US1863541A - Steam boiler and process of firing it - Google Patents
Steam boiler and process of firing it Download PDFInfo
- 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
- Authority
- 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
Links
- 238000000034 method Methods 0.000 title description 7
- 238000010304 firing Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 239000007789 gas Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 235000007253 Trigonella corniculata Nutrition 0.000 description 1
- 240000004336 Trigonella corniculata Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000004326 stimulated echo acquisition mode for imaging Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING 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
- F23L1/00—Passages or apertures for delivering primary air for combustion
- F23L1/02—Passages or apertures for delivering primary air for combustion by discharging the air below the fire
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING 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
- F23L15/00—Heating of air supplied for combustion
- F23L15/04—Arrangements of recuperators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING 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
- F23L5/00—Blast-producing apparatus before the fire
- F23L5/04—Blast-producing apparatus before the fire by induction of air for combustion, e.g. using steam jet
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING 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
- F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
- F23L7/002—Supplying water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Definitions
- 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.
Landscapes
- 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US239099A US1863541A (en) | 1927-12-10 | 1927-12-10 | Steam boiler and process of firing it |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US239099A US1863541A (en) | 1927-12-10 | 1927-12-10 | Steam boiler and process of firing it |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1863541A true US1863541A (en) | 1932-06-14 |
Family
ID=22900613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US239099A Expired - Lifetime US1863541A (en) | 1927-12-10 | 1927-12-10 | Steam boiler and process of firing it |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1863541A (en) |
Cited By (6)
| 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 |
-
1927
- 1927-12-10 US US239099A patent/US1863541A/en not_active Expired - Lifetime
Cited By (6)
| 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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