JP3750881B2 - Ash melting furnace - Google Patents

Ash melting furnace Download PDF

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Publication number
JP3750881B2
JP3750881B2 JP15117096A JP15117096A JP3750881B2 JP 3750881 B2 JP3750881 B2 JP 3750881B2 JP 15117096 A JP15117096 A JP 15117096A JP 15117096 A JP15117096 A JP 15117096A JP 3750881 B2 JP3750881 B2 JP 3750881B2
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Japan
Prior art keywords
furnace
melting furnace
ash melting
ash
water
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JP15117096A
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Japanese (ja)
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JPH102539A (en
Inventor
英樹 岩田
俊行 鈴木
直明 安田
賢一 田原
順也 西野
啓二 角田
典房 林
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石川島播磨重工業株式会社
株式会社石川島岩国製作所
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  • Processing Of Solid Wastes (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、都市ごみ焼却炉や各種焼却装置等から排出される焼却灰などを溶融処理する灰溶融炉に関するものである。
【0002】
【従来の技術】
都市ごみ、下水汚泥等の各廃棄物は、焼却施設で焼却処理され、生じた焼却灰やばいじんは、従来埋め立て処分されていた。しかし、埋立処分地枯渇の問題や有害重金属類の溶出による地下水汚染の問題があるため、溶融による減量・減容化と無害化の必要性が高まっている。
【0003】
このような背景で、焼却灰中の残留炭素、コークス、灯油および電力を熱源とした、焼却炉等から排出される焼却灰などを溶融処理する灰溶融炉が提案され、一部で実処理が行われている。
【0004】
このうち、電力を熱源とした灰溶融炉には、プラズマアーク加熱方式や抵抗加熱方式などがある。
【0005】
抵抗加熱方式の灰溶融炉は、溶融スラグ内に対抗電極を配置し、直流または交流通電による電気抵抗熱(ジュール熱)により焼却灰を加熱溶融するものであり、▲1▼熱効率が高い、▲2▼発生ガスが少ない、▲3▼アークを生成しないためフリッカが発生しない、▲4▼溶融スラグと溶融メタルとを分離した分割出滓ができる、という特徴がある。
【0006】
図2は従来の抵抗加熱方式の灰溶融炉の縦断面図である。図において、aは灰溶融炉である。この灰溶融炉aの炉壁bは、全体に内部に水冷管dを埋設した耐火レンガ等の耐火材による水冷ジャケットcを有して形成されている。eは灰溶融炉aの頂部に設けた炉蓋である。焼却灰mは、この灰溶融炉aの炉蓋eに設けた灰投入管jから投入される。灰溶融炉a内に投入された焼却灰mは、灰溶融炉aの炉蓋eに挿入した上部電極hおよび灰溶融炉aの炉底に埋設した炉底電極iにより加熱して溶融スラグnにするようにしている。灰溶融炉a内に溶融スラグnが所要量溜まると、溶融スラグnを自重によって加わるヘッド圧により灰溶融炉aの炉壁b下部に設けた出滓口fを通して外部に出滓するようになっている。kは灰溶融炉aの炉蓋eに設けた排気管である。oは灰溶融炉a内底部に溜まった溶融メタルで、溶融スラグnと同様に所要量溜まると、排出口gを通して外部に排出するようになっている。pは上部電極hおよび底部電極iに直流通電する電源であり、qおよびrはその電線である。なお、この従来例の他に、出滓口fを灰溶融炉aの炉壁bの高さ方向の中央部に設けて溶融スラグnを連続的にオーバーフローさせて出滓させるものもある。
【0007】
灰溶融炉aの炉壁bおよび炉蓋eには、一般に気孔率20%〜30%の高アルミナ質の耐火材が使用される。
【0008】
【発明が解決しようとする課題】
しかしながら、図2に示すような灰溶融炉では、灰溶融炉の炉壁を、内部に水冷管を埋設した水冷ジャケットを有する炉壁で形成しているため、炉壁の耐火材が灰溶融炉内の高温の溶融スラグにより損耗し、放置しておくと水冷管を破損する恐れがあるなどの問題がある。
【0009】
本発明は、上記のような問題点を解決するために創案されたもので、水冷ジャケットを設けることなく、耐火材の寿命を長くするような灰溶融炉を提供することを目的とするものである。
【0010】
【課題を解決するための手段】
上記目的を達成するため、本発明によれば、焼却灰を溶融処理する灰溶融炉であって、該灰溶融炉の炉壁の外面の鉄皮を、散水により冷却するようにし、灰溶融炉の底部を、空冷により冷却するようにし、灰溶融炉の底部を空冷した空気を、炉壁外面の鉄皮の散水面に沿って通風するようにした、ことを特徴とする灰溶融炉が提供される。
【0013】
さらに、散水後の水を、灰溶融炉の底部に張り出して設けた受け皿で受けて循環させながら散水するようにするのが好ましい。
【0014】
上記本発明の構成によれば、炉壁の外面の鉄皮に散水し、その蒸発により炉壁を冷却するようにしたので、炉壁の冷却効率を高めることができ、したがって、耐火材の寿命を長くすることができる。蒸発潜熱による冷却なので冷却水管も少なくてすむ。また、灰溶融炉の底部を、空冷により冷却するようにしたので、灰溶融炉底部の炉壁の冷却効率を高めることができるとともに、空冷した後の温められた空気が炉壁に沿って上昇する際、水の蒸発作用を高めるので、冷却効率を一層高めることができる。
【0015】
また、散水後の水を、灰溶融炉の底部に張り出して設けた受け皿で受けて循環させながら散水するようにしたので、冷却水の無駄をなくすことができる。
【0016】
【発明の実施の形態】
以下、本発明の好ましい実施の形態を図面に基づいて説明する。
図1は、本発明の一実施形態を示すものであり、図1は本発明による灰溶融炉の冷却装置の縦断面図である。
図において、1は焼却灰を溶融処理する灰溶融炉である。2はこの灰溶融炉1の炉壁で、全体に耐火レンガにより形成されるとともに、外周面は鉄皮3で形成されている。4は灰溶融炉1の頂部に設けた炉蓋である。5はこの炉蓋4に設けた電極挿入口に挿入した上部電極であり、5aは灰溶融炉1の底部2aに、上部電極5と対峙するように埋設した炉底電極である。6は炉蓋4に設けられた焼却灰投入管で、7はその投入口である。8は焼却灰投入管6と同様に炉蓋4に設けられた排気管で、9はその排出口である。10は灰溶融炉1内に焼却灰投入管6を通して投入された焼却灰で、上部電極5および炉底電極5aに、電源から直流通電することにより加熱溶解して溶融スラグ11と溶融メタル12とに分離し、溶融スラグ11は、灰溶融炉1の下方部に設けられた、出滓口から出滓される。また、溶融スラグ11と分離して灰溶融炉1底部に溜まった溶融メタル12は固まっており、電極5との間でアークを発生させてメタルを溶融してから、排出口を通して外部に排出される。なお、前記溶融スラグ11の出滓口、溶融メタル12の排出口,上部電極5および炉底電極5aに通電する電源は、いずれも図示していないが、従来のものの構造と実質的に同じである。
【0017】
13は冷却水槽で、貯水槽25から給水ポンプ26により給水管27を通して送給された散水用水17を貯水しておき、焼却灰10を溶解する際、炉壁2の鉄皮3の外周面に向けて散水する。16は炉壁2の鉄皮3の外周面に沿って上下に多段に配設された複数本の環状の散水管であり、この散水管には炉壁2の鉄皮3に向かって散水するように多数の散水孔16aが設けられている。なお、この散水孔16の向きを替えることにより、散水角度を任意に変更することができる。14は上端を冷却水槽13に連結した給水管で、下端は分岐して各環状の散水管16にそれぞれ連結している。そして、冷却水17をポンプ15により環状の散水管16に給水する。18は灰溶融炉1の底部2aに張り出して設けられた水受け皿で、散水された水17を受け、この水受け皿18に一端を連結した排水管19を通して貯水槽25に戻すようにしている。
【0018】
20は灰溶融炉1の底部2aおよび炉壁2を囲繞するように設けた囲壁である。22は上端をこの囲壁20の底部に連結し、下端を空冷ファン21に連結した送風管で、焼却灰10を溶解する際、空冷ファン21によって冷却空気を灰溶融炉1の底部2aに向けて送風するとともに、灰溶融炉1の底部2aに吹きつけた空気を、炉壁2の鉄皮3と囲壁20との間隙を炉壁2に沿って上昇させ、排気管23を通して排出するようになっている。このようにして、空冷した後の温められた空気が炉壁2に沿って上昇する際、水の蒸発作用を高める。24は排気管23の立ち上り部に下方に突出するように設けたドレン受け部であり、このドレン受け部24で受けたドレンは、ドレン管19aにより貯水槽25に戻されるようになっている。
【0019】
次に実施の形態に基づく作用について説明する。
灰溶融炉1内に投入された焼却灰10を、電源から上部電極5および炉底電極5aに直流通電し、加熱して溶融スラグ11を生成する。焼却灰11は、灰溶融炉1内では1,200°Cで溶融するが、灰溶融炉1内での溶融スラグ11の最適温度は、1,200°〜1,300°Cと高温であり、焼却灰10に含まれている塩類も蒸発して炉壁2の耐火材に付着し、耐火材に浸透して耐火材を損耗するが、炉壁2の鉄皮3の外周面に向けて冷却水17を散水し、炉壁2を冷却するので、炉壁2の耐火材の損耗を少なくすることができ、耐火材の寿命を長くすることができる。また、冷却水の蒸発による冷却なので、冷却水の使用量が少なくてすむ。底部を空冷することにより、炉の耐久性を高めることができる。水を循環使用することにより、さらに冷却水の使用量を減らすことができる。
【0020】
本発明は、上記実施の形態に限定されるものではなく、本発明の要旨を逸脱しない範囲で種々変更し得ることは勿論である。
【0021】
【発明の効果】
以上述べたように、本発明によれば、溶融炉内に投入された焼却灰を溶融する際、炉壁の鉄皮の外周面に冷却水を散水して冷却し、耐火材の溶損を防止しているので、耐火材の寿命を長くすることができるなどの優れた効果を奏する。
【図面の簡単な説明】
【図1】本発明による灰溶融炉の縦断面図である。
【図2】従来の灰溶融炉の縦断面図である。
【符号の説明】
1 灰溶融炉
2 炉壁
2a 炉底部
3 鉄皮
4 炉蓋
5 上部電極
5a 炉底電極
6 焼却灰投入管
7 焼却灰投入口
8 排気管
9 排気口
10 焼却灰
11 溶融スラグ
12 溶融メタル
13 冷却水槽
14,27 給水管
15,26 給水ポンプ
16 環状の散水管
16a 散水孔
17 冷却水
18 水受け皿
19,19a 排水管
20 囲壁
21 空冷ファン
22 送風管
23 排気管
24 ドレン受け部
25 貯水槽
a 灰溶融炉
b 炉壁
c 水冷ジャケット
d 水冷管
e 炉蓋
f 出滓口
g 排出口
h 上部電極
i 炉底電極
j 焼却灰投入管
k 排気管
m 焼却灰
n 溶融スラグ
o 溶融メタル
p 電源
q,r 電線
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an ash melting furnace for melting incineration ash discharged from municipal waste incinerators and various incinerators.
[0002]
[Prior art]
Municipal waste, sewage sludge, and other wastes were incinerated at incineration facilities, and the resulting incinerated ash and dust were conventionally disposed of in landfills. However, there is a problem of depletion of landfill sites and groundwater contamination due to the elution of toxic heavy metals, so the need for weight reduction / volume reduction and detoxification by melting is increasing.
[0003]
Against this background, ash melting furnaces have been proposed for melting incineration ash discharged from incinerators, etc., using residual carbon, coke, kerosene, and electric power in the incineration ash as heat sources. Has been done.
[0004]
Among these, an ash melting furnace using electric power as a heat source includes a plasma arc heating method and a resistance heating method.
[0005]
The resistance heating type ash melting furnace has a counter electrode in the molten slag, and heats and melts the incinerated ash by electric resistance heat (Joule heat) by direct current or alternating current. (1) High thermal efficiency, (2) Less gas is generated, (3) Flicker is not generated because no arc is generated, and (4) Divided slag separated from molten slag and molten metal can be obtained.
[0006]
FIG. 2 is a longitudinal sectional view of a conventional resistance heating type ash melting furnace. In the figure, a is an ash melting furnace. The furnace wall b of the ash melting furnace a is formed with a water cooling jacket c made of a refractory material such as a refractory brick having a water cooling pipe d embedded therein. e is a furnace lid provided at the top of the ash melting furnace a. The incinerated ash m is charged from an ash charging pipe j provided on a furnace lid e of the ash melting furnace a. The incinerated ash m charged into the ash melting furnace a is heated by the upper electrode h inserted in the furnace lid e of the ash melting furnace a and the furnace bottom electrode i embedded in the furnace bottom of the ash melting furnace a to produce molten slag n. I try to make it. When a required amount of molten slag n is accumulated in the ash melting furnace a, the molten slag n comes out to the outside through the outlet f provided at the lower part of the furnace wall b of the ash melting furnace a by the head pressure applied by its own weight. ing. k is an exhaust pipe provided in the furnace lid e of the ash melting furnace a. o is a molten metal collected at the bottom of the ash melting furnace a, and when a required amount is accumulated like the molten slag n, it is discharged to the outside through the discharge port g. p is a power source for direct current to the upper electrode h and the bottom electrode i, and q and r are electric wires thereof. In addition to this conventional example, there is also a type in which a tap outlet f is provided at the center in the height direction of the furnace wall b of the ash melting furnace a to continuously overflow the molten slag n.
[0007]
A high alumina refractory material having a porosity of 20% to 30% is generally used for the furnace wall b and the furnace lid e of the ash melting furnace a.
[0008]
[Problems to be solved by the invention]
However, in the ash melting furnace as shown in FIG. 2, the furnace wall of the ash melting furnace is formed with a furnace wall having a water cooling jacket with a water cooling pipe embedded therein, so that the refractory material on the furnace wall is the ash melting furnace. There is a problem that the water-cooled tube may be damaged if it is worn away by the high-temperature molten slag inside and left to stand.
[0009]
The present invention was devised to solve the above-described problems, and an object thereof is to provide an ash melting furnace that extends the life of a refractory material without providing a water cooling jacket. is there.
[0010]
[Means for Solving the Problems]
In order to achieve the above object, according to the present invention, an ash melting furnace for melting incinerated ash, wherein the outer skin of the furnace wall of the ash melting furnace is cooled by watering , the bottom of the furnace, so as to cool the air, the air that has cooled the bottom of the ash melting furnace so as to air along the nozzle face of the steel shell of the furnace wall outer surface, ash melting furnace, characterized in that it Provided.
[0013]
Further, it is preferable that the water after sprinkling is sprinkled while being received and circulated by a tray provided overhanging at the bottom of the ash melting furnace.
[0014]
According to the configuration of the present invention, water is sprinkled on the outer skin of the furnace wall, and the furnace wall is cooled by evaporation, so that the cooling efficiency of the furnace wall can be increased, and therefore the life of the refractory material Can be lengthened. Cooling by latent heat of vaporization requires less cooling water pipes. In addition, since the bottom of the ash melting furnace is cooled by air cooling, the cooling efficiency of the furnace wall at the bottom of the ash melting furnace can be improved, and warmed air after air cooling rises along the furnace wall In doing so, the evaporation effect of water is enhanced, so that the cooling efficiency can be further enhanced.
[0015]
Further, since the water after sprinkling is received and circulated by a receiving tray provided overhanging at the bottom of the ash melting furnace, it is possible to eliminate the waste of cooling water.
[0016]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows one embodiment of the present invention, and FIG. 1 is a longitudinal sectional view of a cooling device for an ash melting furnace according to the present invention.
In the figure, 1 is an ash melting furnace for melting incinerated ash. Reference numeral 2 denotes a furnace wall of the ash melting furnace 1, which is formed entirely of refractory bricks and whose outer peripheral surface is formed of an iron skin 3. 4 is a furnace lid provided at the top of the ash melting furnace 1. Reference numeral 5 denotes an upper electrode inserted into an electrode insertion opening provided in the furnace lid 4, and reference numeral 5 a denotes a furnace bottom electrode embedded in the bottom 2 a of the ash melting furnace 1 so as to face the upper electrode 5. 6 is an incineration ash charging pipe provided on the furnace lid 4, and 7 is the charging port. 8 is an exhaust pipe provided in the furnace lid 4 in the same manner as the incineration ash charging pipe 6, and 9 is a discharge port thereof. Reference numeral 10 denotes incineration ash introduced into the ash melting furnace 1 through the incineration ash injection pipe 6. The upper electrode 5 and the furnace bottom electrode 5 a are heated and melted by applying a direct current from a power source to melt the slag 11 and the molten metal 12. The molten slag 11 is fed out from a tap outlet provided in the lower part of the ash melting furnace 1. Further, the molten metal 12 separated from the molten slag 11 and collected at the bottom of the ash melting furnace 1 is solidified, and an arc is generated between the electrodes 5 to melt the metal and then discharged to the outside through the discharge port. The Note that the power supply for energizing the outlet of the molten slag 11, the outlet of the molten metal 12, the upper electrode 5 and the furnace bottom electrode 5 a are not shown, but are substantially the same as the conventional structure. is there.
[0017]
Reference numeral 13 denotes a cooling water tank, which stores water for spraying 17 fed from a water storage tank 25 through a water supply pipe 27 by a water supply pump 26 and melts the incinerated ash 10 on the outer peripheral surface of the iron skin 3 of the furnace wall 2. Sprinkle water. Reference numeral 16 denotes a plurality of annular sprinkling pipes arranged in multiple stages vertically along the outer peripheral surface of the iron skin 3 of the furnace wall 2, and water sprays toward the iron skin 3 of the furnace wall 2 in this watering pipe. Thus, a large number of water spray holes 16a are provided. In addition, the watering angle can be arbitrarily changed by changing the direction of the watering hole 16. Reference numeral 14 denotes a water supply pipe whose upper end is connected to the cooling water tank 13, and the lower end is branched to be connected to each annular sprinkling pipe 16. Then, the cooling water 17 is supplied to the annular sprinkling pipe 16 by the pump 15. Reference numeral 18 denotes a water receiving tray provided overhanging the bottom 2 a of the ash melting furnace 1. The water receiving tray 17 receives the sprinkled water 17 and returns it to the water storage tank 25 through a drain pipe 19 having one end connected to the water receiving tray 18.
[0018]
Reference numeral 20 denotes a surrounding wall provided so as to surround the bottom portion 2 a of the ash melting furnace 1 and the furnace wall 2. Reference numeral 22 denotes a blower pipe having an upper end connected to the bottom of the surrounding wall 20 and a lower end connected to an air cooling fan 21. When the incinerated ash 10 is melted, the cooling air is directed toward the bottom 2 a of the ash melting furnace 1 by the air cooling fan 21. While blowing, the air blown to the bottom 2a of the ash melting furnace 1 is raised along the furnace wall 2 along the furnace wall 2 of the furnace wall 2 and discharged through the exhaust pipe 23. ing. In this way, when the warmed air after air cooling rises along the furnace wall 2, the water evaporation action is enhanced. A drain receiving portion 24 is provided so as to protrude downward at the rising portion of the exhaust pipe 23. The drain received by the drain receiving portion 24 is returned to the water storage tank 25 by the drain pipe 19a.
[0019]
Next, the operation based on the embodiment will be described.
The incinerated ash 10 charged into the ash melting furnace 1 is supplied with direct current from the power source to the upper electrode 5 and the furnace bottom electrode 5a and heated to generate molten slag 11. The incinerated ash 11 melts at 1,200 ° C. in the ash melting furnace 1, but the optimum temperature of the molten slag 11 in the ash melting furnace 1 is as high as 1,200 ° to 1,300 ° C. The salt contained in the incineration ash 10 also evaporates and adheres to the refractory material of the furnace wall 2, penetrates into the refractory material and wears out the refractory material, but toward the outer peripheral surface of the iron skin 3 of the furnace wall 2. Since the cooling water 17 is sprinkled and the furnace wall 2 is cooled, the wear of the refractory material on the furnace wall 2 can be reduced, and the life of the refractory material can be extended. Further, since cooling is performed by evaporation of cooling water, the amount of cooling water used can be reduced. The durability of the furnace can be increased by air cooling the bottom. By circulating water, the amount of cooling water used can be further reduced.
[0020]
The present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the scope of the present invention.
[0021]
【The invention's effect】
As described above, according to the present invention, when the incinerated ash charged into the melting furnace is melted, the cooling water is sprayed on the outer peripheral surface of the iron skin of the furnace wall to cool the refractory material. Since it prevents it, there exists an outstanding effect, such as extending the lifetime of a refractory material.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of an ash melting furnace according to the present invention.
FIG. 2 is a longitudinal sectional view of a conventional ash melting furnace.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Ash melting furnace 2 Furnace wall 2a Furnace bottom 3 Iron skin 4 Furnace lid 5 Upper electrode 5a Furnace bottom electrode 6 Incineration ash injection pipe 7 Incineration ash injection port 8 Exhaust pipe 9 Exhaust outlet 10 Incineration ash 11 Molten slag 12 Molten metal 13 Cooling Water tanks 14 and 27 Water supply pipes 15 and 26 Water supply pump 16 Annular water spray pipe 16a Water spray hole 17 Cooling water 18 Water trays 19 and 19a Drain pipe 20 Enclosure 21 Air cooling fan 22 Blower pipe 23 Exhaust pipe 24 Drain receiving section 25 Water tank a Ash Melting furnace b Furnace wall c Water-cooled jacket d Water-cooled tube e Furnace f Depot outlet g Outlet h Upper electrode i Furnace electrode j Incinerated ash charging pipe k Exhaust pipe m Incinerated ash n Molten slag o Molten metal p Power source q, r Electrical wire

Claims (2)

焼却灰を溶融処理する灰溶融炉であって、該灰溶融炉の炉壁の外面の鉄皮を、散水により冷却するようにし、
灰溶融炉の底部を、空冷により冷却するようにし、
灰溶融炉の底部を空冷した空気を、炉壁外面の鉄皮の散水面に沿って通風するようにした、ことを特徴とする灰溶融炉。
An ash melting furnace for melting incinerated ash, wherein the outer skin of the furnace wall of the ash melting furnace is cooled by watering ,
The bottom of the ash melting furnace is cooled by air cooling,
An ash melting furnace characterized in that air obtained by cooling the bottom of the ash melting furnace is ventilated along the water spray surface of the iron skin on the outer surface of the furnace wall .
散水後の水を、灰溶融炉の底部に張り出して設けた受け皿で受けて循環させながら散水するようにした請求項1に記載の灰溶融炉。The ash melting furnace according to claim 1, wherein the water after sprinkling is sprinkled while being received and circulated by a receiving tray provided overhanging at the bottom of the ash melting furnace.
JP15117096A 1996-06-12 1996-06-12 Ash melting furnace Expired - Lifetime JP3750881B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15117096A JP3750881B2 (en) 1996-06-12 1996-06-12 Ash melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15117096A JP3750881B2 (en) 1996-06-12 1996-06-12 Ash melting furnace

Publications (2)

Publication Number Publication Date
JPH102539A JPH102539A (en) 1998-01-06
JP3750881B2 true JP3750881B2 (en) 2006-03-01

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4800853A (en) * 1988-01-11 1989-01-31 Excelermatic Inc. Adiabatic internal combustion engine
CA2418836A1 (en) * 2003-02-12 2004-08-12 Resorption Canada Ltd. Multiple plasma generator hazardous waste processing system
NZ573217A (en) 2006-05-05 2011-11-25 Plascoenergy Ip Holdings S L Bilbao Schaffhausen Branch A facility for conversion of carbonaceous feedstock into a reformulated syngas containing CO and H2
US8128728B2 (en) 2006-05-05 2012-03-06 Plasco Energy Group, Inc. Gas homogenization system
WO2008104058A1 (en) 2007-02-27 2008-09-04 Plasco Energy Group Inc. Gasification system with processed feedstock/char conversion and gas reformulation
US9321640B2 (en) 2010-10-29 2016-04-26 Plasco Energy Group Inc. Gasification system with processed feedstock/char conversion and gas reformulation

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