WO1986002140A1 - Air preheater for a compact boiler - Google Patents

Air preheater for a compact boiler Download PDF

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Publication number
WO1986002140A1
WO1986002140A1 PCT/US1985/001692 US8501692W WO8602140A1 WO 1986002140 A1 WO1986002140 A1 WO 1986002140A1 US 8501692 W US8501692 W US 8501692W WO 8602140 A1 WO8602140 A1 WO 8602140A1
Authority
WO
WIPO (PCT)
Prior art keywords
air
coil
heat exchange
flow
boiler
Prior art date
Application number
PCT/US1985/001692
Other languages
French (fr)
Inventor
Corporation Vapor
Karl E. Wollner
Original Assignee
Vapor Corp
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 Vapor Corp filed Critical Vapor Corp
Publication of WO1986002140A1 publication Critical patent/WO1986002140A1/en
Priority to FI861992A priority Critical patent/FI861992A0/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H9/00Details
    • F24H9/0084Combustion air preheating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B31/00Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements of dispositions of combustion apparatus
    • F22B31/08Installation of heat-exchange apparatus or of means in boilers for heating air supplied for combustion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L15/00Heating of air supplied for combustion
    • F23L15/04Arrangements of recuperators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/22Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
    • F24H1/40Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H8/00Fluid heaters characterised by means for extracting latent heat from flue gases by means of condensation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0003Recuperative heat exchangers the heat being recuperated from exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0083Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
    • F28D7/0091Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium the supplementary medium flowing in series through the units
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/024Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect 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 combustion gas heat • recovery for heating inlet air and improving overall boiler efficiency.
  • a heat exchange unit is disclosed that provides highly efficient secondary air heating in a- compact boiler such as disclosed in U.S. Patent 3,282,257, hereby incorporated by reference.
  • the heat exchange coil is positioned in a plenum space surrounding the coil bank of the boiler and is connected to an external cold water supply. Water is circulated through the heat exchange coil and preheated water is delivered to an end use or to the coil bank as preheated feed water.
  • an air preheater for a compact coil boiler wherein the heat exchange structure of the preheater is contained within an internal boiler plenum.
  • the heat exchange surfaces include- an essentially corrugated sepa ⁇ rator sheet having longitudinal flow interrupters mounted adjacent to the exhaust gas collector volume. Exhaust gas flow is channeled parallel to the hot side of the separator while traversing a path from a boiler coil outlet to exhaust stack. Combustion air is preheated through transverse flow along similar fins on the cold or opposite side of the corrugated separator sheet.
  • the flow separator acts to exchange heat at reduced pressure drop, and to increase effective heat exchange are for flow along the exhaust gas and combustion air sides, respectively.
  • a transverse hairpin type heat exchange coil is also provided.
  • the heat exchange coil is located in the plenum space surrounding the coil bank of the boiler.
  • An external cold water supply is connected to the heat transfer coil and heated water from the coil may be delivered to an end use or to the boiler as preheated feed water.
  • Figure 1 is a partial sectional view of a compact boiler including a preheater constructed in accordance with the principles of the present invention
  • Figure 2 is a semi-pictorial, partially cut-away view of a typical compact coil boiler, particularly showing the location of the air preheater of the present invention
  • Figure 3 is a partially pictorial view of a typical compact coil boiler, particularly showing the internal locations of boiler heat exchange coils, and air preheater with a source of combustion air;
  • Figure 4 is a detailed semirpictorial view of the preheater of the present invention particularly showing combustion gas and preheated air flow passages with flow " directions of the gases; - ⁇ -.-
  • Figure 5 is a partial sectional view of the preheater structure of the present invention showing action of the air side flow interrupters.
  • Figure 6 is an additional partial sectional view of an alternate embodiment of t__ air preheater; _
  • Figure 7 is a partial , sectional view of a further alternate embodiment of the preheater.
  • Figure 8 is a perspective, partially cut away view of the boiler without the preheater illustrating the heat exchange coil
  • Figure 9 is a perspective view of the coil bank of the boiler and the heat exchange coil
  • Figure 10 is a view taken along line 10-10 in Figure 9;
  • Figure 11 is a schematic illustration of an external use circuit including the heat exchange coil;
  • Figure 12 is a schematic illustration of a feed water circuit including the heat exchange coil.
  • Assembly 10 includes a burner 13 supplying predetermined fuel and air mixtures to a combustion chamber 14 where fuel and air mixtures generate high temperature combustion gases that exit through combustion chamber exit or choke 18.
  • Combustion chamber 14 utilizes refractory material capable of with ⁇ standing high temperatures for the walls 17 and to define the chamber outlet or choke 18.
  • Burner combustion air is provided by a blower assembly 30 (FIG. 2) communicating with the interior of boiler outer shell 12 via a blower.inlet 31.
  • Blower inlet 31 communicates with an annular plenum chamber 32 and blower 30 pressurizes the plenum chamber 32 forcing air through burner 13 and into the combustion chamber 14.
  • Combustion gases exit choke 18, enter a coil inlet zone 20, and under pressure, flow through inter ⁇ stices 19 of coil turns 21. Exhaust gases exiting the coil turns 21 are collected in a combustion or flue gas collecting chamber 24.
  • Flue gas collection chamber 24 is in fluid communication with an air t preheater assembly 26, lying entirely within flue gas collection chamber 24, adjacent combustion chamber 14.
  • Combustion gases passing through coil turns 21 raise the temperature of liquid contained within the coils. Combustion gases then pass through air preheater 26 exiting to the atmosphere via stack or outlet 28.
  • Pre- heater 26 utilizes a separator or wall 34 having an essentially corrugated or fluted surface with flow inter ⁇ rupters 36 fixed to alternate convolutions of the surface.
  • Wall 34 and interrupters 36 are mounted on the boiler bulkhead 33.
  • the flow interrupters 36 and wall 34 define isolated flow areas 35 and 37 for the air and exhaust gas sides of the preheater 26, respectively. Exhaust gas and preheated air are prevented from mixing by separator 34, longitudinal seals or bulkheads 38, and a transverse or end seal or bulkhead 40.
  • air preheater 26 is in fluid com ⁇ munication with the flue gas collection chamber 24 at an open end 39 adjacent bulkhead 33.
  • a lower edge 39A of open end 39 engages and -extends slightly above separator 34, thereby providing a gas flow path via upper passages 37. Gases enter the air preheater 26 through open end 39, traverse the upper surfaces of passages 37 and exit in a vertical direction through stack outlet 28.
  • combustion air entering plenum 32 via the blower inlet 31 flows below separator 34 in a path perpendicular to the flutes or corrugations of the surface 34 and interrupters 36 generating air side flow patterns including turbulent vortices 41 (FIG. 5) .
  • this combination of a corrugated surface 34 and interrupters 36 substantially increases the heat transfer effectiveness of the combination through destruction of the boundary layer along surface 34.
  • the higher temperature gases flowing in a direction parallel to the flow interrupters 36 above surface 34 - by virtue of their high temperature and higher viscosity, provide substantially increased heat transfer without a substan ⁇ tial increase in exhaust gas pressure drop. Excessive pressure drop in the exhaust gas path is highly undesir ⁇ able.
  • Heat transferred to combustion air supplied by blower assembly 30 raises the air temperature substan ⁇ tially resulting in an increase in overall boiler combus ⁇ tion efficiency. This increase is • achieved without appreciable combustion gas pressure drop along the exhaust path to the stack 28. Additionally, novel means has been provided for increasing boiler efficiency without substantially increasing combustion air blower requirements. Further, the heat exchanger of this inven ⁇ tion provides increased efficiency entirely within the initial confines of existing compact boilers, allowing installment of the air preheater* 26 in existing boilers without structure modifications.
  • a sepa ⁇ rator 34A is bent or formed to define vertically extending interrupters 36A.
  • Discontinuous separators 34B in Figure 4 are each formed at a right angle to define vertical separators 36B.
  • boiler 10 includes a heat transfer or economizer coil 100.
  • Heat transfer coil 100 is mounted in the plenum chamber 32 and surrounds the coils or coil bank 21. In this position, coil 100 is heated by exhaust gas of a lower temperature since the gas has passed through interstices 19 and over coils 21. Consequently, water flowing through heat transfer coil 100 is of a lower temperature than the fluid flowing through coils 21. This lower temperature fluid is useful as hot water for customer use or as feedwater for_coils 21.
  • Heat transfer coil 100 is of a hairpin configu ⁇ ration and surrounds at least a portion of the coil bank defined by coils 21. In the preferred embodiment illus- trated, approximately seventy percent of the coil bank is surrounded.
  • Coil 100 includes an inlet 102 that may be" con ⁇ nected to external cold water supply.
  • An outlet 104 is also provided.
  • Outlet 104 may be connected to a tap or other device to allow customer usage.
  • cold water may be provided from a supply 106 to a pump 108.
  • Pump 108 is connected to inlet 102 of coil 100. The water is then heated and flows through outlet 104 to a tap or similar device.
  • boiler 110 is connected to a condensate receiver tank 112. Water- from tank 112 is pumped by pump 114 through heat exchanger coil 100. Heated water is passed into drum 116 for storage and pumped into boiler 10 and coils 21 by pump 118 as preheated feedwater thereby increasing the efficiency of boiler 10.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Air Supply (AREA)

Abstract

A coil boiler (10) includes an air preheater (26) for recovering energy from exhaust gases to heat secondary combustion air. The air preheater is defined by a compact heat exchange structure. The heat exchange structure provides lateral flow interrupters (36) on a combustion gas side, and transverse flow (35) interruption on the flow resistance to exhaust combination gases is minimized while heat transfer to inlet air is substantially increased through flow interruption. A transverse hair-pin heat exchange coil (100) is also provided. The heat exchange coil is located in plenum space (40) in the boiler surrounding the coil bank (22) of the boiler. The heat exchange coil is connected to an external water supply. Water circulating through the heat exchange coil is heated and delivered to the coil bank as preheated feedwater or is delivered to an end use location.

Description

-1-
Ϊ. "AIR PREHEATER FOR A COMPACT BOILER"
BACKGROUND OF THE INVENTION
This invention relates to combustion gas heat recovery for heating inlet air and improving overall boiler efficiency. In particular, a heat exchange unit is disclosed that provides highly efficient secondary air heating in a- compact boiler such as disclosed in U.S. Patent 3,282,257, hereby incorporated by reference.
Known approaches to combustion air preheating such as disclosed in U.S. Patent 3,838,666 have been in existence for some time; however, these structures are expensive and complicated additions to compact boilers. Further, the disclosed techniques require rerouting of exhaust gases with increases in pressure drop over the exhaust gas path. The effectiveness of this approach is, generally speaking, not cost effective. " Applicant has discovered that use of a novel air preheating heat exchange structure located within the existing boiler housing can provide substantial increases in overall boiler efficiency. _These efficiencies are attained without substantial increase in pressure drop, particularly along the exhaust gas discharge path. The novel heat exchange structure disclosed provides a cost-effective means for increasing boiler efficiency and does not require complicated and expensive ancillary structures or appurtenances to the boiler. It has also been discovered that further boiler efficiency can be obtained by the inclusion of a trans¬ verse hairpin type heat exchange coil. The heat exchange coil is positioned in a plenum space surrounding the coil bank of the boiler and is connected to an external cold water supply. Water is circulated through the heat exchange coil and preheated water is delivered to an end use or to the coil bank as preheated feed water.
Accordingly, it is an object of this invention to provide increased efficiency of a compact coil boiler through . utilization of a novel heat exchange structure and coil placed within the existing boiler housing.
It is a further object of this invention to provide a heat exchange unit for recovering heat from exhaust gases of a boiler wherein the existing gas flow is not appreciably affected.
It is an additional object of this invention to provide a heat exchange structure for heat recovery and/or air preheating in a compact boiler which utilizes readily available material in a simple structure.
It is an additional object of this invention to provide a heat exchanger design for using energy from exhaust gases for combustion air preheating in a compact boiler wherein exhaust gas or "hot side" pressure drops are minimized, and combustion air or "cold side" heat exchange is enhanced while utilizing identical heat transfer surface geometry.
It is yet another object of this invention to provide an air preheater and heat exchange coil for increasing efficiency of a compact coil boiler within original boiler envelopes utilizing low cost, easily manuf ctured, and readily available material in a simple structure.
SUMMARY OF THE INVENTION
In accordance with the invention disclosed, an air preheater for a compact coil boiler is provided wherein the heat exchange structure of the preheater is contained within an internal boiler plenum. The heat exchange surfaces include- an essentially corrugated sepa¬ rator sheet having longitudinal flow interrupters mounted adjacent to the exhaust gas collector volume. Exhaust gas flow is channeled parallel to the hot side of the separator while traversing a path from a boiler coil outlet to exhaust stack. Combustion air is preheated through transverse flow along similar fins on the cold or opposite side of the corrugated separator sheet. The flow separator acts to exchange heat at reduced pressure drop, and to increase effective heat exchange are for flow along the exhaust gas and combustion air sides, respectively.
Use .of identical structure for high/low tempera¬ ture gas flows provides substantial increase in heat transfer while remaining totally within the gas collecting portion of the boiler. A transverse hairpin type heat exchange coil is also provided. The heat exchange coil is located in the plenum space surrounding the coil bank of the boiler. An external cold water supply is connected to the heat transfer coil and heated water from the coil may be delivered to an end use or to the boiler as preheated feed water.
BRIEF DESCRIPTION OF THE DRAWINGS
Other objects and advantages of the invention will become apparent upon reading the following detailed description and upon reference to the drawings in which:
Figure 1 is a partial sectional view of a compact boiler including a preheater constructed in accordance with the principles of the present invention; Figure 2 is a semi-pictorial, partially cut-away view of a typical compact coil boiler, particularly showing the location of the air preheater of the present invention;
Figure 3 is a partially pictorial view of a typical compact coil boiler, particularly showing the internal locations of boiler heat exchange coils, and air preheater with a source of combustion air;
Figure 4 is a detailed semirpictorial view of the preheater of the present invention particularly showing combustion gas and preheated air flow passages with flow"directions of the gases; -<-.-
Figure 5 is a partial sectional view of the preheater structure of the present invention showing action of the air side flow interrupters.
Figure 6 is an additional partial sectional view of an alternate embodiment of t__ air preheater; _
Figure 7 is a partial, sectional view of a further alternate embodiment of the preheater;
Figure 8 is a perspective, partially cut away view of the boiler without the preheater illustrating the heat exchange coil;
Figure 9 is a perspective view of the coil bank of the boiler and the heat exchange coil;
Figure 10 is a view taken along line 10-10 in Figure 9; Figure 11 is a schematic illustration of an external use circuit including the heat exchange coil; and
Figure 12 is a schematic illustration of a feed water circuit including the heat exchange coil.
DETAILED DESCRIPTION OF THE INVENTION
With reference to Figures 1-5, a boiler assembly 10 is illustrated. Assembly 10 includes a burner 13 supplying predetermined fuel and air mixtures to a combustion chamber 14 where fuel and air mixtures generate high temperature combustion gases that exit through combustion chamber exit or choke 18. Combustion chamber 14 utilizes refractory material capable of with¬ standing high temperatures for the walls 17 and to define the chamber outlet or choke 18.
Burner combustion air is provided by a blower assembly 30 (FIG. 2) communicating with the interior of boiler outer shell 12 via a blower.inlet 31. Blower inlet 31 communicates with an annular plenum chamber 32 and blower 30 pressurizes the plenum chamber 32 forcing air through burner 13 and into the combustion chamber 14. Combustion gases exit choke 18, enter a coil inlet zone 20, and under pressure, flow through inter¬ stices 19 of coil turns 21. Exhaust gases exiting the coil turns 21 are collected in a combustion or flue gas collecting chamber 24. Flue gas collection chamber 24 is in fluid communication with an air tpreheater assembly 26, lying entirely within flue gas collection chamber 24, adjacent combustion chamber 14.
Combustion gases passing through coil turns 21 raise the temperature of liquid contained within the coils. Combustion gases then pass through air preheater 26 exiting to the atmosphere via stack or outlet 28.
With particular reference to Figure 4, air pre¬ heater 26 of the present invention is illustrated. Pre- heater 26 utilizes a separator or wall 34 having an essentially corrugated or fluted surface with flow inter¬ rupters 36 fixed to alternate convolutions of the surface. Wall 34 and interrupters 36 are mounted on the boiler bulkhead 33. The flow interrupters 36 and wall 34 define isolated flow areas 35 and 37 for the air and exhaust gas sides of the preheater 26, respectively. Exhaust gas and preheated air are prevented from mixing by separator 34, longitudinal seals or bulkheads 38, and a transverse or end seal or bulkhead 40. In operation, air preheater 26 is in fluid com¬ munication with the flue gas collection chamber 24 at an open end 39 adjacent bulkhead 33. A lower edge 39A of open end 39 engages and -extends slightly above separator 34, thereby providing a gas flow path via upper passages 37. Gases enter the air preheater 26 through open end 39, traverse the upper surfaces of passages 37 and exit in a vertical direction through stack outlet 28.
Similarly, combustion air entering plenum 32 via the blower inlet 31 flows below separator 34 in a path perpendicular to the flutes or corrugations of the surface 34 and interrupters 36 generating air side flow patterns including turbulent vortices 41 (FIG. 5) . It has been discovered that this combination of a corrugated surface 34 and interrupters 36 substantially increases the heat transfer effectiveness of the combination through destruction of the boundary layer along surface 34. It _has also been discovered that the higher temperature gases flowing in a direction parallel to the flow interrupters 36 above surface 34,- by virtue of their high temperature and higher viscosity, provide substantially increased heat transfer without a substan¬ tial increase in exhaust gas pressure drop. Excessive pressure drop in the exhaust gas path is highly undesir¬ able.
Heat transferred to combustion air supplied by blower assembly 30 raises the air temperature substan¬ tially resulting in an increase in overall boiler combus¬ tion efficiency. This increase is achieved without appreciable combustion gas pressure drop along the exhaust path to the stack 28. Additionally, novel means has been provided for increasing boiler efficiency without substantially increasing combustion air blower requirements. Further, the heat exchanger of this inven¬ tion provides increased efficiency entirely within the initial confines of existing compact boilers, allowing installment of the air preheater* 26 in existing boilers without structure modifications.
With reference to Figure 6, for example, a sepa¬ rator 34A is bent or formed to define vertically extending interrupters 36A. Discontinuous separators 34B in Figure 4 are each formed at a right angle to define vertical separators 36B.
As best illustrated in Figs. 8-10, boiler 10 includes a heat transfer or economizer coil 100. Heat transfer coil 100 is mounted in the plenum chamber 32 and surrounds the coils or coil bank 21. In this position, coil 100 is heated by exhaust gas of a lower temperature since the gas has passed through interstices 19 and over coils 21. Consequently, water flowing through heat transfer coil 100 is of a lower temperature than the fluid flowing through coils 21. This lower temperature fluid is useful as hot water for customer use or as feedwater for_coils 21.
Heat transfer coil 100 is of a hairpin configu¬ ration and surrounds at least a portion of the coil bank defined by coils 21. In the preferred embodiment illus- trated, approximately seventy percent of the coil bank is surrounded.
Coil 100 includes an inlet 102 that may be" con¬ nected to external cold water supply. An outlet 104 is also provided. Outlet 104 may be connected to a tap or other device to allow customer usage. For example, referring to Fig. 11, cold water may be provided from a supply 106 to a pump 108. Pump 108 is connected to inlet 102 of coil 100. The water is then heated and flows through outlet 104 to a tap or similar device. As illustrated in Fig. 12, a cold water supply
110 is connected to a condensate receiver tank 112. Water- from tank 112 is pumped by pump 114 through heat exchanger coil 100. Heated water is passed into drum 116 for storage and pumped into boiler 10 and coils 21 by pump 118 as preheated feedwater thereby increasing the efficiency of boiler 10.
Thus, it is apparent that there has been provided in accordance with the invention, an air pre¬ heater for compact boilers that fully satisfies the objects, aims and advantages set forth. Although the air preheater has been disclosed utilizing a specific type and variety of a corrugated or fluted surface with continuous longitudinal flow interrupters, it is evident that many alternatives and/or modifications including but not limited to Figures 6 and 7, will be apparent to those skilled in the art in the light of the foregoing description. It is therefore intended to embrace all alternatives, modifications, and variations as fall within the spirit and scope of the appended claims. I claim:

Claims

1. In a compact fluid heater of the type including a shell, a combustion chamber in said shell, coils mounted in said shell, a plenum chamber surrounding said coils, an air blower communicating with said plenum and a source of air, an exhaust gas outlet in said shell, the improvement comprising: an air preheater adjacent said coils and inter- mediate said chamber and plenum including impermeable heat conducting first and second surfaces for isolating exhaust gas and air flows, respectively; said first surface extending in a first direc- tion from said second surface to define a lateral flow channel along said first surface for directing said exhaust gas to said exhaust gas outlet; said first surface extending in a second direc- tion from said second surface to define a flow interrupter transverse to said lateral flow channel for interrupting said air flow.
2. The fluid heater of claim 1 wherein said second surface comprises a fluted surface having convolu- tions parallel to exhaust gas flow.
3. The fluid heater of claim 1 wherein said first surface extends above said second surface in said first direction and • below said second surface in said second direction.
4. The fluid heater of claim 1 further comprising first means for directing said exhaust gas above said second surface and second means for directing said air below said second surface.
5. The fluid heater of claim 1 further comprising a heat exchange coil mounted in said plenum chamber surrounding said coils, said heat exchange coil including an inlet for connection to an external supply of fluid and an outlet for connection to an end use.
6. In a compact boiler, comprising: a generally cylindrical combustion chamber having a burner at one end and a distal outlet for deliv- ering combustion gases; a generally cylindrical coil bank concentric to and axially spaced from said combustion chamber having a central gas inlet and radial interstices for channelling combustion gases from the interior of said coil bank to an outer periphery; a combustion air plenum for supplying air to said combustion chamber; a flue gas collector adjacent said outer peri- phery of said coil bank; " a stack for discharging exhaust gases; a passage extending from said flue gas collector to said plenum for communicating said collector and said stack; a separator extending the length of said pas- sage; -first means communicating flue gas from said col- lector on a first side of said separator; second means communicating air from an air source to a second side of said separator; rectangular transverse extensions on and gener- ally perpendicular to said separator, said extensions defining longitudinal flue gas flow channels on said first side of said separator, and air flow interrupters on said second side; wherein flue gases exiting said collector flow through said channels, and air entering flows across said interrupters thereby raising the temperature of said air.
7 - The compact boiler set forth in claim 6 wherein said extensions are transverse to the direction *
-11-
of flow of said air and of a configuration to create eddy currents in said air flow.
8. The compact boiler set forth in claim 6 wherein said separators is of an undulating configura- tion.
9. The compact boiler set forth in claim 6 further comprising a heat exchange coil mounted in said plenum surrounding said coil bank, said heat exchange coil including an inlet for connection to an external fluid supply and an outlet.
10. The compact boiler set forth in claim 9 wherein said heat exchange coil is of a hairpin configu- ration.
11. A compact boiler, comprising; a housing, a coil bank mounted in said housing, a combustion chamber in said shell, said coil bank surrounding said combustion chamber, a plenum chamber surrounding said coil bank, a heat exchange coil mounted in said plenum chamber surrounding said coil bank*, said heat exchange coil including an inlet for connection to a supply of fluid.
12. The compact boiler claimed in claim 11 wherein said heat exchange coil is of a hairpin configu- ration.
13. The compact boiler claimed in claim 11 further comprising an air preheater mounted in said plenum chamber, said preheater including first and second surfaces, " said first surface in a first direction from said second surface to define a lateral flow channel and extending in a second direction from said second surface to define a flow interrupter transverse to said lateral flow channel for interrupting said air flow.
14. ...The compact boiler claimed in claim 11 wherein said second surface comprises a fluted surface having convolutions parallel to exhaust gas flow.
15. A compact boiler, comprising; a shell, a coil bank mounted in said shell, a plenum chamber surrounding said coil bank, a combustion chamber in said shell surrounded by said coil bank, an air preheater in said plenum, said preheater including first and second surfaces for isolating exhaust gas and air flows, respectively, said first surface extending in a first direc- tion from said second surface to define a lateral flow channel along said first surface for directing said exhaust gas to said exhaust gas outlet, said first surface extending in a second direc- tion from said second surface to define a flow interrupter transverse to said lateral flow channel for interrupting said air flow, a heat exchange coil mounted in said plenum chamber surrounding said coil bank, said heat exchange coil including an inlet for connection to a supply of- fluid and an outlet.
16. The boiler set forth in claim 15 wherein said heat exchange coil is of a hairpin.configuration.
17. The boiler set forth in claim 15 wherein said second surface comprises a fluted surface including convolutions parallel to exhaust gas flow.
PCT/US1985/001692 1984-09-28 1985-08-29 Air preheater for a compact boiler WO1986002140A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FI861992A FI861992A0 (en) 1984-09-28 1986-05-13 LUFTFOERVAERMARE FOER EN KOMPAKT AONGPANNA.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US65609884A 1984-09-28 1984-09-28
US656,098 1984-09-28

Publications (1)

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WO1986002140A1 true WO1986002140A1 (en) 1986-04-10

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ID=24631614

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Application Number Title Priority Date Filing Date
PCT/US1985/001692 WO1986002140A1 (en) 1984-09-28 1985-08-29 Air preheater for a compact boiler

Country Status (6)

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EP (1) EP0197049A4 (en)
JP (1) JPS62500680A (en)
CA (1) CA1268384A (en)
FI (1) FI861992A0 (en)
NO (1) NO161234C (en)
WO (1) WO1986002140A1 (en)

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EP3740715A4 (en) * 2018-01-19 2022-02-16 DRI-Steem Corporation Condensing, ultra-low nox gas-fired humidifier
CN116498991A (en) * 2023-04-04 2023-07-28 江阴金童石化装备有限公司 Promotion reciprocating heat accumulation formula air heater

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EP3740715A4 (en) * 2018-01-19 2022-02-16 DRI-Steem Corporation Condensing, ultra-low nox gas-fired humidifier
US11421899B2 (en) 2018-01-19 2022-08-23 Dri-Steem Corporation Condensing, ultra-low NOx gas-fired humidifier
US11940178B2 (en) 2018-01-19 2024-03-26 Dri-Steem Corporation Condensing, ultra-low NOx gas-fired humidifier
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CN116498991A (en) * 2023-04-04 2023-07-28 江阴金童石化装备有限公司 Promotion reciprocating heat accumulation formula air heater

Also Published As

Publication number Publication date
FI861992A (en) 1986-05-13
EP0197049A1 (en) 1986-10-15
CA1268384A (en) 1990-05-01
JPS62500680A (en) 1987-03-19
EP0197049A4 (en) 1987-08-10
NO862099L (en) 1986-05-27
FI861992A0 (en) 1986-05-13
NO161234C (en) 1989-07-19
NO161234B (en) 1989-04-10

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