US3090332A - Gas recirculation duct - Google Patents

Gas recirculation duct Download PDF

Info

Publication number
US3090332A
US3090332A US79356A US7935660A US3090332A US 3090332 A US3090332 A US 3090332A US 79356 A US79356 A US 79356A US 7935660 A US7935660 A US 7935660A US 3090332 A US3090332 A US 3090332A
Authority
US
United States
Prior art keywords
duct
furnace
gas pass
gas
gases
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
US79356A
Inventor
Henry E Burbach
Otto T Hipp
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.)
Combustion Engineering Inc
Original Assignee
Combustion Engineering Inc
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 Combustion Engineering Inc filed Critical Combustion Engineering Inc
Priority to US79356A priority Critical patent/US3090332A/en
Application granted granted Critical
Publication of US3090332A publication Critical patent/US3090332A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G5/00Controlling superheat temperature
    • F22G5/06Controlling superheat temperature by recirculating flue gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22GSUPERHEATING OF STEAM
    • F22G5/00Controlling superheat temperature
    • F22G5/04Controlling superheat temperature by regulating flue gas flow, e.g. by proportioning or diverting

Definitions

  • the steam temperature In modern steam generating plants, it is found that as the load requirements decrease, the steam temperature also decreases, and this is not desirable. To obtain greatest turbine efliciency, the steam should be kept at a constant temperature, regardless of the load requirements.
  • One of the methods of maintaining constant steam temperature is by gas recirculation. As the load decreases, more combustion gas is recirculated back to the furnace. This prevents to a large extent the amount of heat that passes from the combustion gases within the furnace by radiation to the tubes lining the furnace walls, and hence leaves a greater amount of heat in the gases leaving the furnace outlet to be absorbed by the convection heat exchange members, such as the superheater and reheater. Also, a greater volume of gas leaves the furnace when recirculated gas is introduced into the furnace. In this manner, the steam temperature is maintained substantially constant, regardless of load changes.
  • This invention is particularly directed to the construction and position of the gas recirculation duct extending between the gas pass downstream of the heat exchange means and the furnace, and especially in a coal fired furnace.
  • a coal fire furnace the hot combustion gases leaving the furnace contain a large amount of dust, fly ash and other foreign particles.
  • dust collectors are usually installed in the recirculating gas ducts, on coal fired units, upstream of the fan to remove the dust and ash therefrom. If it is not removed, serious problems can result due to the large amount of such ash and dust being reintroduced into the furnace along with the recirculated gas.
  • a portion of the recirculated gas duct is contained within the gas pass, and the openings thereto are on the underside, such that the gases entering must pass through a 180 turn.
  • the duct within the gas pass need not be insulated.
  • the temperature of the gases in the gas pass dovtmstream of the heat exchange members is approximately 700 F., and normally the entire gas recirculation duct must be insulated.
  • positioning a portion of the duct within the gas pass results in a substantial saving of space. In large modern boilers this is of significance.
  • Another advantage is that only one opening through the wall of the gas pass must be sealed, this being the opening through which the recirculated gas duct extends. In ordinary unit-s utilizing gas recirculation, two or more openings are usually provided for attachment of gas recirculation ducts, which connections must be suitably sealed.
  • FIGURE 1 is a sectional side elevation of a furnace employing gas recirculation
  • FIGURE 2 is a view of the furnace taken along lines 22 of FIGURE 1.
  • 1d designates a horizontal cyclone fired furnace utilizing pulverized coal as a fuel.
  • the walls of the furnace are lined with tubes 12, which absorb heat radiantly from the furnace gases to produce steam. These tubes 12 are supplied with water from lower headers 13. Pulverized coal along with air is introduced into the furnace through horizontal cyclone burners 14, the air being supplied by duct 16. This air is heated in air preheater 18 prior to introduction into the furnace.
  • the furnace 10 contains a hopper bottom 20, the walls of which are also lined with tubes 12. Below the furnace is an ash compartment 22, into which the ash from the furnace is allowed to fall.
  • Gas pass .26 contains convectionsteam heating means 28, such as a superheater and reheater, where a substantial portion of the heat of the hot combustion gases is withdrawn therefrom.
  • convectionsteam heating means 28 such as a superheater and reheater, where a substantial portion of the heat of the hot combustion gases is withdrawn therefrom.
  • the gases continue on past economizer 3i where more of the heat is utilized, and then flows on to air preheater 18 by means of duct 32.
  • a duct 34 extends into gas pass 26, and contains openings 31, 35, and 36 on the underside thereof by means of which the gases are allowed to enter the duct.
  • the duct 34 is connected to duct 33 outside of the gas pass 26, which duct 33 passes recirculated gas to fan 39 by means of ducts 38.
  • Manifold or duct 41 receives the discharge of fan 39. Extending transversely from manifold 41 are a plurality of ducts 42, which are connected to openings 44 in the bottom or throat of hopper 20.
  • the tubes .12 are staggered, as shown at 46 in FIGURE 1, to allow entrance of the recirculated gas therebe-tween.
  • Duct 33 contains damper 37, by means of which the amount of recirculated gas passing back to the furnace can be regulated.
  • This damper can be adjusted manually or automatically, as is well known in the art, to increase the amount of gas recirculation as the load requirements decrease, to thereby maintain a constant steam temperature.
  • the openings 31, 35, and 36 are substantially evenly spaced across the entire width of gas pass 26.
  • duct 34 is centrally located within the gas pass 26. This prevents an imbalance of gas flow through the heat exchange means 28 and 30 directly above duct 34, due to the suction created by fan 39 at openings 31, 35, and 36. Since the suction effect will be greatest near the left end, the openings can be made progressively larger, openings 36 being the largest.
  • Duct 34 is supported directly beneath economizer 30 by means of I-bearns 48, which can also be used to support the economizer.
  • a circular or sloping contour at the top of duct 33 presents a streamlined surface, thereby insuring a minimum resistance to gas flow, and thus very little draft loss, as well as achieving a self-cleaning surface.
  • any gases to be recirculated back to the furnace must pass through a turn to enter openings 31, 35, and 36 in duct 34. Due to the velocity of the flow through gas pass 26, and the force of gravity, very little fly ash, dust, or other foreign particles will be drawn into openings 31, 35, and as :by the suction created by operation of fan 39. The sloping or circular top edge of duct 33 will tend to force the fly ash and dust impinging thereon away from the duct, thus preventing it from entering openings 31, 35, and 36.
  • fly ash carryover to the gas recirculation system is reduced simply and efiiciently, resulting in reduction of fan maintenance costs and reduction of reintroduction of such fly ash into the furnace.
  • the unit is compact and economical, there being no need for insulation of the duct within the gas pass.
  • a steam generating unit comprising a furnace, fuel and air inlets for said furnace, an outlet leading from the upper portion of said furnace through which the hot combustion gases pass, vertical wall means forming a gas pass containing heat exchange means, said gas pass being connected to said furnace outlet such that the gases pass downwardly therethrough, a duct in communication at one end with the gas pass downstream of said heat exchange means, and in communication at its other end with said furnace, a fan in said duct, a portion of said duct contained within said gas pass, said portion of said duct extending across the center portion of the gas pass, a plurality of openings in said duct being evenly spaced across the width of the gas pass through which gases are allowed to flow from the gas pass into said duct, said openings being positioned on the underside of said duct, such that the gases flowing in the gas pass must make a 180 turn to enter said openings, said openings progressively decreasing in size, the smallest opening being located the closest to the fan, so there is no imbalance of flow of gases through the portion of the gas pass containing
  • a furnace fuel and air inlets for said furnace, an outlet leading from said furnace through which the hot combustion gases pass, Wall means forming a gas pass containing heat exchange means, said gas pass being connected to said furnace outlet, a duct in communication at one end with the gas pass downstream of said heat exchange means, and in communication at its other end with said furnace, a fan in said duct, a portion of said duct contained within the gas pass, said portion of said duct extending across the center portion of the gas pass, a plurality of openings in said duct through which gases are allowed to flow from the gas pass into said duct, said openings being positioned such that the gases flowing in the gas pass must make a 180 turn to enter such openings, thereby preventing ash or other foreign particles carried by said gases from entering the duct, said openings progressively decreasing in size, the smallest opening being located the closest to the fan, so there is no imbalance of flow of gases through the portion of the gas pass containing said heat exchange means due to the suction effect of said fan

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion Of Fluid Fuel (AREA)

Description

y 1, 1963 H. E. BURBACH ETAL 3,090,332
GAS RECIRCULATION DUCT 2 Sheets-Sheet 1 Filed Dec. 29, 1960 hl llppuhllw lilrlr with. illvnllllhh hlp up INVENTORS: HENRY E. BURBACH OTTO T. HIPP ATTORiEY y 1, 1963 H. E. BURBACH ETAL 3,090,332
GAS RECIRCULATION DUCT Filed Dec. 29, 1960 2 Sheets-Sheet 2 INVENTORS: HENRY E. BURBACH OTTO T. HIPP BY Q ATTORNEY United States Patent Ofiice 3,999,332 Patented May 21, 1963 3,ii90,332 GAS RECIRCULATION DUCT Henry E. Burbach, Avon, and fltto T. Hipp, West Hartford, Conn, assignors to Combustion Engineering, Inc, Windsor, Conn, a corporation of Delaware Filed Dec. 29, 1960, Ser. No. 79,356 2 Claims. (Cl. 110-49) This invention relates to steam generating units employing gas recirculation, where a portion of the gases leaving the furnace are recirculated back to the furnace for temperature control.
In modern steam generating plants, it is found that as the load requirements decrease, the steam temperature also decreases, and this is not desirable. To obtain greatest turbine efliciency, the steam should be kept at a constant temperature, regardless of the load requirements. One of the methods of maintaining constant steam temperature is by gas recirculation. As the load decreases, more combustion gas is recirculated back to the furnace. This prevents to a large extent the amount of heat that passes from the combustion gases within the furnace by radiation to the tubes lining the furnace walls, and hence leaves a greater amount of heat in the gases leaving the furnace outlet to be absorbed by the convection heat exchange members, such as the superheater and reheater. Also, a greater volume of gas leaves the furnace when recirculated gas is introduced into the furnace. In this manner, the steam temperature is maintained substantially constant, regardless of load changes.
This invention is particularly directed to the construction and position of the gas recirculation duct extending between the gas pass downstream of the heat exchange means and the furnace, and especially in a coal fired furnace. In a coal fire furnace, the hot combustion gases leaving the furnace contain a large amount of dust, fly ash and other foreign particles. In present steam generating units, dust collectors are usually installed in the recirculating gas ducts, on coal fired units, upstream of the fan to remove the dust and ash therefrom. If it is not removed, serious problems can result due to the large amount of such ash and dust being reintroduced into the furnace along with the recirculated gas.
In accordance with this invention, a portion of the recirculated gas duct is contained within the gas pass, and the openings thereto are on the underside, such that the gases entering must pass through a 180 turn. By such construction, a large portion of the fly ash, dust, and other foreign particles are prevented from entering the recirculated gas duct. This also gives protection to the fan in the recirculated gas duct, the abrasive action of the fly ash and dust on the fan being very damaging and costly.
Other advantages are that the duct within the gas pass need not be insulated. The temperature of the gases in the gas pass dovtmstream of the heat exchange members is approximately 700 F., and normally the entire gas recirculation duct must be insulated. Also, positioning a portion of the duct within the gas pass results in a substantial saving of space. In large modern boilers this is of significance. Another advantage is that only one opening through the wall of the gas pass must be sealed, this being the opening through which the recirculated gas duct extends. In ordinary unit-s utilizing gas recirculation, two or more openings are usually provided for attachment of gas recirculation ducts, which connections must be suitably sealed. The above listed advantages apply not only to a coal fired furnace, but apply equally well to any furnace, regardless of the type of fuel being burned.
Additional objects and advantages of the invention will appear from the following description of a preferred embodirnent thereof when considered in conjunction with the accompanying drawings wherein:
FIGURE 1 is a sectional side elevation of a furnace employing gas recirculation;
FIGURE 2 is a view of the furnace taken along lines 22 of FIGURE 1.
Referring to FIGURE 1 of the drawings, 1d designates a horizontal cyclone fired furnace utilizing pulverized coal as a fuel. The walls of the furnace are lined with tubes 12, which absorb heat radiantly from the furnace gases to produce steam. These tubes 12 are supplied with water from lower headers 13. Pulverized coal along with air is introduced into the furnace through horizontal cyclone burners 14, the air being supplied by duct 16. This air is heated in air preheater 18 prior to introduction into the furnace. The furnace 10 contains a hopper bottom 20, the walls of which are also lined with tubes 12. Below the furnace is an ash compartment 22, into which the ash from the furnace is allowed to fall.
The hot combustion gases within the furnace rise upwardly past the narrow portion of the furnace formed by arch 24, then flow through a horizontal pass (shown schematically) and flow downwardly through vertical gas pass 26. Gas pass .26 contains convectionsteam heating means 28, such as a superheater and reheater, where a substantial portion of the heat of the hot combustion gases is withdrawn therefrom. The gases continue on past economizer 3i where more of the heat is utilized, and then flows on to air preheater 18 by means of duct 32.
A portion of the gases are withdrawn from gas pass 26 and are recirculated back to the furnace as the need arises. For this purpose a duct 34 extends into gas pass 26, and contains openings 31, 35, and 36 on the underside thereof by means of which the gases are allowed to enter the duct. The duct 34 is connected to duct 33 outside of the gas pass 26, which duct 33 passes recirculated gas to fan 39 by means of ducts 38. Manifold or duct 41 receives the discharge of fan 39. Extending transversely from manifold 41 are a plurality of ducts 42, which are connected to openings 44 in the bottom or throat of hopper 20. The tubes .12 are staggered, as shown at 46 in FIGURE 1, to allow entrance of the recirculated gas therebe-tween.
Duct 33 contains damper 37, by means of which the amount of recirculated gas passing back to the furnace can be regulated. This damper can be adjusted manually or automatically, as is well known in the art, to increase the amount of gas recirculation as the load requirements decrease, to thereby maintain a constant steam temperature.
As illustrated in FIGURE 2, the openings 31, 35, and 36 are substantially evenly spaced across the entire width of gas pass 26. Also, duct 34 is centrally located within the gas pass 26. This prevents an imbalance of gas flow through the heat exchange means 28 and 30 directly above duct 34, due to the suction created by fan 39 at openings 31, 35, and 36. Since the suction effect will be greatest near the left end, the openings can be made progressively larger, openings 36 being the largest. Duct 34 is supported directly beneath economizer 30 by means of I-bearns 48, which can also be used to support the economizer. A circular or sloping contour at the top of duct 33 presents a streamlined surface, thereby insuring a minimum resistance to gas flow, and thus very little draft loss, as well as achieving a self-cleaning surface.
From the foregoing it can be seen that any gases to be recirculated back to the furnace must pass through a turn to enter openings 31, 35, and 36 in duct 34. Due to the velocity of the flow through gas pass 26, and the force of gravity, very little fly ash, dust, or other foreign particles will be drawn into openings 31, 35, and as :by the suction created by operation of fan 39. The sloping or circular top edge of duct 33 will tend to force the fly ash and dust impinging thereon away from the duct, thus preventing it from entering openings 31, 35, and 36. In summarizing, it can be seen that fly ash carryover to the gas recirculation system is reduced simply and efiiciently, resulting in reduction of fan maintenance costs and reduction of reintroduction of such fly ash into the furnace. Also, the unit is compact and economical, there being no need for insulation of the duct within the gas pass.
While the preferred embodiment of the invention has been shown and described, it will be understood that such is merely illustrative and not restrictive.
What we claim is:
1. A steam generating unit comprising a furnace, fuel and air inlets for said furnace, an outlet leading from the upper portion of said furnace through which the hot combustion gases pass, vertical wall means forming a gas pass containing heat exchange means, said gas pass being connected to said furnace outlet such that the gases pass downwardly therethrough, a duct in communication at one end with the gas pass downstream of said heat exchange means, and in communication at its other end with said furnace, a fan in said duct, a portion of said duct contained within said gas pass, said portion of said duct extending across the center portion of the gas pass, a plurality of openings in said duct being evenly spaced across the width of the gas pass through which gases are allowed to flow from the gas pass into said duct, said openings being positioned on the underside of said duct, such that the gases flowing in the gas pass must make a 180 turn to enter said openings, said openings progressively decreasing in size, the smallest opening being located the closest to the fan, so there is no imbalance of flow of gases through the portion of the gas pass containing said heat exchange means due to the suction effect of said fan. i
2. In a steam generating unit, a furnace, fuel and air inlets for said furnace, an outlet leading from said furnace through which the hot combustion gases pass, Wall means forming a gas pass containing heat exchange means, said gas pass being connected to said furnace outlet, a duct in communication at one end with the gas pass downstream of said heat exchange means, and in communication at its other end with said furnace, a fan in said duct, a portion of said duct contained within the gas pass, said portion of said duct extending across the center portion of the gas pass, a plurality of openings in said duct through which gases are allowed to flow from the gas pass into said duct, said openings being positioned such that the gases flowing in the gas pass must make a 180 turn to enter such openings, thereby preventing ash or other foreign particles carried by said gases from entering the duct, said openings progressively decreasing in size, the smallest opening being located the closest to the fan, so there is no imbalance of flow of gases through the portion of the gas pass containing said heat exchange means due to the suction effect of said fan.
References Cited in the file of this patent FOREIGN PATENTS 744,797 Great Britain Feb. 15, 1956

Claims (1)

1. A STEAM GENERATING UNIT COMPRISING A FURNACE, FUEL AND AIR INLETS FOR SAID FURNACE, AN OUTLET LEADING FROM THE UPPER PORTION OF SAID FURNACE THROUGH WHICH THE HOT COMBUSTION GASES PASS, VERTICALL WALL MEANS FORMING A GAS PASS CONTAINING HEAT EXCHANGE MEANS, SAID GAS PASS BEING CONNECTED TO SAID FURNACE OUTLET SUCH THAT THE GASES PASS DOWNWARDLY THERETHROUGH, A DUCT IN COMMUNICATION AT ONE END WITH THE GAS PASS DOWNSTREAM OF SAID HEAT EXCHANGE MEANS, AND IN COMMUNICTION AT ITS OTHER END WITH SAID FURNACE, A FAN IN SAID DUCT, A PORTION OF SAID DUCT CONTAINED WITHIN SAID GAS PASS, SAID PORTION OF SAID DUCT EXTENDING ACROSS THE CENTER PORTION OF THE GAS PASS, A PLURALITY OF OPENINGS IN SAID DUCT BEING EVENLY SPACED ACROSS THE WIDTH OF THE GAS PASS THROUGH WHICH GASES ARE ALLOWED TO FLOW FROM THE GAS PASS INTO SAID DUCT, SAID OPENINGS BEING POSITIONED ON THE UNDERSIDE OF SAID DUCT, SUCH THAT THE GASES FLOWING IN THE GAS PASS MUST MAKE A 180* TURN TO ENTER SAID OPENINGS, SAID OPENINGS PROGRESSIVELY DECREASING IN SIZE, THE SMALLEST OPENING BEING LOCATED THE CLOSEST TO THE FAN, SO THERE IS NO IMBALANCE OF FLOW OF GASES THROUGH THE PORTION OF THE GAS PASS CONTAINING SAID HEAT EXCHANGE MEANS DUE TO THE SUCTION EFFECT OF SAID FAN.
US79356A 1960-12-29 1960-12-29 Gas recirculation duct Expired - Lifetime US3090332A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US79356A US3090332A (en) 1960-12-29 1960-12-29 Gas recirculation duct

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US79356A US3090332A (en) 1960-12-29 1960-12-29 Gas recirculation duct

Publications (1)

Publication Number Publication Date
US3090332A true US3090332A (en) 1963-05-21

Family

ID=22150013

Family Applications (1)

Application Number Title Priority Date Filing Date
US79356A Expired - Lifetime US3090332A (en) 1960-12-29 1960-12-29 Gas recirculation duct

Country Status (1)

Country Link
US (1) US3090332A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3310036A (en) * 1965-09-28 1967-03-21 Babcock & Wilcox Co Gas off-take system
US3425602A (en) * 1967-02-21 1969-02-04 Julius C Tucci One-piece seed dispensing carton
EP0547540A1 (en) * 1991-12-18 1993-06-23 STEIN INDUSTRIE Société Anonyme dite: Boiler with flue gas recycling circuit
US20040025437A1 (en) * 2001-01-09 2004-02-12 Williams Paul Douglas Ash handling and treatment in solid fuel burners
US20190145635A1 (en) * 2017-11-14 2019-05-16 Regal Beloit America, Inc. Air handling system and method for assembling the same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB744797A (en) * 1953-09-30 1956-02-15 Friedrich Beuthner Improvements in forced flow, once-through tubulous vapour generating and vapour heating units and to a method of operation thereof

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB744797A (en) * 1953-09-30 1956-02-15 Friedrich Beuthner Improvements in forced flow, once-through tubulous vapour generating and vapour heating units and to a method of operation thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3310036A (en) * 1965-09-28 1967-03-21 Babcock & Wilcox Co Gas off-take system
US3425602A (en) * 1967-02-21 1969-02-04 Julius C Tucci One-piece seed dispensing carton
EP0547540A1 (en) * 1991-12-18 1993-06-23 STEIN INDUSTRIE Société Anonyme dite: Boiler with flue gas recycling circuit
FR2685446A1 (en) * 1991-12-18 1993-06-25 Stein Industrie BOILER WITH SMOKE RECYCLING CIRCUIT.
US5375538A (en) * 1991-12-18 1994-12-27 Stein Industrie Boiler having a flue gas recycling circuit
US20040025437A1 (en) * 2001-01-09 2004-02-12 Williams Paul Douglas Ash handling and treatment in solid fuel burners
US7678164B2 (en) * 2001-01-09 2010-03-16 Salinas Energy Limited Ash handling and treatment in solid fuel burners
US20190145635A1 (en) * 2017-11-14 2019-05-16 Regal Beloit America, Inc. Air handling system and method for assembling the same

Similar Documents

Publication Publication Date Title
US3224419A (en) Vapor generator with tangential firing arrangement
CN103175199B (en) Low-load burner capable of achieving boiler flue heat recycling for boiler
CN103776020A (en) Double reheat power station boiler with three rear flues and double rear baffles and capable of recycling jet flow flue gas
US2243909A (en) Means for controlling superheat
US4286548A (en) Gas recirculation apparatus with integral ash hoppers
US3090332A (en) Gas recirculation duct
US2737930A (en) Vapor generating and superheating method and apparatus
AU604603B2 (en) Steam generator with combustion of brown coal with different compositions of ash
US3194214A (en) Air heater having by-pass to prevent cold-end corrosion
US1734669A (en) Pulverized-fuel-burning furnace
CN205119100U (en) Owner, reheat steam temperature and exhaust gas temperature adjustable boiler afterbody flue structure
US3155079A (en) Supercritical vapor generator power plant system
US2817498A (en) Air heater
US2677437A (en) Heating system and low draft loss dust collector for use therein
US1966054A (en) Method of combustion
US2114619A (en) Apparatus for burning bagasse and like fuels
CN109084319A (en) The flue gas recirculation system to be exchanged heat using two-stage
US2973750A (en) Steam generator
WO2013020254A1 (en) Environmentally friendly energy-saving boiler of circulating fluidized bed type with organic thermal carrier
CN208967826U (en) The flue gas recirculation system to be exchanged heat using two-stage
US2905155A (en) Gas recirculation method for controlling superheat in a slag tap vapor generating and superheating unit and apparatus therefor
US3274961A (en) System for heating air and drying fuel
US2841102A (en) Heat exchanger
US1828483A (en) Art of steam generation
US3171390A (en) Steam generating unit