CA1145617A - Pretreatment to dewater bottom ash from a stem generator firing solid fuels - Google Patents
Pretreatment to dewater bottom ash from a stem generator firing solid fuelsInfo
- Publication number
- CA1145617A CA1145617A CA000357957A CA357957A CA1145617A CA 1145617 A CA1145617 A CA 1145617A CA 000357957 A CA000357957 A CA 000357957A CA 357957 A CA357957 A CA 357957A CA 1145617 A CA1145617 A CA 1145617A
- Authority
- CA
- Canada
- Prior art keywords
- ash
- water
- hopper
- screen means
- discharge opening
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
- F23J1/02—Apparatus for removing ash, clinker, or slag from ash-pits, e.g. by employing trucks or conveyors, by employing suction devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Filtration Of Liquid (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
PRETREATMENT TO DEWATER BOTTOM ASH
FROM A STEAM GENERATOR FIRING SOLID FUELS
Abstract of the Invention Apparatus for handling ash produced in the combustion of coal in the furnace (10) of a steam generator, including an ash hopper (14) beneath the furnace (10), a water transport system (26) for carrying the ash away from the hopper (14), a screen arrangement (32) for separating most of the water from the ash, and a relatively small settling bin (40) or tank for separating the ash from the remainder of the water. The separated water can be recycled in a closed loop (44), to be used again as the transport water.
FROM A STEAM GENERATOR FIRING SOLID FUELS
Abstract of the Invention Apparatus for handling ash produced in the combustion of coal in the furnace (10) of a steam generator, including an ash hopper (14) beneath the furnace (10), a water transport system (26) for carrying the ash away from the hopper (14), a screen arrangement (32) for separating most of the water from the ash, and a relatively small settling bin (40) or tank for separating the ash from the remainder of the water. The separated water can be recycled in a closed loop (44), to be used again as the transport water.
Description
In coal-firecL steam generators, the manner in which the ash is disposed of is a matter of considerable importance. The equipment for handling the ash is costly and can require much maintenance. In prior systems, the ash is usually removed from an asl~ hopper beneath the steam generator furnace along with a considerable amount of water and allowed to settle out in dewatering bins over a long period of time, such as 18 hours. ThusJ large amounts of water have to be stored and held in reserve, not only requiring much water but also a huge storage facility. Also, in colder climates, the dewatering bins are subject to freezing and plugging during the lengthy dewatering period.
In accordanee witll the invention, an ash disposal system for ash dlscharged from a eoal-fired eombustion ehamber is provided, ineluding an ash llopper positioned beneath the eombustion ehamber into whieh tlle ash falls, means Eor maintaining a given water level in the ash hopper, a diseharge opening in the bottom of the ash hopper, through whieh the ash is diseharged, sereen means Eor separating ash from water, pipe means eonnecting the ash hopper diseharge opening with the screen means, means for adding transport water to the pipe at a point adjacent the ash hopper diseharge opening, moalls for reeyeling the water separated in the screoll means baek to tho point acljaeent tlle ash hopper discharge opening, and mealls by whicll the seplrltecl ash ean be clisehar~ed Erom the screon means.
rhe figure is a seetionZIl sicle view ot an asll clis})osll systom Eor the furnaee of a stellll gonerator.
I.ooking now to the clrawing, numeral 10 clesigllltes the furnaee of a steam generator in wh;ieh eoal is burned as 1 Euel. Slag and ash fall through the bottom opening 12 into an ash hopper 14, whieh is kept filled with water to a level 16 by means of pipe 18, _ ~5~
which continuously admits water to the hopper. An overf]ow pipe 20 keeps the water level constant.
~ valve 22 is periodically opened to discharge the ash. A clinker grinder 24 breaks up the large ash particles so that they will not become jammed in the discharge opening, and so that they may be easily transported in a stream of water away from the hopper 14. Generally, the material discharged from the hopper 14 contains 75% solids, and 25% water. Water is added to the transport pipe 26, by means of valved line 25, so that the mix transported therein is 20% ash and 80% water. This mixture is transported to a holding or surge tank 28.
A gate valve 30 in the bottom of tank 28 can be opened at short intervals, or be maintained in an opened position except when the equipment downstream thereof is being repaired, to discharge the ash and water into a vibrating dewatering screen arrangement 32. A pair of screens, 34 and 36, are continuously vibrated in any well-known manner, to separate the ash from a ma~ority of the water. The first screen 34 can separate out the more coarse particles, and screen 36 can remove the fines.
The screens are preferably slightly lnclinecl so that the solids gravi-tate towards and are dLschar~ed througll outlet 38. Some wnter will still be carried over wLth the ash The mlxturc bcLng ~ chnrged througll outlet 38 wlll be approxLmately 25% wnter nnd 75% ash, nnd Ls dlscharged Lnto holdLng tank 40. From here, Lt can be discllarged Lnto n truck, storage pond, etc.
The water f:lowing thro-l~t- the screens ls dlscharged through openlng 42, and flows througtl pipe 44 and pump 46 back to the hopper discharge to be used again as transport water.
From the above, it can be seen that a system is provided which elimi-
In accordanee witll the invention, an ash disposal system for ash dlscharged from a eoal-fired eombustion ehamber is provided, ineluding an ash llopper positioned beneath the eombustion ehamber into whieh tlle ash falls, means Eor maintaining a given water level in the ash hopper, a diseharge opening in the bottom of the ash hopper, through whieh the ash is diseharged, sereen means Eor separating ash from water, pipe means eonnecting the ash hopper diseharge opening with the screen means, means for adding transport water to the pipe at a point adjacent the ash hopper diseharge opening, moalls for reeyeling the water separated in the screoll means baek to tho point acljaeent tlle ash hopper discharge opening, and mealls by whicll the seplrltecl ash ean be clisehar~ed Erom the screon means.
rhe figure is a seetionZIl sicle view ot an asll clis})osll systom Eor the furnaee of a stellll gonerator.
I.ooking now to the clrawing, numeral 10 clesigllltes the furnaee of a steam generator in wh;ieh eoal is burned as 1 Euel. Slag and ash fall through the bottom opening 12 into an ash hopper 14, whieh is kept filled with water to a level 16 by means of pipe 18, _ ~5~
which continuously admits water to the hopper. An overf]ow pipe 20 keeps the water level constant.
~ valve 22 is periodically opened to discharge the ash. A clinker grinder 24 breaks up the large ash particles so that they will not become jammed in the discharge opening, and so that they may be easily transported in a stream of water away from the hopper 14. Generally, the material discharged from the hopper 14 contains 75% solids, and 25% water. Water is added to the transport pipe 26, by means of valved line 25, so that the mix transported therein is 20% ash and 80% water. This mixture is transported to a holding or surge tank 28.
A gate valve 30 in the bottom of tank 28 can be opened at short intervals, or be maintained in an opened position except when the equipment downstream thereof is being repaired, to discharge the ash and water into a vibrating dewatering screen arrangement 32. A pair of screens, 34 and 36, are continuously vibrated in any well-known manner, to separate the ash from a ma~ority of the water. The first screen 34 can separate out the more coarse particles, and screen 36 can remove the fines.
The screens are preferably slightly lnclinecl so that the solids gravi-tate towards and are dLschar~ed througll outlet 38. Some wnter will still be carried over wLth the ash The mlxturc bcLng ~ chnrged througll outlet 38 wlll be approxLmately 25% wnter nnd 75% ash, nnd Ls dlscharged Lnto holdLng tank 40. From here, Lt can be discllarged Lnto n truck, storage pond, etc.
The water f:lowing thro-l~t- the screens ls dlscharged through openlng 42, and flows througtl pipe 44 and pump 46 back to the hopper discharge to be used again as transport water.
From the above, it can be seen that a system is provided which elimi-
- 2 ~5~'7 nates the need for large settling tanks. The majority of the water can be quickly recycled, thus reducing the requirement for large quantities of water. Also, because very little time is involved, there are no freezing or plugging problems in the system. The majority of the water is constantly flowing.
t ~ 2a
t ~ 2a
Claims (4)
1. An ash disposal system for ash discharged from a coal-fired combustion chamber, including an ash hopper positioned beneath the combustion chamber into which the ash falls, means for maintaining a given water level in the ash hopper, a discharge opening in the bottom of the ash hopper, through which the ash is discharged, screen means for separating ash from water, pipe means connecting the ash hopper discharge opening with the screen means, means for adding transport water to the pipe at a point adjacent the ash hopper discharge opening, means for recycling the water separated in the screen means back to the point adjacent the ash hopper discharge opening, and means by which the separated ash can be discharged from the screen means.
2. An ash disposal system as set forth in Claim 1, including a holding tank in the pipe means upstream of the screen means.
3. An ash disposal system set forth in Claim 2, whrein the screen means includes a pair of screens, the first of which separates coarse ash particles from the water, and the second of which separates fine ash particles from the water.
4. An ash disposal system as set forth in Claim 3, including a settling tank downstream of the screen means ash dis-charge opening.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US9504179A | 1979-11-16 | 1979-11-16 | |
US95,041 | 1979-11-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1145617A true CA1145617A (en) | 1983-05-03 |
Family
ID=22248924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000357957A Expired CA1145617A (en) | 1979-11-16 | 1980-08-11 | Pretreatment to dewater bottom ash from a stem generator firing solid fuels |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0029235A1 (en) |
JP (1) | JPS5681167A (en) |
KR (1) | KR830004565A (en) |
AU (1) | AU6437380A (en) |
CA (1) | CA1145617A (en) |
ES (1) | ES8201719A1 (en) |
IN (1) | IN154188B (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1180954A (en) * | 1980-12-09 | 1985-01-15 | Kiyomi Okada | Combustion apparatus for granular solid fuel |
FR2560970B1 (en) * | 1984-03-07 | 1989-08-18 | Aiello Raymond | SOLID FUEL FIREPLACE |
JPS6243690U (en) * | 1986-08-21 | 1987-03-16 | ||
US5082572A (en) * | 1990-09-05 | 1992-01-21 | Ogden Martin Systems, Inc. | Ash vibration process and apparatus |
DE19830943B4 (en) * | 1998-07-10 | 2010-09-09 | Hitachi Power Europe Gmbh | Process for dewatering ash |
CN107300186A (en) * | 2017-06-06 | 2017-10-27 | 大唐贵州发耳发电有限公司 | A kind of HHT higher high tensile dehydration device |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB134081A (en) * | ||||
GB220749A (en) * | 1923-06-12 | 1924-08-28 | Underfeed Stoker Co Ltd | Improvements relating to the removal of ashes and the like from furnaces |
AT137077B (en) * | 1932-07-02 | 1934-04-10 | Anton Rothstein | Procedure and arrangement for removing the ash from the collecting hoppers under combustion boiler systems and other ash collectors. |
DE967861C (en) * | 1948-10-29 | 1957-12-19 | Babcock & Wilcox Dampfkessel W | Ash removal device for a furnace operated with excess pressure in the combustion chamber and method for ash removal with such a device |
JPS5341861A (en) * | 1976-09-29 | 1978-04-15 | Oki Electric Ind Co Ltd | Apparatus for removing solids or half-melted substances contained in treating solution |
-
1980
- 1980-08-11 CA CA000357957A patent/CA1145617A/en not_active Expired
- 1980-08-26 IN IN979/CAL/80A patent/IN154188B/en unknown
- 1980-11-12 ES ES496759A patent/ES8201719A1/en not_active Expired
- 1980-11-13 JP JP15894480A patent/JPS5681167A/en active Pending
- 1980-11-14 AU AU64373/80A patent/AU6437380A/en not_active Abandoned
- 1980-11-14 EP EP80107060A patent/EP0029235A1/en not_active Withdrawn
- 1980-11-14 KR KR1019800004377A patent/KR830004565A/en unknown
Also Published As
Publication number | Publication date |
---|---|
JPS5681167A (en) | 1981-07-02 |
IN154188B (en) | 1984-09-29 |
AU6437380A (en) | 1981-05-21 |
ES496759A0 (en) | 1982-01-01 |
EP0029235A1 (en) | 1981-05-27 |
KR830004565A (en) | 1983-07-13 |
ES8201719A1 (en) | 1982-01-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4144088A (en) | Process of reclaiming used foundry sand | |
CA1145617A (en) | Pretreatment to dewater bottom ash from a stem generator firing solid fuels | |
US4455148A (en) | Method for de-ashing and transportation of coal | |
US3073652A (en) | Transportation of coal by pipeline | |
US20110226194A1 (en) | Bottom Ash Dewatering System Using a Remote Submerged Scraper Conveyor | |
GB985817A (en) | Improvements in slag conditioning means | |
CA1320642C (en) | Slag removal system for a solid fuels gasification reactor | |
RU2520466C2 (en) | Gating of dust accumulating at dust trap plant for rough gas | |
KR100324856B1 (en) | Slag treatment system | |
CA1178061A (en) | Process for the continuous blowing of fine-particle reducing agents, especially mineral oil, into a shaft furnace | |
RU2150422C1 (en) | Method of introduction of second flow of dust-like materials into pneumatic transportation pipeline along which first flow of dust-like materials with variable delivery is transported | |
US3313251A (en) | Method and apparatus for handling and burning coal slurries | |
Shah | Fundamentals, troubleshooting & maintenance of ash handling plants and pneumatic conveying systems for bulk materials | |
EP0671588B1 (en) | Cleaning methods for pulverized coal injection systems | |
CA1043837A (en) | System for hydraulically transporting solid material | |
US3517628A (en) | Process for the treatment of crude coal slurry for fuel purposes | |
US3060869A (en) | Sewage sludge disposal | |
DE202024000232U1 (en) | Device for dry granulation of liquid slags resulting from fuel gasification and/or liquid ash separation from separators | |
PL203253B1 (en) | Method and facility for utilization of incomplete combustion products | |
US5183478A (en) | Process for dewatering quenched slag | |
US20070210012A1 (en) | Wet solids removal and separation system | |
PL112063B1 (en) | Method of autothermal gasification of the fuel of grained fraction,especially hard coal,and apparatus therefor | |
SU992359A1 (en) | Installation for hydraulic transport of loose materials | |
Sisler et al. | Anthracite culm and silt | |
JPH11106761A (en) | Gasification apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MKEX | Expiry |