CA1156697A - Method of pneumatically conveying fine-grain fuel to a gasifier - Google Patents

Method of pneumatically conveying fine-grain fuel to a gasifier

Info

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
Application number
CA000360773A
Other languages
French (fr)
Inventor
Karl Peter
Heinz J. Filipiak
Wolfgang Grams
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.)
SAARBERG DR C OTTO GESELLSCHAFT fur KOHLEDRUCKVERGASUNG MBH
Original Assignee
SAARBERG DR C OTTO GESELLSCHAFT fur KOHLEDRUCKVERGASUNG MBH
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 SAARBERG DR C OTTO GESELLSCHAFT fur KOHLEDRUCKVERGASUNG MBH filed Critical SAARBERG DR C OTTO GESELLSCHAFT fur KOHLEDRUCKVERGASUNG MBH
Application granted granted Critical
Publication of CA1156697A publication Critical patent/CA1156697A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/723Controlling or regulating the gasification process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/34Details
    • B65G53/66Use 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/50Fuel charging devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/78High-pressure apparatus
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/093Coal

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.

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.

, ,, .. . . , ~.

,

Claims

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
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.
CA000360773A 1979-09-22 1980-09-19 Method of pneumatically conveying fine-grain fuel to a gasifier Expired CA1156697A (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

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