JPH08302365A - Gasification apparatus for coal or the like - Google Patents
Gasification apparatus for coal or the likeInfo
- Publication number
- JPH08302365A JPH08302365A JP11567495A JP11567495A JPH08302365A JP H08302365 A JPH08302365 A JP H08302365A JP 11567495 A JP11567495 A JP 11567495A JP 11567495 A JP11567495 A JP 11567495A JP H08302365 A JPH08302365 A JP H08302365A
- Authority
- JP
- Japan
- Prior art keywords
- water
- burner
- slag
- water level
- combustion chamber
- 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 claims abstract description 24
- 238000002309 gasification Methods 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 108
- 239000002893 slag Substances 0.000 claims abstract description 92
- 238000002485 combustion reaction Methods 0.000 claims abstract description 55
- 239000007858 starting material Substances 0.000 claims description 7
- 241001062472 Stokellia anisodon Species 0.000 abstract 1
- 238000000151 deposition Methods 0.000 abstract 1
- 239000000446 fuel Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000007800 oxidant agent Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008033 biological extinction Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Landscapes
- Feeding And Controlling Fuel (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、溶融スラグが燃焼室に
付着することを防止することができるようにした石炭等
のガス化装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gasifier for coal or the like which can prevent molten slag from adhering to a combustion chamber.
【0002】[0002]
【従来の技術】従来の石炭等のガス化装置を、図2に示
す。このガス化装置のガス化炉本体1は、一般的に高圧
力下で石炭をガス化するため圧力容器の中に配置されて
いる。ガス化炉本体1は、主として主燃焼をガス化する
主燃焼室2、同燃焼室2へ燃料及び空気又は酸素を含む
酸化剤を投入する1本又は数本からなる主バーナ3、主
燃焼室2の下方に連設されて主燃焼室2の起動前の加
温、加熱を行うための起動用燃焼室5、起動用燃料及び
酸化剤を起動用燃焼室5へ投入する1本又は数本からな
る起動用バーナ6、主燃焼室2と起動用燃焼室5の間に
設けられ主燃焼室2から排出される溶融スラグ(溶けた
灰分)7を落すスラグホール4、起動用燃焼室5の下方
に連設され溶融スラグ7を水砕するためのスラグホッパ
水8を溜めるスラグホッパ12、スラグホッパ水8の水
位を検知する水位検知器9、及び石炭等のガス化反応を
促進させる主燃焼室1の上方のガス化反応室11により
構成されている。2. Description of the Related Art A conventional gasifier for coal or the like is shown in FIG. The gasification furnace body 1 of this gasifier is generally arranged in a pressure vessel for gasifying coal under high pressure. The gasification furnace main body 1 mainly includes a main combustion chamber 2 that gasifies main combustion, a main burner 3 that includes one or several fuel injectors and an oxidant containing air or oxygen, and a main combustion chamber. 2 which are continuously provided below 2 to perform heating and heating of the main combustion chamber 2 before starting, and one or several of which start fuel and oxidizer are introduced into the starting combustion chamber 5. Of the starting burner 6, the slag hole 4 provided between the main combustion chamber 2 and the starting combustion chamber 5 for dropping the molten slag (molten ash) 7 discharged from the main combustion chamber 2, and the starting combustion chamber 5 The slag hopper 12, which is continuously provided below and collects the slag hopper water 8 for water granulating the molten slag 7, the water level detector 9 for detecting the water level of the slag hopper water 8, and the main combustion chamber 1 for promoting the gasification reaction of coal or the like. It is composed of the upper gasification reaction chamber 11.
【0003】前記の従来の石炭等のガス化装置は、一般
に次のようにして運転される。即ち、水を供給、排水し
つつスラグホッパ水8の水位を起動用バーナ6より下方
のある定められた水位に保つと共にガス化炉本体1内の
圧力を定められた値にしておく。The above-mentioned conventional gasifier for coal or the like is generally operated as follows. That is, while supplying and draining water, the water level of the slag hopper water 8 is maintained at a certain water level below the starting burner 6 and the pressure in the gasification furnace main body 1 is kept at a predetermined value.
【0004】その上で、起動用燃焼室5内において点火
装置等を用い起動用バーナ6を点火、燃焼させ、ガス化
炉本体1内の主燃焼室2及びガス化反応室11の温度を
上昇させる。主燃焼室2の温度が主バーナ3の着火、燃
焼に十分高温となった時点で主バーナ3を着火し、起動
用バーナ6を消火する。Then, the starter burner 6 is ignited and burned in the starter combustion chamber 5 by using an ignition device or the like to raise the temperatures of the main combustion chamber 2 and the gasification reaction chamber 11 in the gasification furnace body 1. Let When the temperature of the main combustion chamber 2 becomes sufficiently high for ignition and combustion of the main burner 3, the main burner 3 is ignited and the starting burner 6 is extinguished.
【0005】主バーナ3の燃料(主燃料)は石炭を粉砕
した微粉炭又は微粉炭をスラリー化した石炭・水スラリ
ー等であるが、油燃料を用いることもできる。主バーナ
2が着火した後、燃料と酸化剤との比率を調整し、石炭
ガス化運転に入る。The fuel (main fuel) of the main burner 3 is pulverized coal obtained by pulverizing coal, or a coal / water slurry prepared by making pulverized coal into a slurry, but an oil fuel can also be used. After the main burner 2 is ignited, the ratio of the fuel and the oxidizer is adjusted, and the coal gasification operation is started.
【0006】以上のように、主燃料が投入、燃焼される
と、燃料中の反分が溶け、溶融スラグ7となって主燃焼
室2の壁を伝ってスラグホール4からスラグホッパ水8
中へ落下する。溶融スラグ7を直接スラグホッパ水8中
に落すことにより、溶融スラグ7は自己粉砕(水砕)さ
れ、スラグホッパ12から排出し易い大きさになる。As described above, when the main fuel is charged and burned, the reciprocal component in the fuel is melted and becomes molten slag 7 that travels along the wall of the main combustion chamber 2 from the slag hole 4 to the slag hopper water 8
Fall inside. By directly dropping the molten slag 7 into the slag hopper water 8, the molten slag 7 is self-pulverized (water granulated) and is easily discharged from the slag hopper 12.
【0007】[0007]
【発明が解決しようとする課題】前記の従来の石炭等の
ガス化装置では、起動用バーナ6はある一定容積の燃焼
用空間を必要とするために、同起動用バーナ6は一般に
起動用燃焼室5の下方の部分に設置される。一方、前記
のように、スラグホッパ水8の水位は起動用バーナ6よ
り下方のある定められた水位に保たれている。従って、
スラグホール4とスラグホッパ水8の水面との間の距離
が大きくなる。In the above-mentioned conventional gasifier for coal or the like, since the starting burner 6 requires a combustion space of a certain fixed volume, the starting burner 6 is generally used for starting combustion. It is installed in the lower part of the chamber 5. On the other hand, as described above, the water level of the slag hopper water 8 is maintained at a certain water level below the starting burner 6. Therefore,
The distance between the slag hole 4 and the surface of the slag hopper water 8 increases.
【0008】このように、従来の石炭等のガス化装置で
はスラグホール4とスラグホッパ水8の水面との間の距
離が大きいために、スラグホール4から流下する溶融ス
ラグ7の一部は、スラグホッパ水8中に落下することな
く起動用燃焼室5の側壁に当って付着し、付着した溶融
スラグは次第に固化成長する。このように固化成長した
溶融スラグは徐々に温度が下るために、これがスラグホ
ッパ水8中に落下しても水砕されることがなく、例えば
400mm×800mmの大きさの大きい塊のまゝになる。As described above, in the conventional gasifier for coal or the like, since the distance between the slag hole 4 and the water surface of the slag hopper water 8 is large, a part of the molten slag 7 flowing down from the slag hole 4 is slag hopper. The molten slag that adheres to the side wall of the startup combustion chamber 5 without falling into the water 8 and adheres gradually solidifies and grows. Since the temperature of the molten slag solidified and grown gradually decreases, even if it falls into the water 8 of the slag hopper, it is not water granulated, and becomes a large lump with a size of 400 mm × 800 mm, for example. .
【0009】このような大きい溶融スラグの塊は、スラ
グホッパ12から排出することは困難でスラグホッパ1
2内に堆積して行き、数時間程度の短時間で石炭等のガ
ス化装置の運転を継続することができなくなる。It is difficult to discharge such a large lump of molten slag from the slag hopper 12, and the slag hopper 1
It becomes impossible to continue the operation of the gasifier for coal etc. within a short time of about several hours.
【0010】本発明は、以上の問題点を解決することが
できる石炭等のガス化装置を提供しようとするものであ
る。The present invention is intended to provide a gasifier for coal or the like which can solve the above problems.
【0011】[0011]
(1)本発明の石炭等のガス化装置は、主燃焼室のスラ
グホール下方に設けられ、ガス化炉運転の起動時に主燃
焼室の温度を上昇させる起動用バーナと;同起動用バー
ナの下方に水面を有するスラグホッパ水の水位を検知
し、前記起動用バーナの燃焼時にはスラグホッパ水の水
位を同起動用バーナによる燃焼領域よりも低くし、前記
起動用バーナが消火しているときにはスラグホッパ水の
水位を同起動用バーナの燃焼時よりも高くするスラグホ
ッパ水の水位を調整する手段とを備えている。(1) A gasifier for coal or the like according to the present invention is provided below a slag hole in a main combustion chamber, and a starter burner that raises the temperature of the main combustion chamber at the time of start-up of gasification furnace operation; Detects the water level of the slag hopper water having a water surface below, lowers the water level of the slag hopper water during the combustion of the startup burner than the combustion region by the startup burner, and when the startup burner is extinguished, the slag hopper water And a means for adjusting the water level of the slag hopper water, which makes the water level higher than that at the time of combustion of the startup burner.
【0012】(2)また、本発明の石炭等のガス化装置
は、前記(1)の石炭等のガス化装置において起動用バ
ーナを斜め下方に向けて設置した。(2) Further, in the gasifier for coal or the like of the present invention, in the gasifier for coal or the like in the above (1), the starting burner is installed obliquely downward.
【0013】[0013]
【作用】前記本発明(1)においては、起動用バーナが
燃焼する起動時にはスラグホッパ水の水位が起動用バー
ナによる燃焼領域より低くされて起動用バーナに必要と
する燃焼用空間が確保され、起動用バーナの燃焼が円滑
に行われる。起動用バーナの燃焼により主燃焼室の温度
が上昇し、主燃焼室内において主バーナによる燃焼が行
われるようになって起動用バーナが消火されると、スラ
グホッパ水の水位は前記起動用バーナ燃焼時の水位より
高くされ、スラグホールとスラグホッパ水の水面との間
の距離が小さくなる。従って、主燃焼室よりスラグホー
ルを経て落下する溶融スラグはすべてスラグホッパ水中
に落下して水砕され、燃焼室の側壁に付着することがな
い。In the present invention (1), at the time of start-up when the start-up burner burns, the water level of the slag hopper water is made lower than the combustion region of the start-up burner to secure the combustion space required for the start-up burner. The burner for use burns smoothly. When the temperature of the main combustion chamber rises due to the combustion of the startup burner, and the combustion by the main burner is performed in the main combustion chamber and the startup burner is extinguished, the water level of the slag hopper water becomes The water level is higher than that of the slag hole and the distance between the slag hole and the water surface of the slag hopper becomes smaller. Therefore, all the molten slag that falls from the main combustion chamber through the slag hole does not fall into the slag hopper water and are water granulated and do not adhere to the side wall of the combustion chamber.
【0014】前記本発明(2)では、前記本発明(1)
の作用に加えて、起動用バーナを斜め下方に向けて設置
することによって、起動用バーナの燃焼のためのスペー
スを確保することができる。In the invention (2), the invention (1)
In addition to the above function, the space for burning the starter burner can be secured by installing the starter burner obliquely downward.
【0015】[0015]
【実施例】本発明の実施例を、図1によって説明する。
本実施例では、スラグホール4の直下の起動用燃焼室5
の上方の部分に斜め下方に向けて1本又は数本の起動用
バーナ6が設置されている。また、給水流量計13と給
水流量調節弁14を備えたスラグホッパ12への給水管
15、及びスラグホッパ水レベル制御弁16を備えたス
ラグホッパ12からの排水管17が設けられており、ス
ラグホッパ水レベル制御弁16はスラグホッパ水8の水
位検知器9の信号によって制御されてスラグホッパ水8
の水位を制御するようになっている。EXAMPLE An example of the present invention will be described with reference to FIG.
In this embodiment, the startup combustion chamber 5 immediately below the slag hole 4
One or several starting burners 6 are installed diagonally downward in the upper part of the. Further, a water supply pipe 15 to the slag hopper 12 provided with the water supply flow meter 13 and the water supply flow rate control valve 14, and a drain pipe 17 from the slag hopper 12 provided with the slag hopper water level control valve 16 are provided. The valve 16 is controlled by the signal of the water level detector 9 of the slag hopper water 8 to
It is designed to control the water level of.
【0016】本実施例のその他の部分は図2に示される
石炭等のガス化装置とは異なるところがなく、図1にお
いて図2におけると同一の部分には同一の符号を付しそ
の説明を省略する。The other parts of this embodiment are the same as those of the gasifier for coal and the like shown in FIG. 2. The same parts as those in FIG. 2 are designated by the same reference numerals in FIG. 1 and their explanations are omitted. To do.
【0017】本実施例における起動用バーナ6によるガ
ス化装置の起動と起動後における起動用バーナ6の消火
と主バーナ3の着火は、図2に示される従来のガス化装
置におけると同様に行われる。In the present embodiment, the start-up of the gasifier by the start-up burner 6 and the extinction of the start-up burner 6 and the ignition of the main burner 3 after the start-up are performed in the same manner as in the conventional gasifier shown in FIG. Be seen.
【0018】一方、給水流量計13により給水の流量が
検出され、予め定められた流量になるように給水流量調
節弁14で制御しつつ給水管15よりスラグホッパ12
への給水を行う。また、スラグホッパ水8の水位を水位
検知器9により検出し、或る定められた水位になるよう
に、スラグホッパ水レベル制御弁16を制御してスラグ
ホッパ水8を排水管17を経てスラグホッパ12外部へ
排水する。これによって、スラグホッパ12内のスラグ
ホッパ水8の水位を調整することができる。On the other hand, the flow rate of the feed water is detected by the feed water flow meter 13, and the slag hopper 12 is fed from the feed pipe 15 while being controlled by the feed water flow control valve 14 so that the flow rate becomes a predetermined flow rate.
Supply water to. In addition, the water level of the slag hopper water 8 is detected by the water level detector 9, and the slag hopper water level control valve 16 is controlled to bring the slag hopper water 8 to the outside of the slag hopper 12 through the drain pipe 17 so that the water level becomes a predetermined water level. Drain. Thereby, the water level of the slag hopper water 8 in the slag hopper 12 can be adjusted.
【0019】本実施例では、以上のように、給水流量計
13と給水流量調節弁14を備えた給水管15、スラグ
ホッパ水レベル制御弁16を備えた排水管17及び水位
検知器9よりなるスラグホッパ水の水位を調整する手段
が設けられているので、起動用バーナ6の点火、燃焼が
行われるガス化装置の起動時には、スラグホッパ12内
のスラグホッパ水の水位が起動用バーナ6の燃焼領域よ
り低くされる。従って、起動用バーナ6に必要とする燃
焼用空間が確保され、その燃焼を円滑に行うことができ
る。In this embodiment, as described above, the water supply pipe 15 having the water supply flow meter 13 and the water supply flow rate control valve 14, the drain pipe 17 having the slag hopper water level control valve 16 and the water level detector 9 are provided. Since the means for adjusting the water level of the water is provided, the water level of the slag hopper water in the slag hopper 12 is lower than the combustion area of the start burner 6 when the gasifier which ignites and burns the start burner 6 is started. To be extinguished. Therefore, the combustion space required for the start-up burner 6 is secured, and the combustion can be performed smoothly.
【0020】また、起動用バーナ6は起動用燃焼室5の
上方の部分に斜め下方に向けて設置することによって、
起動用バーナ6の燃焼のためのスペースを確保すること
ができる。Further, the start-up burner 6 is installed in the upper portion of the start-up combustion chamber 5 so as to face obliquely downward,
A space for combustion of the start-up burner 6 can be secured.
【0021】また、起動用バーナ6が消火されて主バー
ナ3による燃焼が開始されて石炭等のガス化が行われる
ようになると、起動用燃焼室5の容積は少くてよいの
で、前記のスラグホッパ水の水位の調整をする手段によ
って、スラグホッパ水8の水位を、前記起動用バーナ6
の燃焼時の水位から上方へ、例えば起動用バーナ6の直
下まで上昇させる。このスラグホッパ水位の上昇の方法
としては、例えば、スラグホッパ水レベル制御弁16の
設定値を上げること等により容易に行うことができる。When the start-up burner 6 is extinguished and combustion by the main burner 3 is started to gasify coal or the like, the start-up combustion chamber 5 may have a small volume. Therefore, the slag hopper described above is required. By means of adjusting the water level of the water, the water level of the slag hopper water 8 is adjusted to the starting burner 6
Is raised from the water level at the time of combustion to, for example, just below the start-up burner 6. The method of raising the slag hopper water level can be easily performed by, for example, increasing the set value of the slag hopper water level control valve 16.
【0022】このようにスラグホッパ水8の水位を上昇
させることによって、スラグホール4から流下する溶融
スラグ7の飛散による起動用燃焼室5の側壁へのスラグ
付着、スラグ固化成長を防止することができる。また、
溶融スラグ7がすべてスラグホッパ水8へ落下するため
に、溶融スラグ7の自己粉砕(水砕)を確実に行うこと
ができる。By raising the water level of the slag hopper water 8 in this manner, it is possible to prevent slag from adhering to the side wall of the startup combustion chamber 5 and solidified growth of slag due to the scattering of the molten slag 7 flowing down from the slag hole 4. . Also,
Since all the molten slag 7 falls into the slag hopper water 8, the molten slag 7 can be surely self-pulverized (water granulated).
【0023】[0023]
【発明の効果】本発明は、スラグホッパ水の水位を可変
とすることによって、起動時において起動用バーナ使用
中はスラグホッパ水位を低位として燃焼用空間を得るこ
とができ、起動用バーナによる円滑な燃焼を行うことが
できる。According to the present invention, by making the water level of the slag hopper water variable, it is possible to obtain a combustion space by lowering the slag hopper water level during use of the start-up burner at the time of start-up, and smooth combustion by the start-up burner. It can be performed.
【0024】また、起動用バーナの消火後の通常運転中
は、スラグホッパ水位を上昇させることによって、スラ
グホールより落下する溶融スラグが直接スラグホッパ水
中に落下するため、燃焼室側壁に溶融スラグが付着・成
長することがなくなり、長期間運転を継続することがで
きる。Also, during normal operation after the start-up burner is extinguished, the molten slag that falls from the slag hole directly drops into the slag hopper water by raising the slag hopper water level, so the molten slag adheres to the side wall of the combustion chamber. It does not grow and can continue to operate for a long time.
【0025】一方、溶融スラグは、燃焼室の側壁に付着
することなくすべてスラグホッパ水中に落下し、自己粉
砕(水砕)されて小さくなり、後流壁機器での取扱い、
排出が容易となる。On the other hand, the molten slag falls entirely into the slag hopper water without adhering to the side wall of the combustion chamber, is self-pulverized (water granulated) and becomes small, and can be handled by downstream equipment.
Easier to discharge.
【0026】また更に、本発明では、起動用バーナを斜
め下方に向けて設置しており、同バーナの燃焼のための
スペースを確保することができる。Furthermore, in the present invention, the start-up burner is installed diagonally downward, so that a space for burning the burner can be secured.
【図1】本発明の一実施例に係る石炭等のガス化炉の説
明図である。FIG. 1 is an explanatory diagram of a gasifier for coal and the like according to an embodiment of the present invention.
【図2】従来の石炭等のガス化炉の説明図である。FIG. 2 is an explanatory diagram of a conventional gasifier for coal or the like.
1 ガス化炉本体 2 主燃焼室 3 主バーナ 4 スラグホール 5 起動用燃焼室 6 起動用バーナ 7 溶融スラグ 8 スラグホッパ水 9 水位検知器 11 ガス化反応室 12 スラグホッパ 13 給水流量計 14 給水流量調節弁 15 給水管 16 スラグホッパ水レベル制御弁 17 排水管 1 gasification furnace main body 2 main combustion chamber 3 main burner 4 slag hole 5 startup combustion chamber 6 startup burner 7 molten slag 8 slag hopper water 9 water level detector 11 gasification reaction chamber 12 slag hopper 13 feed water flow meter 14 feed water flow control valve 15 Water supply pipe 16 Slag hopper water level control valve 17 Drain pipe
Claims (2)
れ、ガス化炉運転の起動時に主燃焼室の温度を上昇させ
る起動用バーナと;同起動用バーナの下方に水面を有す
るスラグホッパ水の水位を検知し、前記起動用バーナの
燃焼時にはスラグホッパ水の水位を同起動用バーナによ
る燃焼領域よりも低くし、前記起動用バーナが消火して
いるときにはスラグホッパ水の水位を同起動用バーナの
燃焼時よりも高くするスラグホッパ水の水位を調整する
手段とを備えたことを特徴とする石炭等のガス化装置。1. A starter burner provided below the slag hole of the main combustion chamber for raising the temperature of the main combustion chamber at the time of starting the gasification furnace operation; a water level of slag hopper water having a water surface below the starter burner. When the start-up burner burns, the water level of the slag hopper water is made lower than the combustion region by the start-up burner, and when the start-up burner is extinguishing, the water level of the slag hopper water is burned at the start-up burner. And a means for adjusting the water level of the slag hopper water that is higher than the slag hopper water.
たことを特徴とする請求項1に記載の石炭等のガス化装
置。2. The gasifier for coal or the like according to claim 1, wherein the start-up burner is installed obliquely downward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11567495A JPH08302365A (en) | 1995-05-15 | 1995-05-15 | Gasification apparatus for coal or the like |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11567495A JPH08302365A (en) | 1995-05-15 | 1995-05-15 | Gasification apparatus for coal or the like |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08302365A true JPH08302365A (en) | 1996-11-19 |
Family
ID=14668488
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11567495A Pending JPH08302365A (en) | 1995-05-15 | 1995-05-15 | Gasification apparatus for coal or the like |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08302365A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101760244A (en) * | 2008-12-24 | 2010-06-30 | 山东华鲁恒升化工股份有限公司 | Three-phase multi-raw-material pressurized coal gasification device and process thereof |
| CN101760243A (en) * | 2008-12-24 | 2010-06-30 | 山东华鲁恒升化工股份有限公司 | Three-phase multi-material three-dimensional pressurized clash coal gasification device and process thereof |
| JP2011195781A (en) * | 2010-03-23 | 2011-10-06 | Babcock Hitachi Kk | Gasification furnace |
-
1995
- 1995-05-15 JP JP11567495A patent/JPH08302365A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101760244A (en) * | 2008-12-24 | 2010-06-30 | 山东华鲁恒升化工股份有限公司 | Three-phase multi-raw-material pressurized coal gasification device and process thereof |
| CN101760243A (en) * | 2008-12-24 | 2010-06-30 | 山东华鲁恒升化工股份有限公司 | Three-phase multi-material three-dimensional pressurized clash coal gasification device and process thereof |
| JP2011195781A (en) * | 2010-03-23 | 2011-10-06 | Babcock Hitachi Kk | Gasification furnace |
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