JPS61228093A - Fuel gasification apparatus - Google Patents
Fuel gasification apparatusInfo
- Publication number
- JPS61228093A JPS61228093A JP6666085A JP6666085A JPS61228093A JP S61228093 A JPS61228093 A JP S61228093A JP 6666085 A JP6666085 A JP 6666085A JP 6666085 A JP6666085 A JP 6666085A JP S61228093 A JPS61228093 A JP S61228093A
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- diffuser
- combustor
- section
- coal
- 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
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野〕
本発明は燃料のガス化装置に関し、特に石炭、COM(
石炭−油混合物)、CWM(石炭−水混合物)、石油コ
ークス、重質油など各種燃料を同時に利用できるガス化
装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a fuel gasifier, particularly coal, COM (
The present invention relates to a gasification device that can simultaneously use various fuels such as coal-oil mixture), CWM (coal-water mixture), petroleum coke, and heavy oil.
(従来の技術)
従来のガス化装置は、燃料ごとに区別されておシ、微粉
炭、石油コークス、重質油などを同時に利用できるもの
ではなかった。また石炭に関しても、微粉炭供給式ある
いは水スラリ供給方式の二者択一であり、両者を同時に
使用しうるようにされているものは存在しなかった。(Prior Art) Conventional gasifiers have not been able to use different fuels such as coal, pulverized coal, petroleum coke, and heavy oil at the same time. Regarding coal, there are two options: a pulverized coal supply system or a water slurry supply system, and there is no system that allows both to be used at the same time.
(発明が解決しようとする問題点)
本発明は、多炭種に対応でき石炭供給方式に融通性をも
たせ、微粉炭でもスラリーでも同時にガス化でき、更に
石炭、COM、CWM、石油コークス、重質油など如何
なる燃料でも使用することができるガス化装置を提供し
ようとするものである。(Problems to be Solved by the Invention) The present invention can accommodate multiple coal types, provides flexibility in coal supply methods, and can simultaneously gasify both pulverized coal and slurry. The present invention aims to provide a gasification device that can use any fuel such as quality oil.
(問題点を解決するための手段)
すなわち、本発明は燃料を燃焼させて高温の雰囲気を形
成するうコンバスタ部、同コンバスタ部の上部に位置し
てコンバスタ部と連通し、燃料を乾留・熱分解させると
共に前記コンバスタ部からの高温のガスと燃料とを混合
するディフューザ部、及び同ディフューザ部の上部に位
置してディフューザ部と連通し、吸熱のガス化反応を行
わせて前記ディフューザ部かラノ炭素粒をガス化させる
レダクタ部からガス他炉カ構成され、前記コンバスタ部
とディフューザ部に微粉炭、スラリー燃料、及び重油を
夫々単独に供給するノズル部を設けたことを特徴とする
燃料ガス化装置である。(Means for Solving the Problems) That is, the present invention includes a combustor section that burns fuel to form a high-temperature atmosphere, and a combustor section that is located above the combustor section and communicates with the combustor section to carbonize and heat the fuel. A diffuser section that decomposes the fuel and mixes the high-temperature gas from the combustor section with the fuel, and a diffuser section that is located above the diffuser section and communicates with the diffuser section to perform an endothermic gasification reaction so that the diffuser section and the fuel are mixed together. A fuel gasification system comprising a gas furnace including a reductor section for gasifying carbon particles, and a nozzle section for individually supplying pulverized coal, slurry fuel, and heavy oil to the combustor section and the diffuser section. It is a device.
以下、本発明の燃料ガス化装置の一実施態様を第1図に
従って詳述する。Hereinafter, one embodiment of the fuel gasification apparatus of the present invention will be described in detail with reference to FIG.
圧力容器1内に、全体を比較的薄い水冷壁2で囲まれ、
燃料を燃焼させて高温の雰囲気を形成スルコンバスタ3
、このコンバスタ3の上部に位置してコンバスタ3と連
通し燃料を乾留・熱分解させると共に前記コンバスタ3
からの高温ガスと燃料とを混合するディフューザ4、及
びこのディフューザ4の上部に位置してディフューザ4
と連通し吸熱のガス化反応を行わせて前記ディフューザ
4からの炭素粒をガス化させるレダクタ5からなるガス
化炉6が挿入されている。ガス他炉6内上部には熱交換
器群7が内股され、ガス化炉6の下部には灰ホッパ8が
設けられている。Inside the pressure vessel 1, the whole is surrounded by a relatively thin water-cooled wall 2,
Surcon buster 3 burns fuel to create a high-temperature atmosphere
, is located on the upper part of the combustor 3 and communicates with the combustor 3 to carbonize and thermally decompose the fuel.
a diffuser 4 for mixing high-temperature gas from the fuel with the fuel; and a diffuser 4 located above the diffuser 4.
A gasifier 6 comprising a reductor 5 is inserted, which communicates with the diffuser 4 to perform an endothermic gasification reaction to gasify the carbon particles from the diffuser 4. A heat exchanger group 7 is installed in the upper part of the gasification furnace 6, and an ash hopper 8 is provided in the lower part of the gasification furnace 6.
ガス化炉6から発生したガスは熱交換器群7と熱交換し
て、脱硫処理工程9、脱硫処理工程10を経てガスター
ビン11に供給され、コンバスタ3よシ排出される灰は
灰ホッパ8を経て水冷され、水冷スラグ12として系外
に排出される。The gas generated from the gasifier 6 exchanges heat with the heat exchanger group 7 and is supplied to the gas turbine 11 through the desulfurization treatment process 9 and the desulfurization treatment process 10, and the ash discharged from the combustor 3 is sent to the ash hopper 8. The slag is then water-cooled and discharged from the system as water-cooled slag 12.
ガス化炉6は、上述したように、コンバスタ3、ディフ
ューザ4、レダクタ5より構成され、燃料は一部はコン
バスタ3に投入され、残シはディフューザ4に投入され
る2段噴流床方式である。As mentioned above, the gasifier 6 is composed of a combustor 3, a diffuser 4, and a reductor 5, and is of a two-stage spouted bed type in which a part of the fuel is input into the combustor 3 and the rest is input into the diffuser 4. .
同系省略しであるが、圧力容器1とガス化炉6の間の空
間には、発生ガスを精製した精製ガスが注入され、この
間の空間の圧力を制御しうるようにするのが好ましい。Although the same system is omitted, it is preferable that purified gas obtained by refining generated gas is injected into the space between the pressure vessel 1 and the gasifier 6, so that the pressure in the space between them can be controlled.
燃料は、前述の通り一部はコンバスタ5、一部はディフ
ューザ4に供給されるが、燃料の供給系統として、大別
して微粉炭供給系13、石炭−水スラ!J(CWM)供
給系14及び重質油供給系15を単独あるいは組合せて
装備する。As mentioned above, some of the fuel is supplied to the combustor 5 and some to the diffuser 4, but the fuel supply systems can be roughly divided into the pulverized coal supply system 13, the coal-water slurry! A J (CWM) supply system 14 and a heavy oil supply system 15 are provided singly or in combination.
また燃料のガス化剤は空気16を主とするが、燃料の多
種化に対応してバックアップのために酸素17を空気に
富化させるように設計され、ガス化剤はガスタービンコ
ンプレッサ、ブースタコンプレッサ18を介してコンバ
スタ3に供給されるようになっている。In addition, the gasification agent for fuel is mainly air 16, but in response to the diversification of fuels, it is designed to enrich air with oxygen 17 for backup.The gasification agent is used for gas turbine compressors, booster compressors It is supplied to the combustor 3 via 18.
微粉炭供給系13は、例えば下記のように構成させるの
がよい。The pulverized coal supply system 13 is preferably configured as follows, for example.
石炭19又は石油コークス2.0はミA/21で粉砕乾
燥され、サイクロン22、バグフィルタ23、石炭ビン
24、石炭ロックホッパ群25ヲ経て、コンバスタ3及
びディフューザ4に供給する。供給ノズルは複数本設置
し、負荷に応じて本数制御を行いうるようにしておくの
がよい。なお図中26はキャリアガスの排気を示す。Coal 19 or petroleum coke 2.0 is pulverized and dried in Mi A/21, and is supplied to combustor 3 and diffuser 4 through cyclone 22, bag filter 23, coal bin 24, and coal lock hopper group 25. It is preferable to install a plurality of supply nozzles so that the number can be controlled according to the load. Note that 26 in the figure indicates exhaust of the carrier gas.
石炭−水スラリ供給系14は、例えば下記のように構成
させるのがよい。The coal-water slurry supply system 14 is preferably configured as follows, for example.
石炭27及び水28が同時に湿式ミ/I/29に注入さ
れ、スラリ化され、スフリボンプ30で、コンバスタ3
及びディフューザ4に供給される。Coal 27 and water 28 are simultaneously injected into the wet mixer/I/29, slurried, and sent to the combustor 3 in the souffle bump 30.
and is supplied to the diffuser 4.
この供給ノズルも負荷に応じて制御できるように複数本
設けておくのがよい。It is preferable to provide a plurality of supply nozzles so that they can be controlled according to the load.
重質油供給系15は、ターμ、ピッチ、アスファμトな
どの重質油を加熱してパーナノズμヨシ、コンバスタ3
及びディフューザ4に供給するようにされる。The heavy oil supply system 15 heats heavy oil such as tar, pitch, asphalt, etc.
and is supplied to the diffuser 4.
本発明の燃料ガス化装置の一実施態様について述べたが
、本発明の燃料ガス化装置は、各種燃料供給設備を備え
ているので、多炭種対応のみならず、各種燃料の併用が
可能であシ、燃料事情に対応して微粉炭単独使用は勿論
、スラリ供給方式も可能であり、また同時に重質油のガ
ス化も行うことが可能であるという効果を奏しうる。Although one embodiment of the fuel gasification device of the present invention has been described, since the fuel gasification device of the present invention is equipped with various fuel supply equipment, it is not only compatible with multiple coal types, but can also be used in combination with various fuels. Depending on the fuel situation, it is possible to use not only pulverized coal alone but also a slurry supply system, and it is also possible to gasify heavy oil at the same time.
また上記実施態様において説明したように、ガス化剤で
ある空気の酸素を富化するようにしておけば、燃料に応
じて酸素を富化させて必要なガス化を行わせることが可
能となると共に、高いカロリーのガスを得ることが可能
であるという効果を奏しうる。Furthermore, as explained in the above embodiment, if the air, which is a gasifying agent, is enriched with oxygen, it becomes possible to enrich oxygen and perform the necessary gasification depending on the fuel. At the same time, it is possible to obtain high calorie gas.
第1図は、本発明の燃料ガス化装置の一実施態様を示す
図である。
復代理人 内 1) 明
復代理人 萩 原 亮 −FIG. 1 is a diagram showing one embodiment of the fuel gasification apparatus of the present invention. Sub-agents 1) Meifuku agent Ryo Hagiwara -
Claims (1)
部、同コンバスタ部の上部に位置してコンバスタ部と連
通し、燃料を乾留・熱分解させると共に前記コンバスタ
部からの高温のガスと燃料とを混合するディフューザ部
、及び同ディフューザ部の上部に位置してディフューザ
部と連通し、吸熱のガス化反応を行わせて前記ディフュ
ーザ部からの炭素粒をガス化させるレダクタ部からガス
化炉が構成され、前記コンバスタ部とディフューザ部に
微粉炭、スラリー燃料、及び重油を夫々単独に供給する
ノズルを設けたことを特徴とする燃料ガス化装置。A combustor section that burns fuel to form a high-temperature atmosphere; a combustor section located above the combustor section that communicates with the combustor section, carbonizes and thermally decomposes the fuel, and mixes the high-temperature gas from the combustor section with the fuel; A gasifier includes a diffuser section for mixing, and a reductor section located above the diffuser section and communicating with the diffuser section to perform an endothermic gasification reaction to gasify carbon particles from the diffuser section. . A fuel gasification device, characterized in that the combustor section and the diffuser section are provided with nozzles that individually supply pulverized coal, slurry fuel, and heavy oil, respectively.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6666085A JPS61228093A (en) | 1985-04-01 | 1985-04-01 | Fuel gasification apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6666085A JPS61228093A (en) | 1985-04-01 | 1985-04-01 | Fuel gasification apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61228093A true JPS61228093A (en) | 1986-10-11 |
Family
ID=13322276
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6666085A Pending JPS61228093A (en) | 1985-04-01 | 1985-04-01 | Fuel gasification apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61228093A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61233081A (en) * | 1985-04-09 | 1986-10-17 | Mitsubishi Heavy Ind Ltd | Coal gasifying device of pressure jet bed type |
WO1997044412A1 (en) * | 1996-05-20 | 1997-11-27 | Hitachi, Ltd. | Coal gasification apparatus, coal gasification method and integrated coal gasification combined cycle power generating system |
JP2014527552A (en) * | 2011-07-27 | 2014-10-16 | サウジ アラビアン オイル カンパニー | Gasification process of heavy residual oil using particulate coke from delayed coking unit |
KR20180117691A (en) * | 2016-03-04 | 2018-10-29 | 루머스 테크놀로지 엘엘씨 | Two-stage gasification equipment and feedstock Gasification process with flexibility |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3018174A (en) * | 1958-07-21 | 1962-01-23 | Babcock & Wilcox Co | High pressure pulverized coal gasifier |
JPS5432508A (en) * | 1977-08-18 | 1979-03-09 | Combustion Eng | Operation of coal gasification plant |
JPS5647489A (en) * | 1979-09-28 | 1981-04-30 | Freiberg Brennstoffinst | Reactor for gas manufacture by partial oxidation |
JPS5849790A (en) * | 1981-09-19 | 1983-03-24 | Kawasaki Heavy Ind Ltd | Gasification of coal |
JPS58154797A (en) * | 1982-03-10 | 1983-09-14 | Babcock Hitachi Kk | Starting spouted-bed coal gasifier |
JPS58194986A (en) * | 1982-05-10 | 1983-11-14 | Mitsubishi Heavy Ind Ltd | Multi-stage spouted bed gasification furnace |
-
1985
- 1985-04-01 JP JP6666085A patent/JPS61228093A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3018174A (en) * | 1958-07-21 | 1962-01-23 | Babcock & Wilcox Co | High pressure pulverized coal gasifier |
JPS5432508A (en) * | 1977-08-18 | 1979-03-09 | Combustion Eng | Operation of coal gasification plant |
JPS5647489A (en) * | 1979-09-28 | 1981-04-30 | Freiberg Brennstoffinst | Reactor for gas manufacture by partial oxidation |
JPS5849790A (en) * | 1981-09-19 | 1983-03-24 | Kawasaki Heavy Ind Ltd | Gasification of coal |
JPS58154797A (en) * | 1982-03-10 | 1983-09-14 | Babcock Hitachi Kk | Starting spouted-bed coal gasifier |
JPS58194986A (en) * | 1982-05-10 | 1983-11-14 | Mitsubishi Heavy Ind Ltd | Multi-stage spouted bed gasification furnace |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61233081A (en) * | 1985-04-09 | 1986-10-17 | Mitsubishi Heavy Ind Ltd | Coal gasifying device of pressure jet bed type |
WO1997044412A1 (en) * | 1996-05-20 | 1997-11-27 | Hitachi, Ltd. | Coal gasification apparatus, coal gasification method and integrated coal gasification combined cycle power generating system |
JP2014527552A (en) * | 2011-07-27 | 2014-10-16 | サウジ アラビアン オイル カンパニー | Gasification process of heavy residual oil using particulate coke from delayed coking unit |
KR20180117691A (en) * | 2016-03-04 | 2018-10-29 | 루머스 테크놀로지 엘엘씨 | Two-stage gasification equipment and feedstock Gasification process with flexibility |
CN109072103A (en) * | 2016-03-04 | 2018-12-21 | 鲁姆斯科技有限责任公司 | Two-stage gasifier and gasification process with feed flexibility |
US11084996B2 (en) | 2016-03-04 | 2021-08-10 | Lummus Technology Llc | Two-stage gasifier and gasification process with feedstock flexibility |
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