CA1156697A - Method of pneumatically conveying fine-grain fuel to a gasifier - Google Patents
Method of pneumatically conveying fine-grain fuel to a gasifierInfo
- Publication number
- CA1156697A CA1156697A CA000360773A CA360773A CA1156697A CA 1156697 A CA1156697 A CA 1156697A CA 000360773 A CA000360773 A CA 000360773A CA 360773 A CA360773 A CA 360773A CA 1156697 A CA1156697 A CA 1156697A
- Authority
- CA
- Canada
- Prior art keywords
- gasifier
- fuel
- fine
- container
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/723—Controlling or regulating the gasification process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/66—Use of indicator or control devices, e.g. for controlling gas pressure, for controlling proportions of material and gas, for indicating or preventing jamming of material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/50—Fuel charging devices
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/78—High-pressure apparatus
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Air Transport Of Granular Materials (AREA)
- Feeding And Controlling Fuel (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
A method of operating a device for the pneumatic conveyance of fine-grain fuels to a gasifier, in which the propellent gas and also a pressure maintaining gas (tensioning gas) are introduced into a tank provided with an entry lock, and feed the fuel to the gasifier via conveying pipes which is characterized in that the quantity of fuel supplied to the gasifier is controlled by a device which measures the difference between the pressure in the pressurized tank and the pressure in the gasifier.
A method of operating a device for the pneumatic conveyance of fine-grain fuels to a gasifier, in which the propellent gas and also a pressure maintaining gas (tensioning gas) are introduced into a tank provided with an entry lock, and feed the fuel to the gasifier via conveying pipes which is characterized in that the quantity of fuel supplied to the gasifier is controlled by a device which measures the difference between the pressure in the pressurized tank and the pressure in the gasifier.
Description
2 -A method of ?neu~ tically conveying fine-grain fuel to a ga~ifisr This invention relate~ to a method of operating a device for the pneumatic conveyance of fine-grain fuels to a gasifier, in which the ~ropellent gas and also a pressure maintaining ~ ten~oning ~as~
are introduced into a tank provided with an entry lock, ~nd feed the fuel to the gasifier via conveying pipes.
It ia known to pro~ide pressurized tanks of this kind ~rith no~zle a~semblies, i.e.~ vertically adjustable conduits ectending throu~h the ta~k wall for the conveying gas, an open pipe of the same size being disposed axially above the top end o~ the conduit and Oerving to convey the fuel - a ground and dried coal - to the gasifier. The bottom end of the conduit is adjustablG by up to about 50 ~ for example. The hei~ht of an ~ular gap betwee~ the t~o pipe ends can thus be adjusted and the gap can also be closed~
The object of thi~ invention is to control in the simple~t pos~ible way the qu~nti~y of fuel fed by the pre~Ouri~ed t2~k to the gasifier.
Experiments with pneumatic conveyors of thi~ ki.nd ha~e surprisin~ly sho~m that there is a l;~ear relationship bet.,een the quantity of fine-grain fuel fed to the gasi~ier throu~h the conduit connecting the pr~ssuriæed t~lk and the ~sifier~ ar.d ths di~ference in pressures between the pre~surized t~lk on the one hand and the gasifier on the other.
Accordingly, the invention propoces that the tran~mitter used to control the amount of fuel fed to the gasifier should be a device ,' :
~ ~5~69~
ch measures the said differenlial precs~eO The control can be effected, for example, by var~Jing the rate of flow Or the press~re maintaining ga~ fed into the pressurized tank. The control can al~o be effected by influencing other operating variable~ on which the amount of fuel fed to the conve~ing conduit is dependentO
The pre~sure-difference meaOuring device is connected to a device adjusted to the set-value of a s~ecific differential pressure equivalent to the required qua~tity of delivered coal. Ii` the actual value devlate~ from the set value~ a control member is actuated by me~ns of which the rate of flow of pre~sure maintaining gas i~ altered.
1 ~5~697 The accompanyin~ dra~"in~ show~ one exemplified embodiment of performance of the new proress in a plant for conveying fine-~rain fuel to a ga~ifier.
A ga~ifier 10 and a ~ressurized tank 11 are 3hown ~urely diagra~matically. Reference 12 denotes the fine-grain coal filling in the pressurized tanlcv Reference 13 denotes the propellent ~as supply pipe, which contains a valve 14 and which is ~ubject to the action of an instrument 26 for controlling the gas throughput. Reference 15 is the conduit for supp].~ing the flow of pressure maintaining gas, and this conduit contains a valve 16. The coal is conveyed from the tank 11 to the gasifier 10 via a conduit 17.
Conduit portion 13 and conveyin~ conduit 17 are connected by a conduit 18 extending through the tanlc 11. In6ide the filling 12, conduit 18 is provided ~.rth a clo6ure device 19 such that ~rhen it ia open the fine-grain fuel passes from the filling 12 into ccnduit 18 and then into the conveying conduit 17.
Reference 20 is a device which on the one hand i~ connected by a conduit 21 to ths ta~ç 11 and on the other hand ~via the ccnduit 22 to the ga3ifier 10. It mea~ure~ the di~ference in the pre~ures in the two device~ This differential pres6ure is an index of the amount of fine-grain material conveyed through the conduit 17.
The am.ount of fuel fed per unit of time to the gasifier 10 determines the differential pres~ure mea~ured in the device 20. To keep the a~ount of fuel con~tant, a specific value mu3t be maintained for the differential ~res~ure between ~he ga~ifier and the pre~surized tank.
:
.' ' 1 1 5~69 ' ` ' Thia differential presaure value i~ fed to the set-value tra~3mitter 23. The device~ 20 and 23 act U~G~ the controller 24, I the latter detect~ deviations of the actual value measured by device 20 from the set value, it influences valve 16 via conduit 25, and hence the ~upply of pres~ure maintaining gas, in the direction ~uch that the predetermined value for the differential pre~sure bet~reen the pres~urized tank and the gasifier is re~tored, so that the quantity of fine-grain fuel delivered to the g~sifier via conduit 17 has the predetermined value~
It is clear that thi~ type of control for the operation of the gasifier i~ very simple and requires only simple equipment.
, ,, .. . . , ~.
,
are introduced into a tank provided with an entry lock, ~nd feed the fuel to the gasifier via conveying pipes.
It ia known to pro~ide pressurized tanks of this kind ~rith no~zle a~semblies, i.e.~ vertically adjustable conduits ectending throu~h the ta~k wall for the conveying gas, an open pipe of the same size being disposed axially above the top end o~ the conduit and Oerving to convey the fuel - a ground and dried coal - to the gasifier. The bottom end of the conduit is adjustablG by up to about 50 ~ for example. The hei~ht of an ~ular gap betwee~ the t~o pipe ends can thus be adjusted and the gap can also be closed~
The object of thi~ invention is to control in the simple~t pos~ible way the qu~nti~y of fuel fed by the pre~Ouri~ed t2~k to the gasifier.
Experiments with pneumatic conveyors of thi~ ki.nd ha~e surprisin~ly sho~m that there is a l;~ear relationship bet.,een the quantity of fine-grain fuel fed to the gasi~ier throu~h the conduit connecting the pr~ssuriæed t~lk and the ~sifier~ ar.d ths di~ference in pressures between the pre~surized t~lk on the one hand and the gasifier on the other.
Accordingly, the invention propoces that the tran~mitter used to control the amount of fuel fed to the gasifier should be a device ,' :
~ ~5~69~
ch measures the said differenlial precs~eO The control can be effected, for example, by var~Jing the rate of flow Or the press~re maintaining ga~ fed into the pressurized tank. The control can al~o be effected by influencing other operating variable~ on which the amount of fuel fed to the conve~ing conduit is dependentO
The pre~sure-difference meaOuring device is connected to a device adjusted to the set-value of a s~ecific differential pressure equivalent to the required qua~tity of delivered coal. Ii` the actual value devlate~ from the set value~ a control member is actuated by me~ns of which the rate of flow of pre~sure maintaining gas i~ altered.
1 ~5~697 The accompanyin~ dra~"in~ show~ one exemplified embodiment of performance of the new proress in a plant for conveying fine-~rain fuel to a ga~ifier.
A ga~ifier 10 and a ~ressurized tank 11 are 3hown ~urely diagra~matically. Reference 12 denotes the fine-grain coal filling in the pressurized tanlcv Reference 13 denotes the propellent ~as supply pipe, which contains a valve 14 and which is ~ubject to the action of an instrument 26 for controlling the gas throughput. Reference 15 is the conduit for supp].~ing the flow of pressure maintaining gas, and this conduit contains a valve 16. The coal is conveyed from the tank 11 to the gasifier 10 via a conduit 17.
Conduit portion 13 and conveyin~ conduit 17 are connected by a conduit 18 extending through the tanlc 11. In6ide the filling 12, conduit 18 is provided ~.rth a clo6ure device 19 such that ~rhen it ia open the fine-grain fuel passes from the filling 12 into ccnduit 18 and then into the conveying conduit 17.
Reference 20 is a device which on the one hand i~ connected by a conduit 21 to ths ta~ç 11 and on the other hand ~via the ccnduit 22 to the ga3ifier 10. It mea~ure~ the di~ference in the pre~ures in the two device~ This differential pres6ure is an index of the amount of fine-grain material conveyed through the conduit 17.
The am.ount of fuel fed per unit of time to the gasifier 10 determines the differential pres~ure mea~ured in the device 20. To keep the a~ount of fuel con~tant, a specific value mu3t be maintained for the differential ~res~ure between ~he ga~ifier and the pre~surized tank.
:
.' ' 1 1 5~69 ' ` ' Thia differential presaure value i~ fed to the set-value tra~3mitter 23. The device~ 20 and 23 act U~G~ the controller 24, I the latter detect~ deviations of the actual value measured by device 20 from the set value, it influences valve 16 via conduit 25, and hence the ~upply of pres~ure maintaining gas, in the direction ~uch that the predetermined value for the differential pre~sure bet~reen the pres~urized tank and the gasifier is re~tored, so that the quantity of fine-grain fuel delivered to the g~sifier via conduit 17 has the predetermined value~
It is clear that thi~ type of control for the operation of the gasifier i~ very simple and requires only simple equipment.
, ,, .. . . , ~.
,
Claims
1. Method for the regulation of the throughput of pneumatically conveyed fine-particled fuel through a transport conductor, which is conducted through a container subjected to the pressure of a pressurizing gas and which joins the container with a gasifier, wherein the transport conductor contains closure means within the container for permitting the fine-particled fuel to pass into the transport conductor when the closure means is open, characterized in that the regula-tion of the amount of fuel led into the gasifier is effected in dependence upon the pressure difference between that in the container and that in the gasifier, which pressure difference is measured by known means and compared with a reference point, and in that the flow of the pressurizing gas led into the container is increased with variations of the pressure difference below the reference point and decreased with variations above the reference point.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19792938369 DE2938369A1 (en) | 1979-09-22 | 1979-09-22 | METHOD FOR PNEUMATICALLY CONVEYING FINE GRAIN FUEL TO A CARBURETOR |
DEP2938369.5-24 | 1979-09-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1156697A true CA1156697A (en) | 1983-11-08 |
Family
ID=6081560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000360773A Expired CA1156697A (en) | 1979-09-22 | 1980-09-19 | Method of pneumatically conveying fine-grain fuel to a gasifier |
Country Status (9)
Country | Link |
---|---|
AU (1) | AU6246680A (en) |
BR (1) | BR8006000A (en) |
CA (1) | CA1156697A (en) |
DE (1) | DE2938369A1 (en) |
FR (1) | FR2466044A1 (en) |
GB (1) | GB2059377B (en) |
IN (1) | IN153341B (en) |
PL (1) | PL226791A1 (en) |
ZA (1) | ZA805781B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108628352A (en) * | 2018-04-19 | 2018-10-09 | 兰州空间技术物理研究所 | A kind of solid-state working medium gasification flow automatic control device |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DD206309A3 (en) * | 1981-07-17 | 1984-01-18 | Kretschmer Horst | METHOD FOR REGULATING MASS STRUCTURES |
JPS59124624A (en) * | 1982-12-27 | 1984-07-18 | Kawasaki Steel Corp | Method for distribution and transport of pulverized/ granular material |
DE3810404A1 (en) * | 1988-03-26 | 1989-10-12 | Krupp Koppers Gmbh | METHOD AND DEVICE FOR PNEUMATICALLY CONVEYING A FINE-GRAINED TO DUST-SHAPED FUEL IN A GASIFICATION REACTOR UNDER INCREASED PRESSURE |
DE3823773A1 (en) * | 1988-07-14 | 1990-01-18 | Krupp Koppers Gmbh | METHOD FOR DETERMINING AND CONTROLLING THE FUEL MASS CURRENT IN PARTIAL OXIDATION (GASIFICATION) OF FINE-GRAINED TO DUST-SHAPED FUELS |
DE4432994C2 (en) * | 1994-09-16 | 2003-01-30 | Gerd Krischik | Plant for the discharge of fine dust |
CN111272508B (en) * | 2020-02-29 | 2024-05-17 | 天津大学 | Device for loading dry particles into Hall-Shore thin plate by adopting pneumatic force |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1345088A (en) * | 1962-10-24 | 1963-12-06 | Siderurgie Fse Inst Rech | Improvements to the methods of regulating injections of pulverulent products into the blast furnace nozzles |
DE2703736C2 (en) * | 1977-01-29 | 1982-11-25 | Freier Grunder Eisen- Und Metallwerke Gmbh, 5908 Neunkirchen | Device for pneumatic upward conveyance of powdery or fine-grained bulk material |
-
1979
- 1979-09-22 DE DE19792938369 patent/DE2938369A1/en not_active Ceased
-
1980
- 1980-09-17 PL PL22679180A patent/PL226791A1/xx unknown
- 1980-09-17 AU AU62466/80A patent/AU6246680A/en not_active Abandoned
- 1980-09-18 ZA ZA00805781A patent/ZA805781B/en unknown
- 1980-09-19 BR BR8006000A patent/BR8006000A/en unknown
- 1980-09-19 CA CA000360773A patent/CA1156697A/en not_active Expired
- 1980-09-22 FR FR8020367A patent/FR2466044A1/en not_active Withdrawn
- 1980-09-22 GB GB8030536A patent/GB2059377B/en not_active Expired
- 1980-12-04 IN IN1341/CAL/80A patent/IN153341B/en unknown
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108628352A (en) * | 2018-04-19 | 2018-10-09 | 兰州空间技术物理研究所 | A kind of solid-state working medium gasification flow automatic control device |
CN108628352B (en) * | 2018-04-19 | 2021-07-06 | 兰州空间技术物理研究所 | Solid working medium gasification flow automatic control device |
Also Published As
Publication number | Publication date |
---|---|
GB2059377B (en) | 1983-12-07 |
FR2466044A1 (en) | 1981-03-27 |
PL226791A1 (en) | 1981-06-19 |
GB2059377A (en) | 1981-04-23 |
BR8006000A (en) | 1981-03-31 |
ZA805781B (en) | 1981-09-30 |
DE2938369A1 (en) | 1981-04-16 |
AU6246680A (en) | 1981-04-09 |
IN153341B (en) | 1984-07-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE3211045C2 (en) | ||
US6666629B2 (en) | Process for conveying granular solids | |
US4146370A (en) | Process and apparatus for the partial combustion of coal powder | |
US2924489A (en) | Process and apparatus for conveying finely divided material | |
US4381897A (en) | Installation for transporting fine-grained material | |
EP0202796B1 (en) | Apparatus and process for pneumatically conveying particulate material | |
ES485899A1 (en) | Pneumatic conveyor of adjustable conveyance capacity for powdered to granular bulk material | |
CA1156697A (en) | Method of pneumatically conveying fine-grain fuel to a gasifier | |
IT1027970B (en) | Delivery control system for pneumatic bulk conveyor - varies material fed into fluidised column in response to gas press | |
CA1162962A (en) | Installation for transporting fine-grained material | |
US5899641A (en) | Bulk material conveying system and ejector therefor | |
JPS6317650Y2 (en) | ||
US3599832A (en) | Flow control of fluidized material | |
GB1146823A (en) | Powder spray device | |
SE9202928L (en) | Method and apparatus for dispensing granular material from a pressurized container | |
GB981826A (en) | Fluidizable solid injection system for furnaces | |
US2608446A (en) | Flux feed mechanism for cutting torches | |
CN108795503A (en) | Pressurization of dry pulverized coal dense-phase transporting system and method | |
GB1560297A (en) | Apparatus for the pneumatic conveyance of pulverulent or granular materials | |
JPS57107316A (en) | Method and device of distribution control for high pressure powder | |
US4483646A (en) | Apparatus for distributing powdered particles | |
US4089563A (en) | Apparatus for pneumatic conveyance of pulverulent or granular materials | |
CA1223774A (en) | Arrangement for introducing coal into a combustion chamber under elevated pressure | |
JPS59115981A (en) | Method and device for blowing in powdered and granular body into smelting furnace, etc. | |
JPH0356274B2 (en) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MKEX | Expiry |