JPS5817519B2 - Bisaikanenriyouno Kikasouchi - Google Patents
Bisaikanenriyouno KikasouchiInfo
- Publication number
- JPS5817519B2 JPS5817519B2 JP50063372A JP6337275A JPS5817519B2 JP S5817519 B2 JPS5817519 B2 JP S5817519B2 JP 50063372 A JP50063372 A JP 50063372A JP 6337275 A JP6337275 A JP 6337275A JP S5817519 B2 JPS5817519 B2 JP S5817519B2
- Authority
- JP
- Japan
- Prior art keywords
- wall
- water
- supplied
- vaporization chamber
- pressure
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 230000008016 vaporization Effects 0.000 claims description 15
- 238000009834 vaporization Methods 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 10
- 239000000446 fuel Substances 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 239000002893 slag Substances 0.000 description 11
- 238000000926 separation method Methods 0.000 description 4
- 239000000945 filler Substances 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000006200 vaporizer Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000009970 fire resistant effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000001154 acute effect Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/52—Ash-removing devices
- C10J3/526—Ash-removing devices for entrained flow gasifiers
-
- 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
- C10J3/485—Entrained flow gasifiers
-
- 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
- C10J3/74—Construction of shells or jackets
-
- 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
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
- C10J3/845—Quench rings
-
- 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
- C10J3/86—Other features combined with waste-heat boilers
-
- 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
-
- 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
- C10J2300/0953—Gasifying agents
- C10J2300/0956—Air or oxygen enriched air
-
- 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
- C10J2300/0953—Gasifying agents
- C10J2300/0959—Oxygen
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Furnace Housings, Linings, Walls, And Ceilings (AREA)
- Gasification And Melting Of Waste (AREA)
- Air Supply (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
【発明の詳細な説明】
本発明は、例えは１５気圧〜８０気圧の高圧で供給され
る酸素含有ガス中に浮遊状態で含まれた微細化燃料の気
化装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for vaporizing atomized fuel contained in a suspended state in an oxygen-containing gas supplied at a high pressure of, for example, 15 atmospheres to 80 atmospheres.
この微細化燃料としては固体燃料または液体・燃料が使
用されることができる。A solid fuel or a liquid fuel can be used as the atomized fuel.
本発明の目的は、気化の過程中に＜＋＝しる熱の一部を
、気化装置の範囲内でもオ叶［１可能にし、また長時間
の作動後に整備や場合によって修理を必要とする部材に
良好に接近可能なように構成された気化装置を提供する
ことである。The purpose of the invention is to make it possible to remove a portion of the heat generated during the vaporization process even within the scope of the vaporization device, and also to eliminate the need for maintenance and possibly repair after long periods of operation. It is an object of the present invention to provide a vaporizer configured to allow good access to members.
この目的を達成するために本発明の構成では、気化室が
、管および壁より成り水を供給される構造体内に形成さ
れており、この構造体全体は外側の耐用外壁内に取出し
可能に配置されており、かつ、前記耐圧外壁と前記構造
体との間には絶縁層が設けられている。To this end, the invention provides an arrangement in which the vaporization chamber is formed within a water-supplied structure consisting of tubes and walls, the entire structure being removably arranged within the outer durable exterior wall. and an insulating layer is provided between the voltage-resistant outer wall and the structure.
本発明の一実施例ではこの絶縁層内には分離継ぎ目が設
けられている。In one embodiment of the invention, a separation seam is provided within this insulating layer.
有利には前記構造体はその内側を耐火性の突固め物質に
よって覆われている。Advantageously, the structure is covered on the inside with a fire-resistant tamping material.
また、本発明の別の実施例では下部の耐圧外壁底部とこ
れに接続したスラグ取出し筒が下方へ取外し可能に構成
されている。In another embodiment of the present invention, the bottom of the lower pressure-resistant outer wall and the slag removal tube connected thereto are configured to be removable downward.
本発明においては、気化室内で生じた熱を蒸気発生のた
めに利用することかできる。In the present invention, the heat generated within the vaporization chamber can be used to generate steam.
この場合１００気圧以上の飽和蒸気が生じることがあり
、このため前記構造体は気化装置に後置された廃熱ボイ
ラに接続されることができる。In this case, saturated steam of more than 100 atmospheres may be produced, for which purpose the structure can be connected to a waste heat boiler downstream of the vaporizer.
前記構造体は取出し可能に配置されているので、修理作
業を比較的価かな費用で行なうことができる。Since the structure is arranged in a removable manner, repair work can be carried out relatively inexpensively.
更に、前記構造体を極めて短時間で交換でき、この結果
何らかの機能障害の発生した際に生産停市が小さくてす
む。Furthermore, the structure can be replaced in a very short time, resulting in less production stoppage in the event of any malfunction.
次に図示の実施例につき本発明を説明する１、外側の耐
圧外壁１内には、全体として符号２で示されている、管
と壁とから成る構造体が配置されており、この構造体２
内には気化室３が形成されている。The invention will now be explained with reference to the embodiment shown: 1. Within the outer pressure-resistant wall 1 there is arranged a structure consisting of tubes and walls, generally indicated by the reference numeral 2. 2
A vaporization chamber 3 is formed inside.
この構造体２は互いに溶接された多数の管４を有してお
り、これらの管４は上部の環状導管５および下部の環状
導管６に接続している。This structure 2 has a number of tubes 4 welded together, which connect to an upper annular conduit 5 and a lower annular conduit 6.
下部の環状導管６へのボイラ水の供給は外部の環状導管
７から落下管８を介して行なわれ、加熱されたボイラ水
は上部の環状導管５から別の外部の環状導管９に排出さ
れる。Boiler water is supplied to the lower annular conduit 6 via a drop pipe 8 from an external annular conduit 7, and the heated boiler water is discharged from the upper annular conduit 5 into another external annular conduit 9. .
管と壁とから成る構造体２と気化室３との間には耐火性
の、突固め物質から成るライニング１０が配置されてお
り、このライニング１０によって構造体２が燃焼の直接
的な影響から守られている。A fire-resistant lining 10 of compacted material is arranged between the structure 2 of tubes and walls and the vaporization chamber 3, which protects the structure 2 from the direct effects of combustion. Protected.
構造体２と耐圧外壁１との間には絶縁層が配置されてお
り、この絶縁層は耐圧外壁１が不都合に高温になること
を阻１トする。An insulating layer is arranged between the structure 2 and the voltage-resistant outer wall 1, which prevents the voltage-resistant outer wall 1 from reaching an undesirably high temperature.
この絶縁層の外側層は本実施例においては、耐圧外壁に
接していて絶縁材料から成る絶縁外層１１から構成され
ており、この絶縁外層１１には構造体２の構成要素とし
ての絶縁充填材１２が接している。In this embodiment, the outer layer of this insulating layer is composed of an insulating outer layer 11 made of an insulating material and in contact with the voltage-resistant outer wall. are in contact with each other.
絶縁外層１１と絶縁充填材１２との間には分離継ぎ目１
３が設けられており、この分離継ぎ目１３、絶縁外層１
１および絶縁充填材１２には不活性気体例えば窒素が供
給され、作用する。There is a separation seam 1 between the insulating outer layer 11 and the insulating filler 12.
3 is provided, and this separation seam 13, the insulating outer layer 1
1 and the insulating filler 12 are supplied with an inert gas such as nitrogen.
不活性気体の流入は流入管片１４を介して行なわれ、こ
の不活性気体の流出は流出管片１５を介して行なわれる
。The inert gas flows in via the inlet fitting 14 and the inert gas flows out via the outlet fitting 15.
本実施例においては４つの水冷式のバーナ１６が設けら
れており、このバーナ１６には微粉炭・酸素混合物がそ
れぞれ吹込み導管１７を介して供給される。In this exemplary embodiment, four water-cooled burners 16 are provided, each of which is supplied with a pulverized coal/oxygen mixture via a blowing conduit 17 .
これらのバーナ１６は水平に配置されており、また第２
図から分るように、例えば直径３００朋の中心円に対す
る接線の延長線上に配置されている。These burners 16 are arranged horizontally and
As can be seen from the figure, it is arranged, for example, on an extension of a tangent to a central circle with a diameter of 300 mm.
生せしめられたガスは気化室からその上方にある円錐状
のガス流出管１８を通って流出する。The generated gas leaves the vaporization chamber through a conical gas outlet pipe 18 located above it.
このガス流出管１８は水冷機構を備えて構成されている
かまたは蒸気発生器としての機能も備えて構成されてお
り、このガス流出管１８には取水管片１９と出口管片２
０とが配置されている。The gas outlet pipe 18 is equipped with a water cooling mechanism or has a function as a steam generator, and the gas outlet pipe 18 is provided with a water intake pipe piece 19 and an outlet pipe piece 2.
0 is arranged.
ガス流出管１８内へは多数の水ノズル３３が開口してお
り、これらの水ノズル３３によって、発生したガスの急
速冷却とひいてはこのガス中に含まれていることのある
粘稠性のスラグ細片の凝固を行なうことができる。A number of water nozzles 33 open into the gas outlet pipe 18, and these water nozzles 33 rapidly cool the generated gas and thereby remove the viscous slag fines that may be contained in this gas. Coagulation of the pieces can be carried out.
燃料の気化の際に付加的に生じた液状のスラグは気化室
の底部内に配置された流出開口２１を通って流出し、こ
の流出開口２１は鋭角の滴下縁２２を備えている。The liquid slag additionally produced during the vaporization of the fuel flows out through an outlet opening 21 arranged in the bottom of the vaporization chamber, which outlet opening 21 is provided with an acute drip edge 22 .
スラグはスラグ取出し筒２３内の水だめ２４内へ落下し
、この水だめ２４内で粒状化する。The slag falls into a water reservoir 24 in the slag removal tube 23 and is granulated within this water reservoir 24.
粒状化したスラグは、図示されていない破砕機によって
破砕され、この破砕機に後置されたロックゲートを介し
て取り出される。The granulated slag is crushed by a crusher (not shown) and taken out through a lock gate provided after the crusher.
スラグ取出し筒２３は水冷機構を備えてかまたは蒸気発
生器として構成されており、この目的のために取水管片
２５と出口管片２６とを備えている。The slag removal tube 23 is equipped with a water cooling system or is constructed as a steam generator and is provided with an intake pipe piece 25 and an outlet pipe piece 26 for this purpose.
水だめ２４への給水は給水口２７を介して、また水だめ
２４からの排水は排水口２日を介して行なわれる。Water is supplied to the water reservoir 24 through a water supply port 27, and drainage from the water reservoir 24 is performed through a drain port 27.
スラグ取出し筒２３は水冷されるマンホール２９を備え
ており、このマンホール２９は気化室３に設けられたマ
ンホール３０と同様に温度および圧力の測定のための管
片３１を備えている。The slag removal tube 23 is equipped with a water-cooled manhole 29, which, like the manhole 30 provided in the vaporization chamber 3, is equipped with a tube piece 31 for measuring temperature and pressure.
流出開口２１へ向かって酸素管３２が延びており、この
酸素管３２は、スラグが流出開口２１の所に固着した場
合にこのスラグを溶融するためのものである。An oxygen pipe 32 extends towards the outlet opening 21 and is intended to melt the slag if it becomes stuck at the outlet opening 21.
第２図に示されているように更に点火バーナ４０が設け
られている。As shown in FIG. 2, an ignition burner 40 is also provided.
分離継ぎ目１３、水平な分離継ぎ目３４および、この分
離継ぎ目３４に接続していて排出管片３５を取囲んでい
る分離継ぎ目３６が設けられていることによって、バー
ナ１６を取外した後に構造体２を耐圧外壁１から容易に
上方に取出すことができる。The provision of a separating seam 13, a horizontal separating seam 34 and a separating seam 36 connected to this separating seam 34 and surrounding the discharge pipe piece 35 makes it possible to remove the structure 2 after removing the burner 16. It can be easily taken out upward from the pressure-resistant outer wall 1.
必要に応じて、スラグ取出し筒２３もまた、フランジ結
合部３８の結合の解除後に下部の耐圧外壁底部３７から
下方へ取外されることができる。If necessary, the slag removal cylinder 23 can also be removed downward from the lower pressure-resistant outer wall bottom 37 after the flange connection part 38 is uncoupled.
同様に耐圧外壁底部３Ｔもフランジ結合部３９の結合の
解除後に耐圧外壁１から取外されることができる。Similarly, the pressure-resistant outer wall bottom portion 3T can also be removed from the pressure-resistant outer wall 1 after the connection of the flange joint portion 39 is released.
本発明は図示の実施例に限定されるものではなく、バー
ナ１６が別の形式で配置されていてもよい。The invention is not limited to the illustrated embodiment; the burners 16 may be arranged in other ways.
本発明の構成は構造体２の形式に無関係である。The configuration of the invention is independent of the type of structure 2.
第１図は本発明の１実施例の気化装置の鉛直断面図、第
２図は第１図の■−■線に沿った断面図である。
１・・・・・・耐圧外壁、２・・・・・・構造体、３・
・・・・・気化室、４・・・・・・管、５，６，７．９
・・・・・・環状導管、８・・・・・・落下管、１０・
・・・・・ライニング、１１・・・・・・絶縁外層、１
２・・・・・・絶縁充填材、１３，３４．３６・・・・
・・分離継き泪、１４・・・・・・流入管片、１５・・
・・・・流出管片、１６・・・・・・バーナ、１７・・
・・・・吹込み導管、１８・・・・・・ガス流出管、１
９，２５・・・・・・取水管片、２０．２６・・・・・
・出口管片、２１・・・・・・流出開口、２２・・・・
・・滴下縁、２３・・・・・・スラグ取出し筒、２４・
・・・・・水ため、２７・・・・・・給水口、２８・・
・・・・排水口、２９．３０・・・・・・マンホール、
３１・・・・・・管片、３２・・・・・・酸素管、３３
・・・・・・水ノズル、３５・・・・・・排出管片、３
７・・・・・・耐圧外壁底部、３８ 、３９・・・・・
・フランジ結合部、４０・・・・・・点火バーナ。FIG. 1 is a vertical cross-sectional view of a vaporizer according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along the line ■-■ in FIG. 1...Pressure-resistant outer wall, 2...Structure, 3.
... vaporization chamber, 4 ... tube, 5, 6, 7.9
...Annular conduit, 8... Fall pipe, 10.
... Lining, 11 ... Insulating outer layer, 1
2...Insulating filler, 13,34.36...
... Separation joint tears, 14 ... Inflow pipe piece, 15 ...
...Outflow tube piece, 16...Burner, 17...
...Blowing conduit, 18... Gas outflow pipe, 1
9,25... Water intake pipe piece, 20.26...
・Outlet pipe piece, 21...Outflow opening, 22...
...Dripping edge, 23...Slag removal tube, 24.
...Water reservoir, 27...Water inlet, 28...
...Drainage port, 29.30 ...Manhole,
31...Pipe piece, 32...Oxygen tube, 33
...Water nozzle, 35 ...Discharge pipe piece, 3
7...Bottom of pressure-resistant outer wall, 38, 39...
・Flange joint, 40...Ignition burner.
Claims (1)
た微細化燃料の気化装置において、気化室３が、管およ
び壁より成り水を供給される構造体２内に形成されてお
り、この構造体２全体は外側の面」圧外壁１内に取出し
可能に配置されており、かつ、前記面ｔｆＥ外壁１と前
記構造体２との間には絶縁層１１．１２が設けられてい
ることを特徴とする、微細化燃料の気化装置。1 In an apparatus for vaporizing atomized fuel contained in a suspended state in an oxygen-containing gas supplied at high pressure, a vaporization chamber 3 is formed within a structure 2 consisting of a pipe and a wall and supplied with water. The entire structure 2 is removably arranged in the outer wall 1 on the outer surface, and an insulating layer 11, 12 is provided between the surface tfE outer wall 1 and the structure 2. A vaporization device for finely divided fuel, which is characterized by:
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2425962A DE2425962C3 (en) | 1974-05-30 | 1974-05-30 | Gas generator for the gasification of finely divided fuels |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS515302A JPS515302A (en) | 1976-01-17 |
| JPS5817519B2 true JPS5817519B2 (en) | 1983-04-07 |
Family
ID=5916764
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50063372A Expired JPS5817519B2 (en) | 1974-05-30 | 1975-05-27 | Bisaikanenriyouno Kikasouchi |
Country Status (17)
| Country | Link |
|---|---|
| JP (1) | JPS5817519B2 (en) |
| BE (1) | BE829733A (en) |
| BR (1) | BR7503392A (en) |
| CA (1) | CA1078613A (en) |
| CS (1) | CS181294B2 (en) |
| DD (1) | DD119266A5 (en) |
| DE (1) | DE2425962C3 (en) |
| DK (1) | DK140601B (en) |
| FR (1) | FR2273232B1 (en) |
| GB (1) | GB1501284A (en) |
| IE (1) | IE42149B1 (en) |
| IN (1) | IN143291B (en) |
| IT (1) | IT1037718B (en) |
| LU (1) | LU72613A1 (en) |
| NL (1) | NL7505661A (en) |
| SU (1) | SU839442A3 (en) |
| ZA (1) | ZA752996B (en) |
Families Citing this family (37)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1578443A (en) * | 1976-12-24 | 1980-11-05 | Shell Int Research | Apparatus for producing a gaseous fuel from finely divided solid or liquid fuels |
| NL7704399A (en) * | 1977-04-22 | 1978-10-24 | Shell Int Research | METHOD AND REACTOR FOR THE PARTIAL BURNING OF COAL POWDER. |
| DD145026A3 (en) * | 1978-09-28 | 1980-11-19 | Dieter Koenig | PRESSURE RELIEF DEVICE V N REACTORS |
| DE3009850C2 (en) * | 1980-03-14 | 1983-04-21 | Karrena GmbH, 4000 Düsseldorf | Reactor vessel |
| DE3009851C2 (en) * | 1980-03-14 | 1983-09-15 | Karrena GmbH, 4000 Düsseldorf | Reactor containers, in particular for gasifying fossil fuels |
| NL8101447A (en) * | 1981-03-24 | 1982-10-18 | Shell Int Research | METHOD FOR PREPARING HYDROCARBONS FROM CARBON-CONTAINING MATERIAL |
| DE3124263A1 (en) * | 1981-06-19 | 1983-01-05 | Karrena GmbH, 4000 Düsseldorf | LINING FOR A ROUND BURNING ROOM AT LEAST APPROXIMATELY CROSS-SECTIONED |
| DE3263016D1 (en) * | 1981-11-09 | 1985-05-15 | Shell Int Research | Apparatus for gasifying finely divided fuels |
| IN156182B (en) * | 1981-11-16 | 1985-06-01 | Shell Int Research | |
| DE3613508A1 (en) * | 1986-04-22 | 1987-10-29 | Krupp Koppers Gmbh | DEVICE FOR THE GASIFICATION OF FINE-DIVISION, IN PARTICULAR SOLID FUELS UNDER INCREASED PRESSURE |
| JPH07116456B2 (en) * | 1986-06-09 | 1995-12-13 | 大阪瓦斯株式会社 | Exothermic gas generator |
| DE3623604A1 (en) * | 1986-07-12 | 1988-01-14 | Krupp Koppers Gmbh | DEVICE FOR THE GASIFICATION OF FINE-DIVISION, IN PARTICULAR SOLID FUELS UNDER INCREASED PRESSURE |
| JPS63215794A (en) * | 1987-03-03 | 1988-09-08 | Nobuo Suzuki | Gas generator for biomass mainly composed of wood refuse powder |
| US4823741A (en) * | 1987-12-11 | 1989-04-25 | Shell Oil Company | Coal gasification process with inhibition of quench zone plugging |
| US4805562A (en) * | 1987-12-11 | 1989-02-21 | Shell Oil Company | Coal gasification process with inhibition of quench zone plugging |
| US4805561A (en) * | 1987-12-11 | 1989-02-21 | Shell Oil Company | Coal gasification process with inhibition of quench zone plugging |
| US4823742A (en) * | 1987-12-11 | 1989-04-25 | Shell Oil Company | Coal gasification process with inhibition of quench zone plugging |
| DE4017219A1 (en) * | 1990-05-29 | 1991-12-05 | Babcock Werke Ag | DEVICE FOR GASIFYING CARBONATED MATERIALS |
| DE19829385C1 (en) * | 1998-07-01 | 1999-10-28 | Krc Umwelttechnik Gmbh | Pressurised slagging gasifier for treating ash-containing carbonaceous materials |
| US8317885B2 (en) | 2004-11-22 | 2012-11-27 | Shell Oil Company | Apparatus for gasifying fuel with a dripper edge and heat shield |
| US9051522B2 (en) | 2006-12-01 | 2015-06-09 | Shell Oil Company | Gasification reactor |
| WO2008087133A1 (en) * | 2007-01-17 | 2008-07-24 | Shell Internationale Research Maatschappij B.V. | Gasification reactor |
| JP5420426B2 (en) | 2007-03-15 | 2014-02-19 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | Gasification reaction vessel with internal multi-tube wall and multiple burners |
| CN201205497Y (en) * | 2007-03-30 | 2009-03-11 | 国际壳牌研究有限公司 | Gasification Reactor |
| WO2009095365A2 (en) * | 2008-01-28 | 2009-08-06 | Shell Internationale Research Maatschappij B.V. | Process to start-up a coal gasification reactor |
| JP4844584B2 (en) * | 2008-04-11 | 2011-12-28 | 日本電気株式会社 | Equipment unit attachment / detachment device |
| DE102008033095A1 (en) * | 2008-07-15 | 2010-01-28 | Uhde Gmbh | Apparatus for slag removal from a coal gasification reactor |
| US8960651B2 (en) | 2008-12-04 | 2015-02-24 | Shell Oil Company | Vessel for cooling syngas |
| US8475546B2 (en) | 2008-12-04 | 2013-07-02 | Shell Oil Company | Reactor for preparing syngas |
| US20130199461A1 (en) | 2010-02-18 | 2013-08-08 | Eckhard Friese | Tubular wall assembly and gasification reactor |
| KR101900118B1 (en) * | 2011-01-14 | 2018-09-18 | 에어 프로덕츠 앤드 케미칼스, 인코오포레이티드 | Gasification reactor |
| EP2678407B1 (en) | 2011-02-24 | 2015-03-25 | Shell Internationale Research Maatschappij B.V. | Gasification reactor |
| CN102851080B (en) * | 2011-06-30 | 2015-08-26 | 通用电气公司 | Integrated gasification combined cycle power generation system and gasifying reactor and method |
| DE202014104519U1 (en) | 2014-09-22 | 2014-10-02 | Choren Industrietechnik GmbH | Reactor for entrained flow gasification of carbonaceous fuels |
| DE102014113653B4 (en) | 2014-09-22 | 2025-07-03 | Choren Industrietechnik GmbH | Reactor for entrained flow gasification of carbonaceous fuels |
| CN108204586B (en) * | 2018-01-17 | 2024-08-09 | 江苏新方圆电气设备制造有限公司 | Barrel part capable of discharging slag rapidly for film type slag cooler |
| CN112439764B (en) * | 2019-08-28 | 2023-01-20 | 中国石油化工股份有限公司 | Method for treating waste alumina in anthraquinone process hydrogen peroxide production process |
-
1974
- 1974-05-30 DE DE2425962A patent/DE2425962C3/en not_active Expired
-
1975
- 1975-04-29 IT IT22842/75A patent/IT1037718B/en active
- 1975-05-02 GB GB18550/75A patent/GB1501284A/en not_active Expired
- 1975-05-07 CS CS7500003206A patent/CS181294B2/en unknown
- 1975-05-09 ZA ZA00752996A patent/ZA752996B/en unknown
- 1975-05-13 IN IN959/CAL/75A patent/IN143291B/en unknown
- 1975-05-14 NL NL7505661A patent/NL7505661A/en not_active Application Discontinuation
- 1975-05-27 JP JP50063372A patent/JPS5817519B2/en not_active Expired
- 1975-05-28 DK DK237875AA patent/DK140601B/en not_active IP Right Cessation
- 1975-05-28 DD DD186312A patent/DD119266A5/xx unknown
- 1975-05-28 FR FR7516616A patent/FR2273232B1/fr not_active Expired
- 1975-05-28 BR BR4337/75D patent/BR7503392A/en unknown
- 1975-05-29 CA CA228,058A patent/CA1078613A/en not_active Expired
- 1975-05-29 LU LU72613A patent/LU72613A1/xx unknown
- 1975-05-29 IE IE1201/75A patent/IE42149B1/en unknown
- 1975-05-30 BE BE156908A patent/BE829733A/en not_active IP Right Cessation
- 1975-05-30 SU SU752146656A patent/SU839442A3/en active
Also Published As
| Publication number | Publication date |
|---|---|
| IE42149B1 (en) | 1980-06-18 |
| ZA752996B (en) | 1976-04-28 |
| IE42149L (en) | 1975-11-30 |
| IN143291B (en) | 1977-10-29 |
| BE829733A (en) | 1975-12-01 |
| DE2425962A1 (en) | 1975-12-11 |
| DK237875A (en) | 1975-12-01 |
| CA1078613A (en) | 1980-06-03 |
| DK140601C (en) | 1980-02-25 |
| FR2273232A1 (en) | 1975-12-26 |
| GB1501284A (en) | 1978-02-15 |
| DK140601B (en) | 1979-10-08 |
| DD119266A5 (en) | 1976-04-12 |
| FR2273232B1 (en) | 1980-08-01 |
| IT1037718B (en) | 1979-11-20 |
| CS181294B2 (en) | 1978-03-31 |
| SU839442A3 (en) | 1981-06-15 |
| BR7503392A (en) | 1976-04-27 |
| DE2425962B2 (en) | 1978-08-17 |
| DE2425962C3 (en) | 1979-04-05 |
| NL7505661A (en) | 1975-12-02 |
| JPS515302A (en) | 1976-01-17 |
| AU8164275A (en) | 1976-12-02 |
| LU72613A1 (en) | 1975-10-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS5817519B2 (en) | Bisaikanenriyouno Kikasouchi | |
| US4218423A (en) | Quench ring and dip tube assembly for a reactor vessel | |
| KR101449219B1 (en) | Highly efficient, clean and pressurized gasification apparatus for dry powder of carbonaceous material and method thereof | |
| US4157244A (en) | Gas-cooling method and apparatus | |
| JPS60120110A (en) | Soot blower device | |
| CN104531219A (en) | Pressure gasification process for simultaneously gasifying powdered coal and coal water slurry | |
| CN103436298B (en) | Swirl injection type coal water slurry gasification device | |
| JP7784423B2 (en) | Blast furnace with shaft supply of hot process gas | |
| JPS60155806A (en) | Combustion apparatus | |
| US2792058A (en) | Vaporising oil burner and method of vaporising and burning heavy fuel | |
| US2801158A (en) | Method of and apparatus for gasification of pulverized coal | |
| CS221507B2 (en) | Device for gasifying the coal | |
| CN104531221B (en) | A kind of gasification furnace structure that can simultaneously process fine coal and water-coal-slurry | |
| KR100220171B1 (en) | Hot dust recycling method and apparatus | |
| HU181855B (en) | Removing slag from a gasifier | |
| US20150107496A1 (en) | Biomass gasifier system for power generation | |
| US1716667A (en) | Process of producing water gas and extracting oil from oil shale | |
| JPS6239193B2 (en) | ||
| KR200335225Y1 (en) | dry distillation furnace for dry distillation gas generator of scrapped material, scrapped tire, scrapped resin | |
| US3997299A (en) | Apparatus for producing protective gas | |
| US3994244A (en) | Fluidized waste incinerator and method | |
| US1838667A (en) | Slagging furnace | |
| CN203582819U (en) | Entrained-flow bed gasifier for cyclone melt-cinder solidification | |
| CN204356292U (en) | A kind of gasification furnace structure that simultaneously can process fine coal and coal water slurry | |
| US3888632A (en) | Combustion chamber |