JPS6375093A - Reactor for gasifying coal - Google Patents
Reactor for gasifying coalInfo
- Publication number
- JPS6375093A JPS6375093A JP62219320A JP21932087A JPS6375093A JP S6375093 A JPS6375093 A JP S6375093A JP 62219320 A JP62219320 A JP 62219320A JP 21932087 A JP21932087 A JP 21932087A JP S6375093 A JPS6375093 A JP S6375093A
- Authority
- JP
- Japan
- Prior art keywords
- reactor
- cyclone
- coal gasification
- gas cyclone
- dust
- 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.)
- Pending
Links
- 239000003245 coal Substances 0.000 title description 11
- 239000000428 dust Substances 0.000 claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 239000000446 fuel Substances 0.000 claims description 2
- 238000002309 gasification Methods 0.000 description 11
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 5
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 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
- C10J3/54—Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
- C10J3/56—Apparatus; Plants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C11/00—Accessories, e.g. safety or control devices, not otherwise provided for, e.g. regulators, valves in inlet or overflow ducting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/24—Multiple arrangement thereof
- B04C5/28—Multiple arrangement thereof for parallel flow
-
- 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
- C10J3/523—Ash-removing devices for gasifiers with stationary fluidised bed
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Cyclones (AREA)
- Industrial Gases (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 〔産業上の利用分}〕 本発明は、炭素含有燃料のガス化用反応器に関する。[Detailed description of the invention] [Industrial use] The present invention relates to a reactor for the gasification of carbon-containing fuels.
従来の石炭ガス化方法では、発生したガスが反応器の後
に接続される高温ガスサイクロンにおいて粉塵を除去さ
れる。後に接続されるサイクロンとして、反応器とは別
に設けられて耐火内張りされた圧力容器として構成され
る装置が用いられるが、これを特定の動作点に設計せね
ばならない。In conventional coal gasification methods, the generated gas is cleaned of dust in a hot gas cyclone connected after the reactor. As a subsequent cyclone, a device is used which is separate from the reactor and is constructed as a pressure vessel with a refractory lining, which must be designed for a specific operating point.
本発明の基礎になっている課題は、石炭ガス化反応器の
ために、構造費が少なく安価に製心可能で負荷変化の際
調整可能なサイクロン分雛器に基く除ル装置を提供する
ことである。The problem underlying the present invention is to provide a removal device for coal gasification reactors based on a cyclone splitter that has low constructional costs, can be centered at low cost, and can be adjusted in the event of load changes. It is.
この課題を解決するため本発明によれば、反応器に生ず
るガスの除塵用高温ガスサイクロンが反応器内にまとめ
られている。In order to solve this problem, according to the present invention, a high-temperature gas cyclone for removing dust from the gas generated in the reactor is integrated in the reactor.
石炭ガス化反応器として圧力容器が用いられるので、反
応器内に設けられるサイクロン用の圧力外被及び耐火内
張りが不要になる。Since a pressure vessel is used as the coal gasification reactor, there is no need for a pressure jacket and a refractory lining for the cyclone within the reactor.
口前変化の際サイクロンの分譲効率をほぼ一定に保つこ
とができるようにするため、個々のサイクロンの入口を
移動可能な板により閉鎖することができる。操作は反応
器外から7ic気的に駆動されるねじ軸を介して行なわ
れる。In order to be able to keep the dispensing efficiency of the cyclones approximately constant during the mouth change, the inlets of the individual cyclones can be closed off by movable plates. Operation is carried out via a 7ic pneumatically driven screw shaft from outside the reactor.
分難サイクロンが石炭ガス化反応器内にまとめられてい
ることにより、Q何字的配置のため、灰及び粉塵を1つ
の搬送通路装置のみで排出することができる。Because the separation cyclones are integrated in the coal gasification reactor, the ash and dust can be discharged with only one conveying channel device due to the Q-shaped arrangement.
概略図に基いて実ゐ例を以下に説明する。 An example will be explained below based on a schematic diagram.
第1図は、石炭ガス化反応器lと横に設置されてその後
に接続される高温ガスサイクロン2とを示している。サ
イクロン入口は3で、耐熱板から成る没入管が4で、耐
火内張りが5で、また圧力外被が6で示されている。FIG. 1 shows a coal gasification reactor 1 and a hot gas cyclone 2 installed laterally and connected afterwards. The cyclone inlet is indicated at 3, the immersion tube made of heat-resistant plate at 4, the refractory lining at 5, and the pressure jacket at 6.
第2図ないし第4図に示す石炭ガス化反応器lとして、
例えばドイツ連邦共和国特許出別箇P3600432.
4号に記載されているような形式の反応器、しかも横形
流fiffl IC’1反応器が用いられる。As the coal gasification reactor l shown in Figures 2 to 4,
For example, the Federal Republic of Germany patent article P3600432.
A reactor of the type described in No. 4 is used, but also a horizontal flow fiffl IC'1 reactor.
第4図には左に反応器lの反応空間12が示され、その
右に堰により隔離されて除塵空間14がある。In FIG. 4, the reaction space 12 of the reactor I is shown on the left, and the dust removal space 14 is located on the right, separated by a weir.
第4図では、除塵空間14に1つの高温ガスサイクロン
7しか示されてないが、第2図及び第3図では、除塵空
間4が複数の高温ガスサイクロン7を持っている。In FIG. 4, only one high-temperature gas cyclone 7 is shown in the dust removal space 14, but in FIGS. 2 and 3, the dust removal space 4 has a plurality of high-temperature gas cyclones 7.
4つのサイクロンは同じ構窃である。反応器内に存在す
る正圧のため、ガス供給は均一である。サイクロンは耐
熱板から1偕されている。The four cyclones are the same plagiarism. Due to the positive pressure present in the reactor, the gas supply is uniform. The cyclone is made from a heat-resistant plate.
圧力外被及び耐火円張りは必要でない。Pressure jacketing and fireproof shingles are not required.
サイクロンの清浄ガス出口管は、反応器壁の管貫通部に
補償装置を含んでいる。The clean gas outlet pipe of the cyclone contains a compensation device in the pipe penetration in the reactor wall.
移動可能な閉鎖装@10により、負荷変化の際分譲効率
を一定に保つため、ねじ軸に設けられる板により、個々
のサイクロン人口3が閉鎖される。操作は反応器外から
〒11動機を介して行なわれる。大した差圧が存在しな
いので、サイクロン入口上への板の載置部は密封片を必
要としない。閉鎖装置10の反応器壁n通は、射出ガス
環を持つ水冷パツキン箱において行なわれる。By means of a movable closure @10, the individual cyclone population 3 is closed off by means of a plate mounted on the screw shaft in order to keep the distribution efficiency constant during load changes. The operation is carried out from outside the reactor via the 11 motor. The rest of the plate on the cyclone inlet does not require a sealing piece since there are no significant pressure differentials. The reactor wall n passage of the closure device 10 takes place in a water-cooled packing box with an injection gas ring.
高温ガスサイクロン7により分等される粉塵を排出する
ため、水冷パケット車8が設けられている。天空間13
からの灰も同様に水冷パケット卓9により排出される。A water-cooled packet truck 8 is provided to discharge the dust separated by the hot gas cyclone 7. Heavenly space 13
The ash from the ash is likewise discharged by the water-cooled packet table 9.
反応器内に尚温ガスサイクロンを設けることにより、幾
何学的条件のため、第4図のように、灰及び粉塵を1つ
の宍送通路装置15だけで排出することができる。By providing a hot gas cyclone in the reactor, due to the geometrical conditions, the ash and dust can be discharged with only one removal channel device 15, as shown in FIG.
第1図は別個にサイクロン分屡器を設けられた直立石炭
ガス化反応器の一部を切欠いた側面図、第2図はサイク
ロンを内lする横形石炭ガス化反応器の垂1a断面図、
第3図は第2図の平面図、第4図は搬送通路装置を持つ
石炭ガス化反応器の第2図に対応する漸面図である。
l・・・石炭ガス化反応器、7・・・品温ガスサイクロ
ン、14・・・除叩空間。
IG 1
FIG 2
FIG 3Fig. 1 is a partially cutaway side view of an upright coal gasification reactor equipped with a separate cyclone separator; Fig. 2 is a vertical 1a sectional view of a horizontal coal gasification reactor containing a cyclone;
FIG. 3 is a plan view of FIG. 2, and FIG. 4 is a gradual view corresponding to FIG. 2 of a coal gasification reactor with a conveying passage device. 1... Coal gasification reactor, 7... Temperature gas cyclone, 14... Debeating space. IG 1 FIG 2 FIG 3
Claims (1)
ロン(7)が反応器内にまとめられていることを特徴と
する、炭素含有燃料のガス化用反応器。 2 高温ガスサイクロン入口(3)が、反応器(1)外
から操作可能で移動可能な閉鎖装置(10)により閉鎖
可能であることを特徴とする、特許請求の範囲第1項に
記載の反応器。 3 高温ガスサイクロン(7)の分離された粉塵の排出
装置(8)と灰の排出装置(8)とが、共通な搬送通路
装置(15)へまとめて導かれていることを特徴とする
、特許請求の範囲第1項に記載の反応器。[Scope of Claims] 1. A reactor for gasifying carbon-containing fuel, characterized in that a high-temperature gas cyclone (7) for removing dust from the gas generated in the reactor (1) is integrated in the reactor. 2. Reaction according to claim 1, characterized in that the hot gas cyclone inlet (3) is closable by a movable closing device (10) that can be operated from outside the reactor (1). vessel. 3. characterized in that the separated dust evacuation device (8) and ash evacuation device (8) of the hot gas cyclone (7) are led together into a common conveying channel device (15), A reactor according to claim 1.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19863630916 DE3630916A1 (en) | 1986-09-11 | 1986-09-11 | COAL GASIFICATION REACTOR |
DE3630916.8 | 1986-09-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6375093A true JPS6375093A (en) | 1988-04-05 |
Family
ID=6309352
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62219320A Pending JPS6375093A (en) | 1986-09-11 | 1987-09-03 | Reactor for gasifying coal |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0259577A3 (en) |
JP (1) | JPS6375093A (en) |
CN (1) | CN87106252A (en) |
BR (1) | BR8704701A (en) |
DE (1) | DE3630916A1 (en) |
PT (1) | PT85659A (en) |
ZA (1) | ZA876599B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6369144U (en) * | 1986-10-23 | 1988-05-10 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101285007B (en) * | 2008-06-06 | 2011-06-22 | 沈阳清井环保机械工程有限公司 | High-low temperature dry method ash-unloading method of coal gas |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1890070A (en) * | 1931-07-14 | 1932-12-06 | Prat Daniel Corp | Dust separator control |
DE974634C (en) * | 1951-03-03 | 1961-03-09 | Ruhrgas Ag | Process for burning glass by gasifying a fine-grain fuel |
GB687097A (en) * | 1951-11-09 | 1953-02-04 | Richard Fritz Heinrich | Improvements relating to multi-cyclone assemblies |
FR1403764A (en) * | 1964-05-12 | 1965-06-25 | Aerotec Ind | Multi-compartment centrifugal separation |
DE1271655B (en) * | 1964-07-08 | 1968-07-04 | Donald A Sillers Jun | Device for reducing the particle content of and the pulsations in a gas flow |
US4257788A (en) * | 1979-04-16 | 1981-03-24 | Nicholas Nassir | Power recovery hot gas separator |
DE2947222A1 (en) * | 1979-11-23 | 1981-05-27 | Carbon Gas Technologie GmbH, 4030 Ratingen | METHOD FOR GASIFYING SOLID, DUST-MADE TO PIECE-LIKE CARBONATED MATERIAL |
FR2530796A1 (en) * | 1982-07-21 | 1984-01-27 | Creusot Loire | THERMAL CONVERSION AND RECOVERY DEVICE |
US4588558A (en) * | 1983-09-06 | 1986-05-13 | Mobil Oil Corporation | Closed FCC cyclone system |
EP0159473A3 (en) * | 1984-02-28 | 1986-08-20 | Ruhrkohle Aktiengesellschaft | Gas-producing plant, fixed-bed pressure reactor with cyclone epuration |
-
1986
- 1986-09-11 DE DE19863630916 patent/DE3630916A1/en not_active Withdrawn
-
1987
- 1987-07-18 EP EP87110422A patent/EP0259577A3/en not_active Withdrawn
- 1987-09-03 JP JP62219320A patent/JPS6375093A/en active Pending
- 1987-09-03 ZA ZA876599A patent/ZA876599B/en unknown
- 1987-09-08 PT PT85659A patent/PT85659A/en not_active Application Discontinuation
- 1987-09-10 BR BR8704701A patent/BR8704701A/en unknown
- 1987-09-11 CN CN198787106252A patent/CN87106252A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6369144U (en) * | 1986-10-23 | 1988-05-10 |
Also Published As
Publication number | Publication date |
---|---|
CN87106252A (en) | 1988-05-11 |
PT85659A (en) | 1988-10-14 |
DE3630916A1 (en) | 1988-03-24 |
EP0259577A3 (en) | 1988-09-14 |
ZA876599B (en) | 1988-03-14 |
EP0259577A2 (en) | 1988-03-16 |
BR8704701A (en) | 1988-04-26 |
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