US20090056696A1 - Flameless combustion heater - Google Patents

Flameless combustion heater Download PDF

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Publication number
US20090056696A1
US20090056696A1 US12/176,220 US17622008A US2009056696A1 US 20090056696 A1 US20090056696 A1 US 20090056696A1 US 17622008 A US17622008 A US 17622008A US 2009056696 A1 US2009056696 A1 US 2009056696A1
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Prior art keywords
conduit
fuel
oxidation
centralizer
heater
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US12/176,220
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Abdul Wahid Munshi
Peter Veenstra
Rachel Anna Worthen
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Shell USA Inc
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Individual
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Priority to US12/176,220 priority Critical patent/US20090056696A1/en
Assigned to SHELL OIL COMPANY reassignment SHELL OIL COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MUNSHI, ABDUL WAHID, VEENSTRA, PETER, WORTHEN, RACHEL ANNA
Publication of US20090056696A1 publication Critical patent/US20090056696A1/en
Abandoned legal-status Critical Current

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C3/00—Combustion apparatus characterised by the shape of the combustion chamber
    • F23C3/002—Combustion apparatus characterised by the shape of the combustion chamber the chamber having an elongated tubular form, e.g. for a radiant tube
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
    • F23C2900/03009—Elongated tube-shaped combustion chambers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
    • F23C2900/99001—Cold flame combustion or flameless oxidation processes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Definitions

  • This invention relates to a flameless combustion heater and a method for providing heat to a process.
  • Flameless combustion heaters are described in U.S. Pat. No. 7,025,940.
  • the patent describes a process heater utilizing flameless combustion, which is accomplished by preheating a fuel and combustion air to a temperature above the auto-ignition temperature of the mixture.
  • the fuel is introduced in relatively small increments over time through a plurality of orifices in a fuel gas conduit, which provide communication between the fuel gas conduit and an oxidation reaction chamber.
  • a process chamber is in heat exchange relationship with the oxidation reaction chamber.
  • Flameless combustion heaters provide several benefits over conventional fired heaters as described in the aforementioned patent. Flameless combustion heaters can, however, encounter problems related to the mixing of the fuel and oxidant in the oxidation reaction chamber.
  • Peak temperatures can occur near each opening in the fuel conduit, and this non-uniform heating causes non-uniform thermal expansion of the fuel conduit. Therefore, the fuel conduit has a tendency to bend, which bending positions the fuel conduit openings close to the wall of the oxidation reaction chamber and can result in hot spots that may lead to failure of the oxidation reaction chamber wall.
  • the fuel passing through the openings may exhibit a jet effect as it enters the oxidation reaction chamber. If the wall of the oxidation reaction chamber is too close to the opening then the fuel will impinge directly on the wall. This requires that a minimum distance be maintained between the outside of the fuel conduit and the inside of the oxidation reaction chamber.
  • the invention provides a flameless combustion heater comprising: an oxidation conduit and a fuel conduit having a plurality of centralizers attached to the external wall of the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit.
  • the invention also provides a method for providing heat to a process conduit comprising providing an oxidation conduit; providing a fuel conduit having a plurality of openings that provide fluid communication from within the fuel conduit to the oxidation conduit, and a plurality of centralizers attached to the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit; providing a process conduit in a heat exchange relationship with the oxidation conduit; introducing fuel into the fuel conduit; introducing an oxidant into the oxidation conduit; and introducing the fuel into the oxidation conduit through the plurality of openings such that flameless combustion occurs in the oxidation conduit.
  • FIG. 1 a depicts a two-tube flameless combustion heater with angled centralizers.
  • FIG. 1 b depicts an external view of a fuel conduit with angled centralizers.
  • the invention provides a flameless combustion heater that is used in the direct transfer of heat energy released by the flameless combustion of fuel.
  • the heater has many possible uses and applications including heating underground formations and heating process streams.
  • the flameless combustion heater is especially useful in conjunction with processes that carry out endothermic reactions, for example, dehydrogenation of alkylaromatic compounds and steam methane reforming.
  • the invention provides a flameless combustion heater with an improved design of the centralizers attached to the external wall of the fuel conduit.
  • the centralizers are protrusions attached to the external wall of the fuel conduit to prevent contact between the fuel conduit and the oxidation conduit.
  • the present invention addresses the aforementioned problems.
  • the use of angled centralizers results in improved mixing of the fuel and air within the heater, reduces or eliminates peak temperatures and helps prevent fuel impingement on the inside of the oxidation conduit.
  • Flameless combustion in a heater can be accomplished by preheating an oxidant stream and a fuel stream sufficiently that when the two streams are combined the temperature of the mixture exceeds the auto-ignition temperature of the mixture, but the temperature of the mixture is less than a temperature that would result in the oxidation upon mixing being limited by the rate of mixing as described in U.S. Pat. No. 7,025,940 which is herein incorporated by reference.
  • the auto ignition temperature of the mixture depends on the types of fuel and oxidant and the fuel/oxidant ratio.
  • the auto ignition temperature of mixtures used in a flameless combustion heater may be in a range of from 850° C. to 1400° C.
  • the auto ignition temperature may be reduced if an oxidation catalyst is employed in the heater because this type of catalyst effectively lowers the auto-ignition temperature of the mixture.
  • the fuel conduit provides for the controlled rate of fuel introduction into an oxidation conduit in a manner so as to provide for a desired heat release.
  • the heat release is determined in part by the location and number of openings, which can be tailored to each heater application.
  • the heat release may be constant over the length of the heater, or it may be decreasing or increasing over the length of the heater.
  • the flameless combustion reaction occurs at a lower temperature than that observed in conventional fired heaters. Due to the lower temperatures observed, and the efficiency of direct heating, the heater may be designed using lower cost materials resulting in reduced capital expenditure.
  • the flameless combustion heater has two main elements: an oxidation conduit and a fuel conduit.
  • the oxidation conduit may be a tube or pipe that has an inlet for oxidant, an outlet for oxidation products and a flow path between the inlet and outlet. Suitable oxidants include air, oxygen, and nitrous oxide.
  • the oxidant that is introduced into the oxidation conduit may be preheated such that when mixed with fuel, the mixture is at a temperature above the auto-ignition temperature of the mixture.
  • the oxidant may be heated externally to the flameless combustion heater.
  • the oxidant may be heated inside the heater by heat exchange with any of the streams inside the heater.
  • the oxidation conduit may have an internal diameter of from about 2 cm to about 20 cm.
  • the oxidant conduit may however be larger or smaller than this range depending on the heater requirements.
  • the fuel conduit transports fuel into the heater and introduces it into the oxidation conduit.
  • the fuel conduit may be a tube or pipe that has an inlet for fuel and a plurality of openings that provide fluid communication from within the fuel conduit to the oxidation conduit.
  • the fuel conduit may be located within and surrounded by the oxidation conduit. The fuel passes through the openings and into the oxidation conduit where it mixes with the oxidant and results in flameless combustion.
  • the fuel conduit may have an internal diameter of from about 1 cm to about 10 cm, preferably from about 1.5 cm to 5 cm. Depending on the design, however, the fuel conduit may have a diameter greater than 10 cm or less than 1 cm.
  • the openings can be drilled or cut into the wall of the fuel conduit.
  • the wall of the fuel conduit typically has a thickness of from about 0.25 cm to about 2.5 cm.
  • the openings may have cross sections that are circular, elliptical, rectangular, of another shape, or even irregularly shaped.
  • the openings preferably have a circular cross-section.
  • the openings may have a cross-sectional area of from about 0.001 cm 2 to about 2 cm 2 , preferably from about 0.03 cm 2 to about 0.2 cm 2 .
  • the size of the openings is determined by the desired rate of fuel introduction into the oxidation conduit, but openings that are too small may result in plugging.
  • the openings may be located along the fuel conduit at a distance of from 1 cm to 100 cm in the axial direction from any other opening.
  • the openings are preferably spaced from 15 cm to 50 cm apart in the axial direction.
  • the openings may be positioned in their respective radial planes at different orientations along the length of the fuel conduit.
  • the position of the openings may alternate 180 degrees in the radial plane along the length of the fuel conduit, or they may alternate 120 degrees or 90 degrees. Therefore the position of the openings in the fuel conduit may be such that their orientation in the radial plane alternates along the length of the fuel conduit with their orientations separated by 30 degrees to 180 degrees. It is preferred for the radial orientation of the openings to alternate at from 60 degrees to 120 degrees along the length of the fuel conduit.
  • a sintered plate may be used in addition to openings to provide fluid communication from the fuel conduit to the oxidation zone, and the openings in a sintered plate may have a diameter on the order of 10-100 microns.
  • Different openings along the length of the heater typically have the same cross-sectional area.
  • the cross-sectional area of the openings may be different to provide a desired heat release.
  • the spacing between openings along the fuel conduit may be different to provide a desired heat release.
  • the openings are typically the same shape. In the alternative, the openings may be different shapes.
  • Each centralizer has a proximal end, the end closest to the fuel inlet, and a distal end, the end farthest from the fuel inlet.
  • the centralizers may be triangular, rectangular, semicircular or any other shape.
  • the centralizers may be made of or coated with a material that is softer than the material used for the oxidation conduit so the centralizers do not damage the oxidation conduit when the fuel conduit is installed or removed.
  • the centralizers may be made of a softer metal or a ceramic.
  • the fuel conduit has a longitudinal axis defined by the line connecting the centers of the cross-sections of the conduit. At least one of the centralizers is angled with respect to the longitudinal axis of the fuel conduit.
  • the centralizer may be at any angle that is not parallel and not perpendicular to the longitudinal axis of the fuel conduit.
  • a centralizer that is neither parallel nor perpendicular to the longitudinal axis of the fuel conduit is hereinafter referred to as an angled centralizer.
  • An angled centralizer may be angled such that the angle formed between the centralizer and the longitudinal axis of the fuel conduit is less than ninety degrees.
  • An angled centralizer may be angled such that the angle formed between the centralizer and the longitudinal axis of the fuel conduit is less than sixty degrees or preferably less than forty-five degrees.
  • Positioning angled centralizers upstream (closer to the oxidant inlet) of a fuel conduit opening causes the oxidant to flow in a partially tangential direction as it passes the fuel conduit opening.
  • This tangential flow component reduces the jet effect and minimizes the minimum distance required between the conduits.
  • the partially tangential flow also contributes to improved mixing and a more even radial temperature profile. The heat is distributed more evenly around the circumference of the fuel conduit.
  • the angled centralizers may be straight or curved to provide desired flow characteristics of the oxidant in the oxidant conduit.
  • a straight centralizer is one in which the centralizer is located in one geometric plane.
  • a curved centralizer has portions that are in at least two non-parallel geometric planes. If the centralizer is curved, a portion of the centralizer may be parallel to the longitudinal axis of the fuel conduit.
  • FIGS. 1 a and 1 b depict a flameless combustion heater ( 10 ) with angled centralizers ( 16 ) as described above.
  • the heater ( 10 ) has a fuel conduit ( 12 ) and an oxidation conduit ( 14 ).
  • This type of heater is referred to as a two-tube heater.
  • Fuel conduit ( 12 ) is a cylindrical pipe that has an inlet ( 24 ) for fuel and a plurality of openings ( 20 ).
  • the oxidation conduit ( 14 ) is a cylindrical pipe that has an inlet ( 26 ) for preheated oxidant and an outlet ( 30 ) for combustion products. In the alternative, the oxidant may enter at ( 30 ) and the combustion products may exit at ( 26 ).
  • the fuel enters fuel conduit ( 12 ) via inlet ( 24 ) and then is mixed with oxidant in oxidation conduit ( 14 ) after it passes through the openings ( 20 ).
  • an angled centralizer ( 16 ) is positioned upstream (closer to the oxidant inlet) of each opening ( 20 ).
  • the flameless combustion heater may be operated at a variety of conditions depending on the particular configuration of heater and the heater application. Various examples and conditions are described in U.S. Pat. No. 5,255,742 and U.S. Pat. No. 7,025,940, which are herein incorporated by reference.
  • the flameless combustion heater may be used in an ethylbenzene dehydrogenation unit.
  • a process feedstock containing steam and ethylbenzene is fed to the dehydrogenation reactor.
  • the dehydrogenation reactor contains a suitable dehydrogenation catalyst, which may be an iron oxide based catalyst, and provides means for contacting the process feedstock with the dehydrogenation catalyst.
  • a dehydrogenation reactor effluent is discharged from the dehydrogenation reactor and introduced into the flameless combustion heater. Because the dehydrogenation reaction is an endothermic reaction, the dehydrogenation reactor effluent will have a lower temperature than that of the process feedstock to the dehydrogenation reactor.
  • the flameless combustion heater is used to heat the dehydrogenation reactor effluent before it is introduced into the second stage dehydrogenation reactor.
  • a dehydrogenation reactor effluent is discharged from the second stage reactor.
  • the dehydrogenation process may be carried out with more than two reactors in which case a flameless combustion heater may be placed in front of each additional reactor.
  • the flameless combustion heater described herein can be used in any application with any variation of the described details of centralizer orientation.

Abstract

A flameless combustion heater is described that comprises an oxidation conduit and a fuel conduit having a plurality of centralizers attached to the external wall of the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit. A method for providing heat to a process conduit is also described that comprises providing an oxidation conduit; providing a fuel conduit having a plurality of openings that provide fluid communication from within the fuel conduit to the oxidation conduit, and a plurality of centralizers attached to the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit; providing a process conduit in a heat exchange relationship with the oxidation conduit; introducing fuel into the fuel conduit; introducing an oxidant into the oxidation conduit; and introducing the fuel into the oxidation conduit through the plurality of openings such that flameless combustion occurs in the oxidation conduit.

Description

  • This application claims the benefit of U.S. Provisional Application No. 60/950,943, filed Jul. 20, 2007 which is hereby incorporated by reference.
    • FIELD OF THE INVENTION
  • This invention relates to a flameless combustion heater and a method for providing heat to a process.
    • BACKGROUND OF THE INVENTION
  • Flameless combustion heaters are described in U.S. Pat. No. 7,025,940. The patent describes a process heater utilizing flameless combustion, which is accomplished by preheating a fuel and combustion air to a temperature above the auto-ignition temperature of the mixture. The fuel is introduced in relatively small increments over time through a plurality of orifices in a fuel gas conduit, which provide communication between the fuel gas conduit and an oxidation reaction chamber. As described in the patent, a process chamber is in heat exchange relationship with the oxidation reaction chamber.
  • Flameless combustion heaters provide several benefits over conventional fired heaters as described in the aforementioned patent. Flameless combustion heaters can, however, encounter problems related to the mixing of the fuel and oxidant in the oxidation reaction chamber.
  • Peak temperatures can occur near each opening in the fuel conduit, and this non-uniform heating causes non-uniform thermal expansion of the fuel conduit. Therefore, the fuel conduit has a tendency to bend, which bending positions the fuel conduit openings close to the wall of the oxidation reaction chamber and can result in hot spots that may lead to failure of the oxidation reaction chamber wall.
  • In addition, the fuel passing through the openings may exhibit a jet effect as it enters the oxidation reaction chamber. If the wall of the oxidation reaction chamber is too close to the opening then the fuel will impinge directly on the wall. This requires that a minimum distance be maintained between the outside of the fuel conduit and the inside of the oxidation reaction chamber.
    • SUMMARY OF THE INVENTION
  • The invention provides a flameless combustion heater comprising: an oxidation conduit and a fuel conduit having a plurality of centralizers attached to the external wall of the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit.
  • The invention also provides a method for providing heat to a process conduit comprising providing an oxidation conduit; providing a fuel conduit having a plurality of openings that provide fluid communication from within the fuel conduit to the oxidation conduit, and a plurality of centralizers attached to the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit; providing a process conduit in a heat exchange relationship with the oxidation conduit; introducing fuel into the fuel conduit; introducing an oxidant into the oxidation conduit; and introducing the fuel into the oxidation conduit through the plurality of openings such that flameless combustion occurs in the oxidation conduit.
    • BRIEF DESCRIPTION OF THE DRAWING
  • FIG. 1 a depicts a two-tube flameless combustion heater with angled centralizers.
  • FIG. 1 b depicts an external view of a fuel conduit with angled centralizers.
    •  DETAILED DESCRIPTION OF THE INVENTION
  • The invention provides a flameless combustion heater that is used in the direct transfer of heat energy released by the flameless combustion of fuel. The heater has many possible uses and applications including heating underground formations and heating process streams. The flameless combustion heater is especially useful in conjunction with processes that carry out endothermic reactions, for example, dehydrogenation of alkylaromatic compounds and steam methane reforming. The invention provides a flameless combustion heater with an improved design of the centralizers attached to the external wall of the fuel conduit. The centralizers are protrusions attached to the external wall of the fuel conduit to prevent contact between the fuel conduit and the oxidation conduit.
  • The present invention addresses the aforementioned problems. The use of angled centralizers results in improved mixing of the fuel and air within the heater, reduces or eliminates peak temperatures and helps prevent fuel impingement on the inside of the oxidation conduit.
  • Flameless combustion in a heater can be accomplished by preheating an oxidant stream and a fuel stream sufficiently that when the two streams are combined the temperature of the mixture exceeds the auto-ignition temperature of the mixture, but the temperature of the mixture is less than a temperature that would result in the oxidation upon mixing being limited by the rate of mixing as described in U.S. Pat. No. 7,025,940 which is herein incorporated by reference. The auto ignition temperature of the mixture depends on the types of fuel and oxidant and the fuel/oxidant ratio. The auto ignition temperature of mixtures used in a flameless combustion heater may be in a range of from 850° C. to 1400° C. The auto ignition temperature may be reduced if an oxidation catalyst is employed in the heater because this type of catalyst effectively lowers the auto-ignition temperature of the mixture.
  • The fuel conduit provides for the controlled rate of fuel introduction into an oxidation conduit in a manner so as to provide for a desired heat release. The heat release is determined in part by the location and number of openings, which can be tailored to each heater application. The heat release may be constant over the length of the heater, or it may be decreasing or increasing over the length of the heater.
  • Because there is no visible flame associated with flameless combustion of a fuel, the flameless combustion reaction occurs at a lower temperature than that observed in conventional fired heaters. Due to the lower temperatures observed, and the efficiency of direct heating, the heater may be designed using lower cost materials resulting in reduced capital expenditure.
  • The flameless combustion heater has two main elements: an oxidation conduit and a fuel conduit. The oxidation conduit may be a tube or pipe that has an inlet for oxidant, an outlet for oxidation products and a flow path between the inlet and outlet. Suitable oxidants include air, oxygen, and nitrous oxide. The oxidant that is introduced into the oxidation conduit may be preheated such that when mixed with fuel, the mixture is at a temperature above the auto-ignition temperature of the mixture. The oxidant may be heated externally to the flameless combustion heater.
  • Alternatively, the oxidant may be heated inside the heater by heat exchange with any of the streams inside the heater. The oxidation conduit may have an internal diameter of from about 2 cm to about 20 cm. The oxidant conduit may however be larger or smaller than this range depending on the heater requirements.
  • The fuel conduit transports fuel into the heater and introduces it into the oxidation conduit. The fuel conduit may be a tube or pipe that has an inlet for fuel and a plurality of openings that provide fluid communication from within the fuel conduit to the oxidation conduit. The fuel conduit may be located within and surrounded by the oxidation conduit. The fuel passes through the openings and into the oxidation conduit where it mixes with the oxidant and results in flameless combustion. The fuel conduit may have an internal diameter of from about 1 cm to about 10 cm, preferably from about 1.5 cm to 5 cm. Depending on the design, however, the fuel conduit may have a diameter greater than 10 cm or less than 1 cm.
  • The openings can be drilled or cut into the wall of the fuel conduit. The wall of the fuel conduit typically has a thickness of from about 0.25 cm to about 2.5 cm. The openings may have cross sections that are circular, elliptical, rectangular, of another shape, or even irregularly shaped. The openings preferably have a circular cross-section.
  • The openings may have a cross-sectional area of from about 0.001 cm2 to about 2 cm2, preferably from about 0.03 cm2 to about 0.2 cm2. The size of the openings is determined by the desired rate of fuel introduction into the oxidation conduit, but openings that are too small may result in plugging. The openings may be located along the fuel conduit at a distance of from 1 cm to 100 cm in the axial direction from any other opening. The openings are preferably spaced from 15 cm to 50 cm apart in the axial direction. The openings may be positioned in their respective radial planes at different orientations along the length of the fuel conduit. For example, the position of the openings may alternate 180 degrees in the radial plane along the length of the fuel conduit, or they may alternate 120 degrees or 90 degrees. Therefore the position of the openings in the fuel conduit may be such that their orientation in the radial plane alternates along the length of the fuel conduit with their orientations separated by 30 degrees to 180 degrees. It is preferred for the radial orientation of the openings to alternate at from 60 degrees to 120 degrees along the length of the fuel conduit.
  • In one embodiment, a sintered plate may be used in addition to openings to provide fluid communication from the fuel conduit to the oxidation zone, and the openings in a sintered plate may have a diameter on the order of 10-100 microns.
  • Different openings along the length of the heater typically have the same cross-sectional area. In the alternative, the cross-sectional area of the openings may be different to provide a desired heat release. Additionally the spacing between openings along the fuel conduit may be different to provide a desired heat release. The openings are typically the same shape. In the alternative, the openings may be different shapes.
  • The orientation of the centralizers is important to the design and operation of the heater; and the centralizers may be angled to produce different temperature profiles and to overcome problems that arise due to the fluid and mixing dynamics of the heater system. Each centralizer has a proximal end, the end closest to the fuel inlet, and a distal end, the end farthest from the fuel inlet.
  • The centralizers may be triangular, rectangular, semicircular or any other shape. The centralizers may be made of or coated with a material that is softer than the material used for the oxidation conduit so the centralizers do not damage the oxidation conduit when the fuel conduit is installed or removed. For example, the centralizers may be made of a softer metal or a ceramic.
  • The fuel conduit has a longitudinal axis defined by the line connecting the centers of the cross-sections of the conduit. At least one of the centralizers is angled with respect to the longitudinal axis of the fuel conduit. The centralizer may be at any angle that is not parallel and not perpendicular to the longitudinal axis of the fuel conduit. A centralizer that is neither parallel nor perpendicular to the longitudinal axis of the fuel conduit is hereinafter referred to as an angled centralizer.
  • An angled centralizer may be angled such that the angle formed between the centralizer and the longitudinal axis of the fuel conduit is less than ninety degrees. An angled centralizer may be angled such that the angle formed between the centralizer and the longitudinal axis of the fuel conduit is less than sixty degrees or preferably less than forty-five degrees.
  • Positioning angled centralizers upstream (closer to the oxidant inlet) of a fuel conduit opening causes the oxidant to flow in a partially tangential direction as it passes the fuel conduit opening. This tangential flow component reduces the jet effect and minimizes the minimum distance required between the conduits. The partially tangential flow also contributes to improved mixing and a more even radial temperature profile. The heat is distributed more evenly around the circumference of the fuel conduit.
  • The angled centralizers may be straight or curved to provide desired flow characteristics of the oxidant in the oxidant conduit. A straight centralizer is one in which the centralizer is located in one geometric plane. A curved centralizer, on the other hand, has portions that are in at least two non-parallel geometric planes. If the centralizer is curved, a portion of the centralizer may be parallel to the longitudinal axis of the fuel conduit.
  • FIGS. 1 a and 1 b depict a flameless combustion heater (10) with angled centralizers (16) as described above. The heater (10) has a fuel conduit (12) and an oxidation conduit (14). This type of heater is referred to as a two-tube heater. Fuel conduit (12) is a cylindrical pipe that has an inlet (24) for fuel and a plurality of openings (20). The oxidation conduit (14) is a cylindrical pipe that has an inlet (26) for preheated oxidant and an outlet (30) for combustion products. In the alternative, the oxidant may enter at (30) and the combustion products may exit at (26). During operation, the fuel enters fuel conduit (12) via inlet (24) and then is mixed with oxidant in oxidation conduit (14) after it passes through the openings (20). Preferably, an angled centralizer (16) is positioned upstream (closer to the oxidant inlet) of each opening (20).
  • The flameless combustion heater may be operated at a variety of conditions depending on the particular configuration of heater and the heater application. Various examples and conditions are described in U.S. Pat. No. 5,255,742 and U.S. Pat. No. 7,025,940, which are herein incorporated by reference.
  • The flameless combustion heater may be used in an ethylbenzene dehydrogenation unit. A process feedstock containing steam and ethylbenzene is fed to the dehydrogenation reactor. The dehydrogenation reactor contains a suitable dehydrogenation catalyst, which may be an iron oxide based catalyst, and provides means for contacting the process feedstock with the dehydrogenation catalyst. A dehydrogenation reactor effluent is discharged from the dehydrogenation reactor and introduced into the flameless combustion heater. Because the dehydrogenation reaction is an endothermic reaction, the dehydrogenation reactor effluent will have a lower temperature than that of the process feedstock to the dehydrogenation reactor. The flameless combustion heater is used to heat the dehydrogenation reactor effluent before it is introduced into the second stage dehydrogenation reactor. A dehydrogenation reactor effluent is discharged from the second stage reactor. The dehydrogenation process may be carried out with more than two reactors in which case a flameless combustion heater may be placed in front of each additional reactor.
  • The flameless combustion heater described herein can be used in any application with any variation of the described details of centralizer orientation.

Claims (8)

1. A flameless combustion heater comprising: an oxidation conduit and a fuel conduit having a plurality of centralizers attached to the external wall of the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit.
2. A heater as claimed in claim 1 wherein the at least one centralizer is angled less than ninety degrees with respect to the longitudinal axis of the fuel conduit.
3. A heater as claimed in claim 1 wherein the at least one centralizer is curved such that at least a portion of the centralizer is angled with respect to the longitudinal axis of the fuel conduit.
4. A heater as claimed in claim 1 wherein all or a majority of all of the centralizers are angled with respect to the longitudinal axis of the fuel conduit.
5. A heater as claimed in claim 1 wherein the centralizers are made of a material different from that of the oxidation conduit wall.
6. A heater as claimed in claim 1 wherein the centralizers are coated with a material different from that of the oxidation conduit wall.
7. A heater as claimed in claim 1 wherein the centralizer is triangular shaped.
8. A method for providing heat to a process conduit comprising:
providing an oxidation conduit;
providing a fuel conduit having a plurality of openings that provide fluid communication from within the fuel conduit to the oxidation conduit, and a plurality of centralizers attached to the fuel conduit wherein at least one centralizer or portion of a centralizer is angled with respect to the longitudinal axis of the fuel conduit;
providing a process conduit in a heat exchange relationship with the oxidation conduit;
introducing fuel into the fuel conduit;
introducing an oxidant into the oxidation conduit; and
introducing the fuel into the oxidation conduit through the plurality of openings such that flameless combustion occurs in the oxidation conduit.
US12/176,220 2007-07-20 2008-07-18 Flameless combustion heater Abandoned US20090056696A1 (en)

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US12/176,220 US20090056696A1 (en) 2007-07-20 2008-07-18 Flameless combustion heater

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US95094307P 2007-07-20 2007-07-20
US12/176,220 US20090056696A1 (en) 2007-07-20 2008-07-18 Flameless combustion heater

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ATE511062T1 (en) 2011-06-15
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BRPI0814093A2 (en) 2015-02-03
RU2461775C2 (en) 2012-09-20
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JP2010534312A (en) 2010-11-04
WO2009014979A2 (en) 2009-01-29
AR067577A1 (en) 2009-10-14
RU2010106151A (en) 2011-08-27
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EP2176587A2 (en) 2010-04-21
CN101918761A (en) 2010-12-15

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