US3060903A - Vapor generator - Google Patents

Vapor generator Download PDF

Info

Publication number
US3060903A
US3060903A US4491A US449160A US3060903A US 3060903 A US3060903 A US 3060903A US 4491 A US4491 A US 4491A US 449160 A US449160 A US 449160A US 3060903 A US3060903 A US 3060903A
Authority
US
United States
Prior art keywords
duct
furnace
wall
tubes
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
US4491A
Inventor
Alexander H Rudd
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.)
Babcock and Wilcox Co
Original Assignee
Babcock and Wilcox Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Babcock and Wilcox Co filed Critical Babcock and Wilcox Co
Priority to US4491A priority Critical patent/US3060903A/en
Priority to GB2401/61A priority patent/GB956474A/en
Application granted granted Critical
Publication of US3060903A publication Critical patent/US3060903A/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
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B21/00Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically
    • F22B21/34Water-tube boilers of vertical or steeply-inclined type, i.e. the water-tube sets being arranged vertically or substantially vertically built-up from water tubes grouped in panel form surrounding the combustion chamber, i.e. radiation boilers
    • F22B21/341Vertical radiation boilers with combustion in the lower part
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B35/00Control systems for steam boilers
    • F22B35/002Control by recirculating flue gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/10Water tubes; Accessories therefor
    • F22B37/14Supply mains, e.g. rising mains, down-comers, in connection with water tubes
    • F22B37/147Tube arrangements for cooling orifices, doors and burners
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T24/00Buckles, buttons, clasps, etc.
    • Y10T24/14Bale and package ties, hose clamps
    • Y10T24/1457Metal bands
    • Y10T24/1459Separate connections
    • Y10T24/1461One piece
    • Y10T24/1463Sheet metal
    • Y10T24/1469End-to-end integral with band connecting means

Definitions

  • This invention relates to the art of vapor generation and vapor heating, and is more particularly directed to an improvement to that class of vapor generating and heating unit in which additional heating gases are introduced directly into the furnace or radiant heat absorption chamber thereof.
  • control of the gas temperature, the gas mass flow through the unit, and the resultant vapor temperatures are effected by a recirculating gas system that withdraws partially cooled combustion gases from a position downstream, gasfiowwise, of the vapor heating section and effects the entry of the recirculated gases into the furnace chamber where it com-mingles with the gaseous combustion products.
  • recirculated gases are directed to a duct which extends transversely along a tubular wall portion of a fluid cooled furnace chamber, the recirculated gases being discharged from the duct directly into the furnace chamber through port openings formed by the displacement of alternate or spaced tubes forming the furnace wall in the vicinity of the duct.
  • the recirculated gases thus introduced into the furnace have the effect of controlling slagging and/or maintaining a predetermined steam temperature. This is attained in part by the recirculated gases effecting either a reduction in the heat transfer to the heat absorption surfaces of the furnace wall tubes or a reduction in the gas temperature leaving the furnace chamber, and in part by effecting an increase in the gas mass flow over the convection heating surfaces of the unit.
  • An object of this invention is to overcome the abovementioned difficulties by providing a duct arrangement operatively associated with a wall portion of the radiant 336,903 Patented cf. 30, 1962 ice furnace chamber, wherein the ports through which the recirculated gases are introduced into the furnace are defined by portions of the furnace wall tubes arranged to effect a highly efficient shield in the vicinity of the port opening to protect the interior of the duct from the destructive radiant heating effects emanating from the adjacent furnace chamber.
  • Another object of this invention is to provide a gas recirculating system with novel discharge gas port construction, arranged and constructed in a manner to minimize the tendency for slag to accumulate and seal the port opening, particularly during operation of the unit when little or no recirculated gases are flowing therethrough.
  • Another object of this invention is to provide a port construction having a relatively low resistance to gas flow therethrough.
  • a recirculating gas system which includes a duct that extends transversely along a Wall portion of the unit setting so that an upright portion of the generating tubes defining the wall portion of the setting or furnace chamber forms a wall portion of the duct through which the recirculated gases are directed to the furnace.
  • a plurality of tubes which define the common wall between the duct and adjacent radiation chamber are bent outwardly of the setting and into the duct to define openings at spaced intervals along the Width of the Wall through which the recirculated gases are discharged directly from the duct into the furnace.
  • the adjacent outwardly bent tubes are progressively displaced laterally so as to fan outwardly on either side of the center line of the port to form a radiation shield spaced inwardly of the duct.
  • the portions of the tubes so displaced form a fluid cooled radiation shield to protect the interior of the duct from the deleterious effects of direct radiation emanating from the adjacent furnace chamber.
  • Bafile means are disposed between adjacent laterally displaced tube portions of the radiation shield to close spaces existing therebetween so that a substantially imperforate shield is formed encompassing the area of the port opening.
  • a feature of this invention resides in the provision that the amount of insulation required on the interior of the duct discharging the recirculated gases into the furnace may be substantially reduced, thereby decreasing the initial capital outlay, and also greatly reducing the amount of future maintenance which would otherwise be required to maintain the duct in proper operating condition.
  • FIG. 1 is a vertical sectional view of a vapor generating and heating unit embodying the invention.
  • FIG. 2 is a plan section taken along line 2-2 of FIG. 1.
  • FIG. 3 is a sectional view taken along line 33 of FIG. 2.
  • the unit comprises a setting 11 which includes a vertically elongated furnace 12, a laterally extending gas pass 13 connected adjacent the upper end of the furnace, and a downwardly extending convection heating section 14 serially connected with the gas pass 13.
  • the furnace 12 is defined by upright front, rear and side walls 15, 16 and 17, respectively.
  • the front wall includes a row of steam generating tubes 13 which extend upwardly from a lower water supply drum 1?.
  • tubes 18 first extend along the bottom 18A of the furnace thence upwardly along the front wall of the furnace.
  • a portion 18B of the front wall tubes 18 defines the throat portion of the cyclone furnaces 20 which generate the gaseous products of combustion that are discharged into the furnace 12.
  • the front wall 15 at an intermediate portion 15A of the furnace immediately above the cyclone furnace level is inclined outwardly and upwardly to define with the adjacent side and rear walls an intermediate or transition radiant furnace chamber 12A. Beyond this transition section, the front wall tubes 18 extend upwardly and connect with the steam and water separating drum 21 of the unit.
  • the rear wall 16 includes a row of steam generating tubes 22 which extend upwardly from the supply drum 19 to an upper rear wall header 23, the latter in turn being connected by suitable connectors 24 to the steam drum 21.
  • the opposed side walls 17 of the furnace each include a row of generating tubes 2'7 extending between their respective lower and upper side wall headers 28 and 29, respectively.
  • Each of the side wall headers 28, 29 in turn is connected into the circulation system of the unit by suitable conduits '30, 31 connecting to the supply drum 19 and main steam drum 21, respectively.
  • Portions 27A of the side wall tubes 27 adjacent the upper end of the setting are laterally displaced to define the side walls of the lateral 'gas pass 13.
  • the tubular Walls 18, 22 and 27, thus define a vertically elongated furnace 12 which has a relatively small lower or primary radiation chamber 128 which forms a chamber common to each of the cyclone furnaces 20.
  • the lower segments of the tubular walls defining chamber 12B are preferably covered with suitable high heat resistant refractory material 12D.
  • the lower chamber 12B is open at its upper end and is connected by the transition chamber 12A, formed by the upwardly diverging portion 15A of the front wall 15 to an upper superposed secondary radiation chamber 12C.
  • a plurality of cyclone furnaces 20 of the general construction as disclosed in US. Patent No. 2,357,301 generate the gaseous products of combustion which flow upwardly through the furnace 12. While cyclone furnaces 20 are herein illustrated as the means employed for generating the gases of combustion, it is to be understood that other burner means may be equally suitable for firing the unit in accordance with this invention.
  • the cyclone furnaces 20 are arranged in superposed position and are adapted to be independently fired by relatively low quality, high ash content, coarsely pulverized or granulated coal.
  • Each of the cyclone furnaces 20 is arranged to separately discharge the hot products of combustion and molten slag directly into the lower chamber portions 12B, wherein the gases of the several cyclones are thoroughly mixed.
  • Each of the cyclones 20 is substantially circular in cross-section, and the barrel portion 20A thereof is defined by steam generating tubes which together with the front wall tubes 18, rear wall tubes 22 and side wall tubes 27 constitute the steam generating circuits of the unit.
  • the generating unit shown is of the natural circulation type with feedwater being supplied to the upper drum 21.
  • Downcomers 30A connect the steam and water drum 21 to the lower water supply drum 19 which feeds the individual steam generating circuits.
  • the steam generated in each of the wall circuits during operation of the unit is delivered to the steam drum 21 and is separated therein. Saturated steam from the steam drum 21 is then superheated by flowing through suitable steam heating surfaces which are disposed in heat transfer relationship to the heating gases flowing through the unit.
  • the walls 31, 32 and opposed connecting side Walls 33 defining the convection section or bird cage" 14 are lined with steam cooling tubes.
  • Saturated steam is delivered from the steam drum 21 through steam conduits 34 to a collecting header 35. From the collecting header 35, the steam flows through a row of furnace roof tubes 36 to a distributing header 37.
  • the distributing header 37 in turn supplies steam to each of the tubular wall circuits defining the walls 31 and 32, and by connectors 37A to side walls 33 of the convection gas pass 14, the circuits terminating in a ring header 38 positioned in the lower portion of the chamber 14. From the ring header 33 the steam flows serially through a primary superheater 39.
  • the primary superheater 39 comprises a plurality of platen elements, each platen element being formed of multiple looped return bend tubes. Each of the primary superheater platens discharges into the outlet header 40.
  • the steam flows serially through suitable conduit means 41 to the inlet header 42 of a secondary superheater 43 wherein the steam is finally superheated.
  • the secondary superheater 43 comprises a plurality of transversely spaced platen elements formed of vertically depending tubes disposed adjacent the furnace outlet 25.
  • the steam flowing therethrough is discharged to an outlet header 44 from whence the finally superheated steam is delivered to a point of use through conduit 45.
  • An economizer 46 for preheating the feedwater supplied to the drum is located in the downfiow pass 14 beyond the superheater 39.
  • the gas flow is generally upwardly through the furnace chamber 12, thence laterally through the lateral gas pass 13 and thence downwardly through the convection heating section or downfiow pass 14 from whence the gases are directed through an air heater 47 to a suitable gas outlet or flue 48.
  • a steam reheater 70 comprising spaced platens of return bend tubes may be disposed in the gas pass 13.
  • the gas recirculation system for introducing additional heating gases into the furnace 12 comprises a duct 49 for withdrawing a portion of the flue gases after they pass through the convection heating section 14.
  • the outlet end of duct 49 connects with a fan or blower 50 which discharges the recirculating gases through an outlet duct 51 to a manifold or distributing duct 52.
  • duct 52 extends transversely along the furnace rear wall tube row 22.
  • the manifold duct 52 comprises a sheet metal casing which defines the top 53, rear 54 and bottom 55 of the duct.
  • the front face of duct 52 is defined by that portion of water cooled tubes 22 of the furnace wall which are adjacent the duct.
  • the duct 52 extends transversely of the furnace at a position above the refractory lined portion of the lower furnace chamber 12B and is located adjacent the rear wall opposite the inclined wall portion 15A of the front wall.
  • FIGS. 2 and 3 a plurality of adjacent upright tube portions 22A and 22H of the rear wall tubes 22, in the vicinity of duct 52 and located at spaced intervals along the length of duct 55, are bent out of the plane of the Wall to define port openings 56.
  • the recirculated gases are thus discharged through port openings 56 directly from the duct 52 into the furnace 12 to mix with the combustion gases flow-ing upwardly therethrough.
  • tubes 22A to 22H are bent outward of the furnace and inwardly within the duct 52.
  • Tube groups 22A to 22D, and 22B to 22H, respectively, are grouped on either side of the center line of port 55, the tubes of each group being laterally displaced to fan outwardly from the port center line a progressively increasing amount to a point beyond the port opening 56 to more eifectively shield the inside of the duct from radiation.
  • the outermost or end tubes 22A and 221-1 which define the extreme limits of the openings 55, are spaced rearwardly of the plane of the rear wall tubes 22 and to one side of the port opening to define the entrance to passageways 56A, 56B which lead to port opening 56.
  • the passageways 56A, 56B and opening 56 are sufiiciently large so as not to be easily closed or clogged by slag accumulations, even under the most adverse operating conditions, as for example during operation when little or no gas is being recirculated through duct 52. Also the arrangement facilitates sizing of the port openings 56 so that a relatively low gas flow pressure drop therethrough is maintained. This feature is important where large quantities of recirculated gas are required.
  • baflle means 59 which substantially closes spaces 58.
  • these baffle means 59 are formed by closely spaced fiat studs 60 welded to opposed surfaces of the tube as shown.
  • the irregular portions of spaces 58 formed where the tubes are bending back into the plane of the wall may be closed by appropriately shaped plates and/ or suitable refractory.
  • the tubes 22A to 22H and studs 60, defining the port construction 56 described provide a highly elfective shield or bafile means disposed inwardly of the duct to protect the inner surfaces of the duct 52 from the harmful effects of direct radiation caused by the combustion of fuel in the adjacent furnace chamber 12. For this reason the amount and/ or quality of insulating material heretofore required to protect the interior of the ducts, can be substantially reduced.
  • the curvature of the baflie wall or shield formed by the progressively displaced portion of tubes 22A to 22H, as shown in FIG. 2 streamlines the flow of gases through the port, particularly since they approach each other as indicated by the arrows, and thus minimizes the impact and promotes controlled introduction of the gases into the furnace.
  • the pressure drop through the port 56 tends to be minimized.
  • a retractable soot blower 61 may be located within each port 56, as shown, the arrangement being such that when it is not in operation it is retracted within duct 52 to protect it from furnace radiation.
  • ports 56 of duct 52 are illustrated adjacent the rear wall 22 of the transition section 12A, it will be understood that location of the duct 52 and its port openings 56 to attain the desired gas temperature and/or mass flow of any particular operating unit.

Description

Oct. 30, 1962 A. H. RUDD VAPOR GENERATOR Filed Jan. 25, 1960 2 Sheets-Sheet 1 GAS OUTLET N AIR INLET W ATTORNEY tees This invention relates to the art of vapor generation and vapor heating, and is more particularly directed to an improvement to that class of vapor generating and heating unit in which additional heating gases are introduced directly into the furnace or radiant heat absorption chamber thereof.
In the design of many of the larger high temperature and high pressure vapor generating and heating units control of the gas temperature, the gas mass flow through the unit, and the resultant vapor temperatures are effected by a recirculating gas system that withdraws partially cooled combustion gases from a position downstream, gasfiowwise, of the vapor heating section and effects the entry of the recirculated gases into the furnace chamber where it com-mingles with the gaseous combustion products.
In such units, recirculated gases are directed to a duct which extends transversely along a tubular wall portion of a fluid cooled furnace chamber, the recirculated gases being discharged from the duct directly into the furnace chamber through port openings formed by the displacement of alternate or spaced tubes forming the furnace wall in the vicinity of the duct. The recirculated gases thus introduced into the furnace have the effect of controlling slagging and/or maintaining a predetermined steam temperature. This is attained in part by the recirculated gases effecting either a reduction in the heat transfer to the heat absorption surfaces of the furnace wall tubes or a reduction in the gas temperature leaving the furnace chamber, and in part by effecting an increase in the gas mass flow over the convection heating surfaces of the unit.
Inasmuch as the recirculated gases are oftentimes introduced through port openings located in the high temperature zone of a furnace, experience has indicated the necessity for protecting the inside surfaces of the gas recirculating duct in the vicinity of the furnace walls from the high temperature radiant emission of the furnace gases radiating through the port openings. Heretofore, high temperature insulation, secured by pin studs, was used on the inside of the duct to withstand the deleterious effects of the direct radiation emanating from the adjacent furnace chamber. The use of such insulation increased the initial capital expenditure for such duct work in addition to creating a condition which required continuing maintenance.
In furnaces fired by slag forming fuels, a further difficulty was encountered in that gas discharge ports of the known constructions, had a tendency to become slagged over and thus rendered inoperative. This condition was particularly aggravated at ratings on the unit, when little, or no, recirculated gases are introduced into the furnace to discourage the accumulation of slag across the port opening.
An object of this invention is to overcome the abovementioned difficulties by providing a duct arrangement operatively associated with a wall portion of the radiant 336,903 Patented cf. 30, 1962 ice furnace chamber, wherein the ports through which the recirculated gases are introduced into the furnace are defined by portions of the furnace wall tubes arranged to effect a highly efficient shield in the vicinity of the port opening to protect the interior of the duct from the destructive radiant heating effects emanating from the adjacent furnace chamber.
Another object of this invention is to provide a gas recirculating system with novel discharge gas port construction, arranged and constructed in a manner to minimize the tendency for slag to accumulate and seal the port opening, particularly during operation of the unit when little or no recirculated gases are flowing therethrough.
Another object of this invention is to provide a port construction having a relatively low resistance to gas flow therethrough.
The above objects and other features are attained by a recirculating gas system which includes a duct that extends transversely along a Wall portion of the unit setting so that an upright portion of the generating tubes defining the wall portion of the setting or furnace chamber forms a wall portion of the duct through which the recirculated gases are directed to the furnace. According to this invention, a plurality of tubes which define the common wall between the duct and adjacent radiation chamber are bent outwardly of the setting and into the duct to define openings at spaced intervals along the Width of the Wall through which the recirculated gases are discharged directly from the duct into the furnace. The adjacent outwardly bent tubes are progressively displaced laterally so as to fan outwardly on either side of the center line of the port to form a radiation shield spaced inwardly of the duct. The portions of the tubes so displaced form a fluid cooled radiation shield to protect the interior of the duct from the deleterious effects of direct radiation emanating from the adjacent furnace chamber. Bafile means are disposed between adjacent laterally displaced tube portions of the radiation shield to close spaces existing therebetween so that a substantially imperforate shield is formed encompassing the area of the port opening.
A feature of this invention resides in the provision that the amount of insulation required on the interior of the duct discharging the recirculated gases into the furnace may be substantially reduced, thereby decreasing the initial capital outlay, and also greatly reducing the amount of future maintenance which would otherwise be required to maintain the duct in proper operating condition.
The various features of novelty which characterize the invention are pointed out with particularity in the claims annexed to and forming a part of this specification. For a better understanding of the invention, its operating advantages and specific objects attained by its use, reference should be had to the accompanying drawings and descriptive matter in which is illustrated and described a preferred embodiment of the invention.
In the drawings:
FIG. 1 is a vertical sectional view of a vapor generating and heating unit embodying the invention.
FIG. 2 is a plan section taken along line 2-2 of FIG. 1.
FIG. 3 is a sectional view taken along line 33 of FIG. 2.
Referring to the drawings, the invention herein described is illustrated in conjunction with a high capacity, high pressure and high temperature natural circulation steam generating and heating unit 10. Generally, the unit comprises a setting 11 which includes a vertically elongated furnace 12, a laterally extending gas pass 13 connected adjacent the upper end of the furnace, and a downwardly extending convection heating section 14 serially connected with the gas pass 13.
The furnace 12 is defined by upright front, rear and side walls 15, 16 and 17, respectively. The front wall includes a row of steam generating tubes 13 which extend upwardly from a lower water supply drum 1?. As shown, tubes 18 first extend along the bottom 18A of the furnace thence upwardly along the front wall of the furnace. A portion 18B of the front wall tubes 18 defines the throat portion of the cyclone furnaces 20 which generate the gaseous products of combustion that are discharged into the furnace 12. The front wall 15 at an intermediate portion 15A of the furnace immediately above the cyclone furnace level is inclined outwardly and upwardly to define with the adjacent side and rear walls an intermediate or transition radiant furnace chamber 12A. Beyond this transition section, the front wall tubes 18 extend upwardly and connect with the steam and water separating drum 21 of the unit. The rear wall 16 includes a row of steam generating tubes 22 which extend upwardly from the supply drum 19 to an upper rear wall header 23, the latter in turn being connected by suitable connectors 24 to the steam drum 21. A portion of the rear wall tubes 22 immediately below the furnace outlet 25, which connects with the lateral gas pass 13, is inwardly bent to define a nose arch 2 6. The opposed side walls 17 of the furnace each include a row of generating tubes 2'7 extending between their respective lower and upper side wall headers 28 and 29, respectively. Each of the side wall headers 28, 29 in turn is connected into the circulation system of the unit by suitable conduits '30, 31 connecting to the supply drum 19 and main steam drum 21, respectively. Portions 27A of the side wall tubes 27 adjacent the upper end of the setting are laterally displaced to define the side walls of the lateral 'gas pass 13.
The tubular Walls 18, 22 and 27, thus define a vertically elongated furnace 12 which has a relatively small lower or primary radiation chamber 128 which forms a chamber common to each of the cyclone furnaces 20. The lower segments of the tubular walls defining chamber 12B are preferably covered with suitable high heat resistant refractory material 12D. The lower chamber 12B is open at its upper end and is connected by the transition chamber 12A, formed by the upwardly diverging portion 15A of the front wall 15 to an upper superposed secondary radiation chamber 12C.
A plurality of cyclone furnaces 20 of the general construction as disclosed in US. Patent No. 2,357,301 generate the gaseous products of combustion which flow upwardly through the furnace 12. While cyclone furnaces 20 are herein illustrated as the means employed for generating the gases of combustion, it is to be understood that other burner means may be equally suitable for firing the unit in accordance with this invention.
In the illustrated form, FIG. 1, the cyclone furnaces 20 are arranged in superposed position and are adapted to be independently fired by relatively low quality, high ash content, coarsely pulverized or granulated coal. Each of the cyclone furnaces 20 is arranged to separately discharge the hot products of combustion and molten slag directly into the lower chamber portions 12B, wherein the gases of the several cyclones are thoroughly mixed.
Each of the cyclones 20 is substantially circular in cross-section, and the barrel portion 20A thereof is defined by steam generating tubes which together with the front wall tubes 18, rear wall tubes 22 and side wall tubes 27 constitute the steam generating circuits of the unit. The generating unit shown is of the natural circulation type with feedwater being supplied to the upper drum 21. Downcomers 30A connect the steam and water drum 21 to the lower water supply drum 19 which feeds the individual steam generating circuits.
The steam generated in each of the wall circuits during operation of the unit is delivered to the steam drum 21 and is separated therein. Saturated steam from the steam drum 21 is then superheated by flowing through suitable steam heating surfaces which are disposed in heat transfer relationship to the heating gases flowing through the unit.
As shown, the walls 31, 32 and opposed connecting side Walls 33 defining the convection section or bird cage" 14 are lined with steam cooling tubes. Saturated steam is delivered from the steam drum 21 through steam conduits 34 to a collecting header 35. From the collecting header 35, the steam flows through a row of furnace roof tubes 36 to a distributing header 37.
The distributing header 37 in turn supplies steam to each of the tubular wall circuits defining the walls 31 and 32, and by connectors 37A to side walls 33 of the convection gas pass 14, the circuits terminating in a ring header 38 positioned in the lower portion of the chamber 14. From the ring header 33 the steam flows serially through a primary superheater 39. As shown, the primary superheater 39 comprises a plurality of platen elements, each platen element being formed of multiple looped return bend tubes. Each of the primary superheater platens discharges into the outlet header 40.
From the primary superheater outlet header 4!) the steam flows serially through suitable conduit means 41 to the inlet header 42 of a secondary superheater 43 wherein the steam is finally superheated.
The secondary superheater 43 comprises a plurality of transversely spaced platen elements formed of vertically depending tubes disposed adjacent the furnace outlet 25. The steam flowing therethrough is discharged to an outlet header 44 from whence the finally superheated steam is delivered to a point of use through conduit 45. An economizer 46 for preheating the feedwater supplied to the drum is located in the downfiow pass 14 beyond the superheater 39.
In accordance with this invention the gas flow is generally upwardly through the furnace chamber 12, thence laterally through the lateral gas pass 13 and thence downwardly through the convection heating section or downfiow pass 14 from whence the gases are directed through an air heater 47 to a suitable gas outlet or flue 48. If desired a steam reheater 70 comprising spaced platens of return bend tubes may be disposed in the gas pass 13.
In order to control the gas temperatures and/or gas mass flow through the unit to maintain and control superheat temperatures, it has been customary to withdraw a port-ion of the gases downstream gasflow-wise of the primary superheater 39 and recycle the same through the furnace 12.
In accordance with this invention the gas recirculation system for introducing additional heating gases into the furnace 12 comprises a duct 49 for withdrawing a portion of the flue gases after they pass through the convection heating section 14. The outlet end of duct 49 connects with a fan or blower 50 which discharges the recirculating gases through an outlet duct 51 to a manifold or distributing duct 52. As shown, duct 52 extends transversely along the furnace rear wall tube row 22.
The manifold duct 52 comprises a sheet metal casing which defines the top 53, rear 54 and bottom 55 of the duct. The front face of duct 52 is defined by that portion of water cooled tubes 22 of the furnace wall which are adjacent the duct.
As shown in FIGS. 1 and 2, the duct 52 extends transversely of the furnace at a position above the refractory lined portion of the lower furnace chamber 12B and is located adjacent the rear wall opposite the inclined wall portion 15A of the front wall. The rear wall tubes 22, in
the plane of the wall, are disposed in substantially tangent relationship as shown in FIGS. 2 and 3. In accordance with this invent-ion, and as shown in FIGS. 2 and 3, a plurality of adjacent upright tube portions 22A and 22H of the rear wall tubes 22, in the vicinity of duct 52 and located at spaced intervals along the length of duct 55, are bent out of the plane of the Wall to define port openings 56. The recirculated gases are thus discharged through port openings 56 directly from the duct 52 into the furnace 12 to mix with the combustion gases flow-ing upwardly therethrough.
As shown in FIGS. 2 and 3, portions of tubes 22A to 22H are bent outward of the furnace and inwardly within the duct 52. Tube groups 22A to 22D, and 22B to 22H, respectively, are grouped on either side of the center line of port 55, the tubes of each group being laterally displaced to fan outwardly from the port center line a progressively increasing amount to a point beyond the port opening 56 to more eifectively shield the inside of the duct from radiation. In this manner the outermost or end tubes 22A and 221-1, which define the extreme limits of the openings 55, are spaced rearwardly of the plane of the rear wall tubes 22 and to one side of the port opening to define the entrance to passageways 56A, 56B which lead to port opening 56. The passageways 56A, 56B and opening 56 are sufiiciently large so as not to be easily closed or clogged by slag accumulations, even under the most adverse operating conditions, as for example during operation when little or no gas is being recirculated through duct 52. Also the arrangement facilitates sizing of the port openings 56 so that a relatively low gas flow pressure drop therethrough is maintained. This feature is important where large quantities of recirculated gas are required.
In the spaces 58 formed by the lateral displacement of tubes 22A to 22H, there is disposed a baflle means 59 which substantially closes spaces 58. In the illustrated embodiment these baffle means 59 are formed by closely spaced fiat studs 60 welded to opposed surfaces of the tube as shown. The irregular portions of spaces 58 formed where the tubes are bending back into the plane of the wall may be closed by appropriately shaped plates and/ or suitable refractory.
With this arrangement, the tubes 22A to 22H and studs 60, defining the port construction 56 described, provide a highly elfective shield or bafile means disposed inwardly of the duct to protect the inner surfaces of the duct 52 from the harmful effects of direct radiation caused by the combustion of fuel in the adjacent furnace chamber 12. For this reason the amount and/ or quality of insulating material heretofore required to protect the interior of the ducts, can be substantially reduced.
Further, the curvature of the baflie wall or shield formed by the progressively displaced portion of tubes 22A to 22H, as shown in FIG. 2, streamlines the flow of gases through the port, particularly since they approach each other as indicated by the arrows, and thus minimizes the impact and promotes controlled introduction of the gases into the furnace. Thus the pressure drop through the port 56 tends to be minimized.
If desirable a retractable soot blower 61 may be located within each port 56, as shown, the arrangement being such that when it is not in operation it is retracted within duct 52 to protect it from furnace radiation.
While the location of ports 56 of duct 52 are illustrated adjacent the rear wall 22 of the transition section 12A, it will be understood that location of the duct 52 and its port openings 56 to attain the desired gas temperature and/or mass flow of any particular operating unit.
While in accordance with the provisions of the statutes there is illustrated and described herein the best form and mode of operation of the invention now known to the inventor, those skilled in the art will understand that changes may be made in the form of the apparatus disclosed without departing from the spirit of the invention covered by the claims, and that certain features of the invention may sometimes be used to advantage without a corresponding use of other features.
What is claimed is:
1. A furnace chamber within which combustion gases are generated and bounded in part by a wall including upright fluid cooled tubes, means for introducing low temperature heating gases into said furnace chamber to mix with the gases of combustion generated therein, said means including a duct extending transversely of and connected to said wall with said wall forming a common wall between said duct and said furnace, a group of consecutive tubes of said common wall having intermediate portions offset outwardly a substantial distince into said duct to provide an opening in said common wall and bent laterally in said duct relative to the centerline of said opening, with the intermediate tube portions near to the center line of the opening being outwardly offset from the plane of said common wall a lesser distance than the remaining intermediate tube portions, means for substantially closing the intertube spaces of said intermediate tube portions so bent to form a shield for the protection of said duct from radiation from said furnace, said shield and common wall cooperating to define a passageway of decreasing vertical cross-sectional area in the direction of gas flow therethrough arranged to discharge low temperature gases from said duct to said opening.
2. A furnace chamber within which combustion gases are generated and bounded in part by a wall including upright fluid cooled tubes, means for introducing low temperature heating gases into said furnace chamber to mix with the gases of combustion generated therein, said means including a duct extending transversely of and connected to said wall with said wall forming a common wall between said duct and said furnace, a group of consecutive tubes of said common wall having intermediate portions offset outwardly a substantial distance into said duct to provide an opening in said common wall and bent laterally in said duct relative to the centerline of said opening, with the intermediate tube portions near to the centerline of the opening being outwardly offset from the plane of said common wall a lesser distance than the remaining intermediate tube portions and with the intermediate tube portions on opposite sides of the centerline of said opening being bent laterally in opposite directions away from said centerline, means for substantially closing the intertube spaces of said intermediate tube portions so bent to form a shield for the protection of said duct from radiation from said furnace, said shield and com mon wall cooperating to define a passageway of decreasing vertical cross-sectional area in the direction of gas flow therethrough arranged to discharge low temperature gases from said duct to said opening.
3. A furnace chamber within which combustion gases are generated and bounded in part by a wall including upright fluid cooled tubes, means for introducing low temperature heating gases into said furnace chamber to mix with the gases of combustion generated therein, said means including a duct extending transversely of and connected to said wall with said wall forming a common wall between said duct and said furnace, a group of consecutive tubes of said common wall having intermediate portions offset outwardly a substantial distance into said duct to provide an opening in said common wall and bent laterally in said duct relative to the centerline of said opening, with the intermediate tube portions near to the centerline of the opening being outwardly offset from the plane of said common wall a lesser distance than the remaining intermediate tube portions and with the intermediate tube portions on opposite sides of the centerline of said opening being bent laterally in opposite directions away from said centerline, means for substantially closing the intertube spaces of said intermediate tube portions so bent to form a shield for the protection of said duct 7 from radiation from said furnace, said shield and common Wall cooperating to define a pair of passageways of decreasing vertical cross-sectional area in the direction of gas flow theretbrough disposed on opposite sides of and leading to said opening and arranged to discharge low temperature gases from said duct to said opening.
References Cited in the file of this patent UNITED STATES PATENTS Van Brunt et a1. May 20, 1941 Cermak Dec. 22, 1942 Allen Apr. 29, 1958 Koch Oct. 21, 1958 FOREIGN PATENTS France May 26, 1954 France Oct. 26, 1955
US4491A 1960-01-25 1960-01-25 Vapor generator Expired - Lifetime US3060903A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US4491A US3060903A (en) 1960-01-25 1960-01-25 Vapor generator
GB2401/61A GB956474A (en) 1960-01-25 1961-01-20 Improvements in vapour generating and heating units

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US4491A US3060903A (en) 1960-01-25 1960-01-25 Vapor generator

Publications (1)

Publication Number Publication Date
US3060903A true US3060903A (en) 1962-10-30

Family

ID=21711057

Family Applications (1)

Application Number Title Priority Date Filing Date
US4491A Expired - Lifetime US3060903A (en) 1960-01-25 1960-01-25 Vapor generator

Country Status (2)

Country Link
US (1) US3060903A (en)
GB (1) GB956474A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5390631A (en) * 1994-05-25 1995-02-21 The Babcock & Wilcox Company Use of single-lead and multi-lead ribbed tubing for sliding pressure once-through boilers
US5791300A (en) * 1996-02-13 1998-08-11 The Babcock & Wilcox Company Steam generator parallel back end using pendant primary superheater and baffle wall with gas-tight header vestibule

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2242491A (en) * 1939-06-05 1941-05-20 Comb Eng Co Inc Slagging furnace
US2306156A (en) * 1939-02-22 1942-12-22 Cermak Josef Slag outflow openings for furnaces
FR1080188A (en) * 1954-12-07
FR1111328A (en) * 1953-09-25 1956-02-24 Babcock & Wilcox France Evaporation and superheating unit with gas recirculation
US2832321A (en) * 1955-03-24 1958-04-29 Babcock & Wilcox Co Cyclone furnace fired fluid heating unit
US2856907A (en) * 1955-11-30 1958-10-21 Babcock & Wilcox Co Steam generating, superheating and reheating unit with reheater ahead of the superheater

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1080188A (en) * 1954-12-07
US2306156A (en) * 1939-02-22 1942-12-22 Cermak Josef Slag outflow openings for furnaces
US2242491A (en) * 1939-06-05 1941-05-20 Comb Eng Co Inc Slagging furnace
FR1111328A (en) * 1953-09-25 1956-02-24 Babcock & Wilcox France Evaporation and superheating unit with gas recirculation
US2832321A (en) * 1955-03-24 1958-04-29 Babcock & Wilcox Co Cyclone furnace fired fluid heating unit
US2856907A (en) * 1955-11-30 1958-10-21 Babcock & Wilcox Co Steam generating, superheating and reheating unit with reheater ahead of the superheater

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5390631A (en) * 1994-05-25 1995-02-21 The Babcock & Wilcox Company Use of single-lead and multi-lead ribbed tubing for sliding pressure once-through boilers
US5791300A (en) * 1996-02-13 1998-08-11 The Babcock & Wilcox Company Steam generator parallel back end using pendant primary superheater and baffle wall with gas-tight header vestibule

Also Published As

Publication number Publication date
GB956474A (en) 1964-04-29

Similar Documents

Publication Publication Date Title
US3194214A (en) Air heater having by-pass to prevent cold-end corrosion
US2730080A (en) Vapor generating installation, including a cyclone furnace
US3125995A (en) forced flow vapor generating unit
US2114619A (en) Apparatus for burning bagasse and like fuels
US3060903A (en) Vapor generator
US3081748A (en) Forced flow fluid heating unit
US3174464A (en) Vapor generating apparatus
US2902982A (en) Forced circulation vapor generating units
US2798464A (en) Vapor generators having vapor heaters
US2989039A (en) Fluid heating unit with gas tempering provisions
US2498761A (en) Fuel burning apparatus
US1911501A (en) Steam generating apparatus and method
US3245385A (en) Forced flow vapor generating unit
US1992953A (en) Steam boiler
US2914040A (en) Vapor generator
US2186919A (en) Steam boiler
US2869518A (en) Radiant vapor generating and superheating unit with radiant superheater platens
US2242762A (en) Furnace
US2737160A (en) Steam generators employing radiant superheaters and reheaters
US3171390A (en) Steam generating unit
US2861526A (en) Fuel burning apparatus
US2980084A (en) System for burning low volatile fuels
US2800115A (en) Steam generating and superheating unit with recycled gas flow
US3153402A (en) Steam generator
US2299732A (en) Steam generator