor sections, in that all such sections may be fabricated in any conventional manner in order to provide a high temperature resistant refractory wall and inner surface.
  • the refractory walls may compirse temperature resistant tile members, or of fire brick, or of a castable refractory material.
  • the wall sections may be prefabricated in a manner where a refractory material is connected directly to metal panel sections sized to form the wall and roof sections of a heating chamber.
  • a heater for fluids which comprises in combination, a heating chamber with an internal heating zone having a generally rectangular form with respect to horizontal and vertical cross-sections, a fluid inlet header extending longitudinally along the top of said heating chamber, a heated fluid header parallel to and spaced from said inlet header and similarly extending along the top portion of said heating chamber, a plurality of separate and spaced apart 'U-shaped tubular conduits positioned transversely and depending from said fluid headers down through the top portion of said chamber to thereby be spaced longitudinally throughout said heating zone, burner means projecting into the interior of said heating chamber from each end portion thereof whereby to provide both high temperature radiant flame and hot gases to the walls of said tubular conduits, and gas outlet means from an upper portion of said chamber.
  • the heater of claim 1 further characterized in that said burner means are mounted centrally within each end portion of the heating chamber whereby to provide long lateral flame and hot combustion gases into the central portion of the heating zone between the inner opposing face of the U-shaped tubular conduits.
  • the heater of claim 1 further characterized in that at least three vertical rows of burners are used in each end wall portion of the heating chamber in a manner to provide resulting flame and hot combustion gases to the center portion of the heating chamber and to portions along each interior wall of the heating chamber and externally along the exterior faces of each U-shaped conduit, whereby there is resulting radiant heating through to both the inner and outer faces of the vertical portions of the U-shaped tubular conduits.
  • the heater of claim 1 further characterized in that a flue gas outlet is provided longitudinally along the central top portion of the heating chamber between the spaced longitudinally extending fluid inlet and fluid outlet headers.
  • the heater of claim 4 further characterized in that said longitudinal flue gas outlet is provided with at least one bank of tubular fluid conduits whereby there may be heat recovery from the hot combustion gases passing through said flue gas outlet.
  • both the fluid inlet and fluid outlet headers are provided with spring support means whereby said headers and the depending plurality of U-shaped tubular conduits can 8 better accommodate expansion and contraction movement References Cited greoartrrtemperature changes in connecting piping to the UNITED STATES PATENTS 7.
  • the heater of claim 1 further characterized in that 2,964,033 12/1960 Throckmorton et the inlet to the fluid inlet header is from one end thereof 2,423,997 7/1947 Ruegg 122' 275X 0 2,751,893 6/1956 Permann 122275 and the outlet from the heated fluid header is from the end thereof which is adjacent the same end of the heater, 7 i whereby to provide for optimum flow of fluids through KENNETH SPRAGUE Pnmaly Exammer the plurality of U-shaped conduits.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Gas Burners (AREA)
  • Combustion Of Fluid Fuel (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Air Supply (AREA)
US844837A 1969-07-25 1969-07-25 Low pressure drop heater for fluids Expired - Lifetime US3572296A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US84483769A 1969-07-25 1969-07-25

Publications (1)

Publication Number Publication Date
US3572296A true US3572296A (en) 1971-03-23

Family

ID=25293760

Family Applications (1)

Application Number Title Priority Date Filing Date
US844837A Expired - Lifetime US3572296A (en) 1969-07-25 1969-07-25 Low pressure drop heater for fluids

Country Status (10)

Country Link
US (1) US3572296A (enrdf_load_html_response)
JP (1) JPS5111074B1 (enrdf_load_html_response)
CA (1) CA919044A (enrdf_load_html_response)
FR (1) FR2055599A5 (enrdf_load_html_response)
GB (1) GB1308566A (enrdf_load_html_response)
HU (1) HU163646B (enrdf_load_html_response)
NL (1) NL157344B (enrdf_load_html_response)
NO (1) NO131690C (enrdf_load_html_response)
SE (1) SE363163B (enrdf_load_html_response)
YU (1) YU33040B (enrdf_load_html_response)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4166434A (en) * 1977-03-07 1979-09-04 Uop Inc. Vertical tube fired heater and process
US4409095A (en) * 1981-01-05 1983-10-11 Uop Inc. Catalytic reforming process
US4431522A (en) * 1983-03-09 1984-02-14 Uop Inc. Catalytic reforming process
EP0134335A1 (en) * 1983-08-15 1985-03-20 Uop Inc. A catalytic reforming process
WO2009073340A1 (en) * 2007-11-28 2009-06-11 Uop Llc Heat transfer unit for high reynolds number flow

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4166434A (en) * 1977-03-07 1979-09-04 Uop Inc. Vertical tube fired heater and process
US4409095A (en) * 1981-01-05 1983-10-11 Uop Inc. Catalytic reforming process
US4431522A (en) * 1983-03-09 1984-02-14 Uop Inc. Catalytic reforming process
EP0134335A1 (en) * 1983-08-15 1985-03-20 Uop Inc. A catalytic reforming process
WO2009073340A1 (en) * 2007-11-28 2009-06-11 Uop Llc Heat transfer unit for high reynolds number flow
US7954544B2 (en) 2007-11-28 2011-06-07 Uop Llc Heat transfer unit for high reynolds number flow

Also Published As

Publication number Publication date
NO131690B (enrdf_load_html_response) 1975-04-01
JPS5111074B1 (enrdf_load_html_response) 1976-04-08
GB1308566A (en) 1973-02-21
CA919044A (en) 1973-01-16
YU33040B (en) 1976-03-31
SE363163B (enrdf_load_html_response) 1974-01-07
FR2055599A5 (enrdf_load_html_response) 1971-05-07
HU163646B (enrdf_load_html_response) 1973-09-27
DE2036541A1 (de) 1971-02-18
YU185170A (en) 1975-08-31
NL157344B (nl) 1978-07-17
NO131690C (enrdf_load_html_response) 1975-07-23
NL7010870A (enrdf_load_html_response) 1971-01-27

Similar Documents

Publication Publication Date Title
US4100889A (en) Band type tube support
US2308762A (en) Superheater arrangement and support therefor
CN110617468A (zh) 一种高温受热面优化布置方式
US2757649A (en) Fluid heater with guided convection elements
US4522157A (en) Convection section assembly for process heaters
US3572296A (en) Low pressure drop heater for fluids
US3385271A (en) Tube heater
RU2213307C2 (ru) Водогрейный котел
US2803227A (en) Radiant steam heater construction and operation
US3566845A (en) Heater for fluids providing zone heating
US3947326A (en) Vertical tube type cracking furnace
US1995034A (en) Boiler furnace
US2962007A (en) Long span tubular heat exchange apparatus
RU2640307C1 (ru) Подогреватель жидких и газообразных сред
US2745388A (en) Multiple cell circular heater
US2625917A (en) Fluid heating apparatus
US1782096A (en) Superheater boiler
US3221713A (en) Forced flow vapor generator
RU2125205C1 (ru) Газоподогреватель
US3741174A (en) Tube supports
RU2021326C1 (ru) Трубчатая печь
CN109423321B (zh) 一种乙烯裂解炉
RU204866U1 (ru) Печь установки замедленного коксования
RU37803U1 (ru) Водогрейный водотрубный котел
RU2820369C1 (ru) Трубчатая печь