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US1863541A - Steam boiler and process of firing it - Google Patents

Steam boiler and process of firing it Download PDF

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Publication number
US1863541A
US1863541A US239099A US23909927A US1863541A US 1863541 A US1863541 A US 1863541A US 239099 A US239099 A US 239099A US 23909927 A US23909927 A US 23909927A US 1863541 A US1863541 A US 1863541A
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US
United States
Prior art keywords
air
stoker
water
firing
conduit
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
US239099A
Inventor
Charles E Lucke
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 US239099A priority Critical patent/US1863541A/en
Application granted granted Critical
Publication of US1863541A publication Critical patent/US1863541A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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
    • F23L1/00Passages or apertures for delivering primary air for combustion 
    • F23L1/02Passages or apertures for delivering primary air for combustion  by discharging the air below the fire
    • 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
    • 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
    • F23L5/00Blast-producing apparatus before the fire
    • F23L5/04Blast-producing apparatus before the fire by induction of air for combustion, e.g. using steam jet
    • 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
    • F23L7/00Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
    • F23L7/002Supplying water
    • 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

  • Fig. 1 is a vertical section showing somewhat diagraminatically an illustrative embodiment of the invention
  • Fig. 2 is a section on an enlarged scale along the line 2-2 of Fig. 1
  • Fig. 3 is a section along the line 3 3 of Fig. 2
  • Fig. 4 is a vertical section, partly broken away, illustrating a modification.
  • reference character 1 indicates the furnace of a boiler that is provided with a. chain grate stoker 2.
  • the exit for waste gases is shown at 3 and leads to an air heater 4 from which a conduit 5 leads to the stack.
  • the cold air enters the air heater 4 at 6, and heated air passes out through a conduit 7 that is provided with a damper 8.
  • a humidifier lOor air is provided, and heat in the waste products of combustion air heater 4 is utilized for heating water to humidity the air in the humidiiier.
  • the humidifier is provided Wih a separator 11 to remove unvaporized drops of water from the sprays 12.
  • the heat for vaporization is derived from iiue gases, and in heat thewater to be sprayed into the air.
  • a sump 13 is provided in the lower portion of the humidifier,
  • a fan or blower 20 forces air into the humidiiier where it becomes saturated with moisture at an elevated temperature and this iixes the weight of water vapor carried.
  • the heated saturated air passes through the outlet 21 that is provided with a damper 22 and joins the hot air from the outlet 7, and the mixture passes through the conduit 23 into the spaces below the stoker 2.
  • Adjustment of relative position of dampers 8 and 22 determines the temperature of the air delivered to the stoker and also the amount of water vapor carried by that air. This adjustment also determines what part of the boiler wasteheat is utilized for raising the temperature of the air and what part for vaporizing water.
  • a plurality obranches 25, each provided with a valve 26, leads from the conduit 23 to thecompartments 28 of. the chain grate stoker.
  • the compartments 28 are provided in a ⁇ well known manner to divide the space under the chain grate Stoker into sections, and the amount of air admitted to each section can be regulated by means of the dampers 26.
  • air of one condition as to perature is admitted through the conduit 7 and passes through branches 25 that are provided with dampers 26', into some of the compartments 28 of the chain grate Stoker.
  • Air that contains more from a humidiiier is deliveredthrough the injector nozzle 33 and draws in air of less humidity from conduit 3l producing a mixture in conduit 34 of higher humidity for one of the stoker compartments than is supplied through conduit 7 to the others.
  • the air supplied to 7 and 33 may be the same as, for example, that from the air heater, or it may be dierent as to temperature and moisture. It may be supplied from another hu- In the modification shown in Fig.
  • the humidified air is indicated as being led to thekiirst compartment of the series of compartments 28, but the conduits and dainpers be arranged to give a diii'erent distribuhumidity and temmoisture obtained very hot furnaces and especially when using preheated air.
  • the presence of the moisture in the air causes the formation of water gas when this moisture strikes the lower layers of highly heatedV coal bed nearest to the metal parts, and the endothermic reaction with the coke that results absorbs heat and lowers the temperature of this zone and the metal parts beneath it.
  • the Water gas thus produced undergoes combustion within the furnace so that the heat is not lost.
  • I claim: 1. The hereindescribed method of operating a Stoker ire furnace, which includes the steps of introducing through the Stoker, 'and distributing throughout the area of incandescence adjacent the stoker, an air mixture humiditied only to the required degree for producing an endothermic reaction forming Water gas and cooling the hotter portion of the Stoker area, and consuming the Water gas.'
  • the hereindescribed method of operating a stoker fired furnace which includes the steps of introducing through the stoker and distributing throughout the area of incandescence adjacent the Stoker a mixture of heated, and relatively unheated humidiied air combined in proportionsto preserve only the requisite degree of humidification for producing an endothermic reaction forming lwater gas and cooling the hotter portion of the Stoker area, and consuming the Water gas.
  • an air heater supplying some air to the incandescent area adjacent the stoker, a humidiying air supply means also supplying air to the aforesaid area, and means regulating the air supplies to retain only the requisite humidity to produce alrelidothermic reaction profducing water gas at the aforesaid incandescent area to cool the hotter portion of the Stoker.
  • a humidiying air supply means also supplying air to the aforesaid area, and means regulating the air supplies to retain only the requisite humidity to produce alrelidothermic reaction profducing water gas at the aforesaid incandescent area to cool the hotter portion of the Stoker.
  • the hereindescribed method of operat- 'ing an endless chain grate stoker fired fur'- nace with high temperatures therein which includes the steps of introducing through I the Stoker, and distributing throu hout the area of incandescence of-.the fuel edadjacent the feed end of the Stoker, a preheated air mixture humldified to the'degree required for producing an endothermic reaction form- L ing water gas and thereby limiting the tem- J perature ofy the adjacent portion of the fuel bed'and cooling the adjacent portion of the Stoker, and consuming the water gas so l formed in the furnace.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Furnace Details (AREA)

Description

June 14, 1932. AQ E, UCKE 1,863,541
STEAII BOILER AND PROGESS OF PIRING IT Filed Dec. 10'. 1927 2 Sheets-Sheet l INVENTO j im! W' ATToRNEYa June 14, 1932. c; E. LucKE 1,863,541
STEAK BGH-1ER AND PROCESS 0F FIRING IT vFiled Dec, 10', 1927 2 Sheets-Sheet 2 r BY Wr rbd/ n ATTORNEYS leaving the the form shown these gases Parenteel June 14, 1932 CHARLES E. LUCKE, OF N EW YORK, N. Y., ASSIGNOR TO N11-ED STATES PATENT OFFICE THE BABCOCK & WILCOX COM- PANY, OF BAYONNE, NEW JERSEY, A CORPORATION OF NEW JERSEY STEAM BOILER AND PROCESS FIRING- IT Application filed December 10, 1927. Serial No. 239,099.
This invention relates to a steam boiler that4 is provided with a mechanical stoker and t0 the process of ring the boiler so that it can be operated at high ratings without overheating the stoker and especially with heated air. The invention will be understood from the description in connection with the accompanying drawings, in which Fig. 1 is a vertical section showing somewhat diagraminatically an illustrative embodiment of the invention, Fig. 2 is a section on an enlarged scale along the line 2-2 of Fig. 1; Fig. 3 is a section along the line 3 3 of Fig. 2 and Fig. 4 is a vertical section, partly broken away, illustrating a modification.
1n the drawings, reference character 1 indicates the furnace of a boiler that is provided with a. chain grate stoker 2. The exit for waste gases is shown at 3 and leads to an air heater 4 from which a conduit 5 leads to the stack. The cold air enters the air heater 4 at 6, and heated air passes out through a conduit 7 that is provided with a damper 8.
A humidifier lOor air is provided, and heat in the waste products of combustion air heater 4 is utilized for heating water to humidity the air in the humidiiier. The humidifier is provided Wih a separator 11 to remove unvaporized drops of water from the sprays 12. The heat for vaporization is derived from iiue gases, and in heat thewater to be sprayed into the air. A sump 13 is provided in the lower portion of the humidifier,
` and water is fed to the sump 13 through the pipe 14 with a iioat valve 15v for keeping the proper water level therein and to replace the evaporated water. A ump 16 forces water from the sump 13 through the heating coil 17 located in the waste `gas conduit 5.
A fan or blower 20 forces air into the humidiiier where it becomes saturated with moisture at an elevated temperature and this iixes the weight of water vapor carried. The heated saturated air passes through the outlet 21 that is provided with a damper 22 and joins the hot air from the outlet 7, and the mixture passes through the conduit 23 into the spaces below the stoker 2. Adjustment of relative position of dampers 8 and 22 determines the temperature of the air delivered to the stoker and also the amount of water vapor carried by that air. This adjustment also determines what part of the boiler wasteheat is utilized for raising the temperature of the air and what part for vaporizing water. A plurality obranches 25, each provided with a valve 26, leads from the conduit 23 to thecompartments 28 of. the chain grate stoker. The compartments 28 are provided in a` well known manner to divide the space under the chain grate Stoker into sections, and the amount of air admitted to each section can be regulated by means of the dampers 26.
In the modiiication shown in Fig. 4, air of one condition as to perature is admitted through the conduit 7 and passes through branches 25 that are provided with dampers 26', into some of the compartments 28 of the chain grate Stoker. Air that contains more from a humidiiier is deliveredthrough the injector nozzle 33 and draws in air of less humidity from conduit 3l producing a mixture in conduit 34 of higher humidity for one of the stoker compartments than is supplied through conduit 7 to the others. The air supplied to 7 and 33 may be the same as, for example, that from the air heater, or it may be dierent as to temperature and moisture. It may be supplied from another hu- In the modification shown in Fig. 4, the humidified airis indicated as being led to thekiirst compartment of the series of compartments 28, but the conduits and dainpers be arranged to give a diii'erent distribuhumidity and temmoisture obtained very hot furnaces and especially when using preheated air. The presence of the moisture in the air causes the formation of water gas when this moisture strikes the lower layers of highly heatedV coal bed nearest to the metal parts, and the endothermic reaction with the coke that results absorbs heat and lowers the temperature of this zone and the metal parts beneath it. The Water gas thus produced undergoes combustion within the furnace so that the heat is not lost. Without this temperature control of the metal parts of the stoker the allowable air temperature cannot-be high enough to give the best possible efficiency to the boiler unit by return Aof its waste heat, land with my invention it is possible to use hotter air than would otherwise be safe and thereby vvget higher boiler plant eiciencies. v
I claim: 1. The hereindescribed method of operating a Stoker ire furnace, which includes the steps of introducing through the Stoker, 'and distributing throughout the area of incandescence adjacent the stoker, an air mixture humiditied only to the required degree for producing an endothermic reaction forming Water gas and cooling the hotter portion of the Stoker area, and consuming the Water gas.'
2. The hereindescribed method of operating a stoker fired furnace which includes the steps of introducing through the stoker and distributing throughout the area of incandescence adjacent the Stoker a mixture of heated, and relatively unheated humidiied air combined in proportionsto preserve only the requisite degree of humidification for producing an endothermic reaction forming lwater gas and cooling the hotter portion of the Stoker area, and consuming the Water gas.
3. In combination with a furnace and stoker, an air heater supplying some air to the incandescent area adjacent the stoker, a humidiying air supply means also supplying air to the aforesaid area, and means regulating the air supplies to retain only the requisite humidity to produce alrelidothermic reaction profducing water gas at the aforesaid incandescent area to cool the hotter portion of the Stoker. W 4. The hereindescribed method of operat- 'ing an endless chain grate stoker fired fur'- nace with high temperatures therein, which includes the steps of introducing through I the Stoker, and distributing throu hout the area of incandescence of-.the fuel edadjacent the feed end of the Stoker, a preheated air mixture humldified to the'degree required for producing an endothermic reaction form- L ing water gas and thereby limiting the tem- J perature ofy the adjacent portion of the fuel bed'and cooling the adjacent portion of the Stoker, and consuming the water gas so l formed in the furnace. 1..; Y p CHARLES E. LUCKE.
US239099A 1927-12-10 1927-12-10 Steam boiler and process of firing it Expired - Lifetime US1863541A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2694991A (en) * 1948-08-14 1954-11-23 Babcock & Wilcox Co Forced draft primary and secondary air feeding system for furnaces with air preheating and tempering means
US2730971A (en) * 1949-09-15 1956-01-17 Birkner Max Furnace and boiler plant
US2842076A (en) * 1953-02-05 1958-07-08 Martin Johannes Josef Apparatus for distributing combustion air into different combustion zones of a furnace
US3280768A (en) * 1964-08-13 1966-10-25 Peacock Arthur Sidney Travelling grate stokers
FR2555711A1 (en) * 1983-11-28 1985-05-31 Seccacier Gas boiler
FR3014540A1 (en) * 2013-12-10 2015-06-12 Brunel Bureau Et SOLID FUEL BOILER AND CONDENSATION

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2694991A (en) * 1948-08-14 1954-11-23 Babcock & Wilcox Co Forced draft primary and secondary air feeding system for furnaces with air preheating and tempering means
US2730971A (en) * 1949-09-15 1956-01-17 Birkner Max Furnace and boiler plant
US2842076A (en) * 1953-02-05 1958-07-08 Martin Johannes Josef Apparatus for distributing combustion air into different combustion zones of a furnace
US3280768A (en) * 1964-08-13 1966-10-25 Peacock Arthur Sidney Travelling grate stokers
FR2555711A1 (en) * 1983-11-28 1985-05-31 Seccacier Gas boiler
FR3014540A1 (en) * 2013-12-10 2015-06-12 Brunel Bureau Et SOLID FUEL BOILER AND CONDENSATION

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