JP3891685B2 - Ash melting furnace - Google Patents
Ash melting furnace Download PDFInfo
- Publication number
- JP3891685B2 JP3891685B2 JP10038298A JP10038298A JP3891685B2 JP 3891685 B2 JP3891685 B2 JP 3891685B2 JP 10038298 A JP10038298 A JP 10038298A JP 10038298 A JP10038298 A JP 10038298A JP 3891685 B2 JP3891685 B2 JP 3891685B2
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- Prior art keywords
- slag
- ash
- furnace
- molten
- weir
- 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.)
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- 238000002844 melting Methods 0.000 title claims description 26
- 230000008018 melting Effects 0.000 title claims description 25
- 239000002893 slag Substances 0.000 claims description 96
- 238000010079 rubber tapping Methods 0.000 claims description 5
- 239000002956 ash Substances 0.000 description 61
- 238000010586 diagram Methods 0.000 description 4
- 230000003628 erosive effect Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Gasification And Melting Of Waste (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、都市ごみや産業廃棄物の焼却炉より排出される焼却灰や飛灰並びに石炭焚事業用ボイラ等から排出される灰等の被溶融部材である灰の表面を、バーナにより加熱溶融して、溶融灰を溶融スラグとして排出する灰溶融炉における溶融スラグの排出流動性を高めた効率的出滓部を備えた灰溶融炉に関する。
【0002】
【従来の技術】
上記一般に使用されているバーナ式灰溶融炉には、円形回転式表面溶融炉と角型固定式表面溶融炉とがあるが、本発明が適用される角型固定式表面溶融炉により概略の機能を説明する。
図5に示すように、角型固定式表面灰溶融炉は、斜めに下降する傾斜状の炉底55と、炉本体の一端側に設けた灰供給部53と、他端側に設けた排出口57と、炉天井56に設けた固定バーナ52とよりなる。前記灰供給部53は下端に灰供給口54を備えた灰貯留部60よりなり、灰貯留部60は焼却灰等の被溶融部材を貯留し、その下部より貯留する前記被溶融部材である灰50をプッシャ58を介して排出口57に向け、炉底55の傾斜面に沿って灰供給層59を形成させる構造にしてある。
【0003】
そして、前記固定バーナ52は、炉天井56の中央軸線上に設けられ、該バーナ内に圧送された液体燃料を高圧空気ないし排熱ボイラの蒸気により微粒子化して噴射し、それとともに供給される高温の燃焼空気と混合させて前記微粒化された燃料を燃焼させ、その火炎輻射熱が灰供給層59の表面を加熱溶融し溶融灰25を形成するようにしている。
前記排出口57に向け移動を続ける灰供給層59の外表面の灰は、上記のように加熱溶融され溶融灰25を形成してスラグ池65に貯留された後、溶融スラグ25aとして堰63に設けたスラグ出滓口64を介して排出口57の下部へ滴下させ、図示してない水封コンベアを介して外部へ排出している。
【0004】
【発明が解決しようとする課題】
上記スラグ池65を形成する堰63と、該堰上に設けたスラグ出滓口64とは、図5と図5のIV−IV視図である図6に見るように、スラグ池65は略長方形状の溜め池状に形成され、前記角型のスラグ池65に貯留された溶融灰25は中央に設けられたスラグ出滓口64より排出されるわけであるが、堰63側の二つの角型隅の溶融灰25の動きは澱み状を呈し、該澱み部は温度低下とともに肥大化して流路を狭め、スラグ流の流動性低下の原因を形成している。
【0005】
本発明はかかる課題の解決のためになされたもので、前記スラグ池に貯留された溶融灰よりなる溶融スラグのスラグ排出口への流れに高い流動性を持たせ、溶融スラグの排出速度の向上を図った灰溶融炉、特に角型固定式表面灰溶融炉の提供を目的としたものである。
【0006】
【課題を解決するための手段】
そこで、本発明の灰溶融炉は、炉本体の一端側に灰供給口を設け、他端側に溶融スラグの排出口を形成し、前記灰供給口から供給された灰を傾斜した炉底に沿って前記排出口側へ移動させながらバーナにより加熱溶融するとともに、溶融した溶融灰を前記炉底の他端側に設けた堰により形成されたスラグ池に溶融スラグとして貯留され、且つ該貯留された溶融スラグを炉底末端に設けられ且つ堰の中央に設けたスラグ出滓口より排出されるように構成した灰溶融炉において、
前記スラグ池の炉底面をスラグ出滓口に向かう方向に下降させて形成し、
且つ、前記炉底の他端側に設けた堰の両側壁を炉底末端に設けた出滓口に収束する案内面として形成するとともに、
該案内面を形成する両側壁が前記スラグ出滓口へ向けての溶融スラグの流入幅を除々に挟幅とする直線若しくは曲線状面形状であることを特徴とする。
【0007】
また、前記案内面は前記スラグ出滓口へ向けての溶融スラグの流入幅を除々に挟幅とする直線状または曲線状面形状にするのがよい。
【0008】
また、請求項1記載の灰溶融炉が、炉本体の中央軸芯上に設けられたバーナにより加熱溶融されて、溶融した溶融灰を前記炉底の他端側に設けた堰の中央に設けたスラグ出滓口より排出されるように構成した灰溶融炉である場合において、
前記スラグ出滓口は、前記堰の中央部に設け、前記炉底末端がその中央軸芯部をスラグ出滓口に向け、好ましくは徐々に下降する凹状に形成させるのがよい。
【0009】
【作用】
上記発明によれば、上記溶融スラグを貯留するスラグ池の堰側側壁にスラグ出滓口への溶融スラグの円滑な流れを惹起させるべく該案内面を設けたため、前記バーナにより加熱溶融された溶融灰はスラグ池の出口であるスラグ出滓口へ向け、滞留部を形成することなく澱みなく移動させることができ、スラグ出滓口に前記溶融灰を効率的に集中でき、溶融スラグの円滑な排出を可能にすることができる。
【0010】
また、上記発明によれば、前記案内面が前記スラグ出滓口へ向けて溶融スラグの流入幅を徐々に挟幅とする面形状であるために、スラグ池の形状をスラグ出滓口へ向け漏斗状に形成させ、堰側の二つの角型隅を削除して澱みの原因を排除することができる。また壁にぶつかる方向の流速が小さくなり、侵食を低減することができる。
【0011】
また、請求項2記載の発明によれば、請求項1記載の灰溶融炉が、炉本体の中央軸芯上に設けられたバーナにより加熱溶融されて、溶融した溶融灰を前記炉底の他端側に設けた堰の中央に設けたスラグ出滓口より排出されるように構成した灰溶融炉である場合において、スラグ出滓口を堰の中央部に設ける構成としたため、炉体本体の中央軸芯上に設けられたバーナにより加熱溶融されて、炉底中央軸芯上に流れの中心を形成する溶融灰の流れに対しても円滑な流れを持たせることができる。
また、前記炉底の末端の中央軸芯部を徐々に下降させる凹状に形成したため、前記スラグ出滓口への溶融灰の流れが前記出滓口から離れた位置からも容易に方向付け且つ集中させることができる。
なお、上記スラグ出滓口の切り欠き形状は、船底形状に形成させ溶融スラグの前記出滓口における動きを円滑にしても良い。
【0012】
【発明の実施の形態】
以下、本発明の実施例の形態を、図示例と共に説明する。ただし、この実施例に記載されている構成部品の寸法、形状、その相対的位置等は特に特定的な記載がない限りは、この発明の範囲をそれに限定する趣旨ではなく、単なる説明例にすぎない。なお従来例を示す図面と同一部材については同一符号を使用する。
【0013】
図1は本発明が適用される角型固定式表面灰溶融炉の概略の構成を示す図で、本発明の角型固定式表面灰溶融炉は、炉体本体の一端側には灰供給部53とその下部に灰供給口54が設けられ、灰50は前記灰供給口54よりその下部に設けられた炉底55上に供給され、傾斜する炉底55に沿って灰供給層59を形成させながら炉底55の末端に向け移動させるとともに、炉体本体の上部の炉天井56の中央軸芯に設けた固定バーナ52により前記灰供給層59の表面の灰を加熱溶融させ、溶融された溶融灰25は、前記炉底55の末端に設けた堰12により形成されたスラグ池10に溶融スラグとして貯留され、且つ該貯留された溶融スラグは前記堰12の中央に設けたスラグ出滓口11より排出口57の下部へ排出されるように構成する。
【0014】
上記スラグ池10は図2(A)、(B)、(C)に示す上から見た平面図に見るように、炉底55の末端に設けられ、堰12の中央軸芯Y−Y上に設けたスラグ出滓口11に向け略漏斗状の形状で構成され、例えば三角型スラグ池10aないし放物型スラグ池10bまたは漏斗状スラグ池10cよりなり、堰12の側壁に直線状案内面11aないし曲線状案内面11bまたは漏斗状案内面11cを設け、溶融スラグのスラグ出滓口11への流入幅を上記連続的案内面11a/11b/11cにより除々に狭め、溶融スラグの流れが自然にスラグ出滓口11へ収束するように構成する。
【0015】
また、上記スラグ池10の側面より見た構造を、図1のIII−III視図である図3及び図4に示してある。
図に見るように、底の形状は図3に示すように、中央軸芯Z−Zで最低凹部形成する船底型とし、且つ炉底の長さ方向に対しては、その中央軸芯Y−Y(図2参照)に沿って暫時下降させた船底型炉底13(隅線で図示)により構成してある。該船底型炉底13により、溶融スラグの流れは中央軸芯Y−Yに収束される。
なお、上記スラグ出滓口の切り欠き形状は、船底形状に形成させ溶融スラグの出滓口における動きを円滑にしても良い。
【0016】
【発明の効果】
上記記載のように、本発明の角型固定式表面灰溶融炉によれば、前記バーナにより加熱溶融された溶融灰はスラグ池の出口であるスラグ出滓口へ向け、滞留部を形成することなく澱みなく移動させることができ、スラグ出滓口に前記溶融灰を効率的に収束でき、溶融スラグの円滑な排出を可能にすることができ、溶融スラグの流出速度を上げ、さらに底面との接触面が少なく、表面積も小さくなるので、熱ロスは小さくなる。
【0017】
また、本発明によれば、スラグ池の形状をスラグ出滓口へ向け漏斗状に形成させたため、堰側の二つの角型隅を削除して澱みの原因を排除するとともに、溶融スラグの流れをスラグ出滓口へ向け無理なく収束させることができる。さらに壁に向かう流速が小さいので堰部の耐火材の侵食が小さくなる。
【0018】
また、請求項2記載の発明によれば、スラグ出滓口を堰の中央部に設ける構成としたため、炉体本体の中央軸芯上に設けられたバーナにより加熱溶融されて、炉底中央軸芯上に流れの中心を形成する溶融灰の流れに対して、円滑な流れを持たせることができる。
また、前記炉底の末端がその中央軸芯に沿って暫時下降させ、凹状に形成させたため、前記スラグ出滓口への溶融灰の流れが前記出滓口から離れた位置からも容易に方向付け且つ収束させることができる。
【図面の簡単な説明】
【図1】 本発明の灰溶融炉の概略の構成を示す図である。
【図2】 図1のスラグ池の上から見た平面図の実施例を示す図で、(A)は三角型スラグ池を示し、(B)は放物型スラグ池を示し、(C)漏斗状スラグ池を示す図である。
【図3】 図1のIII−III視図である。
【図4】 図1のスラグ池の縦断面図である。
【図5】 従来の灰溶融炉の概略の構成を示す図である。
【図6】 図5のIV−IV視図である。
【符号の説明】
10 スラグ池
10a 三角型スラグ池
10b 放物型スラグ池
10c 漏斗状スラグ池
11 スラグ出滓口
11a 直線状案内面
11b 曲線状案内面
11c 漏斗状案内面
12 堰
13 船底型炉底
25 溶融灰
25a 溶融スラグ[0001]
BACKGROUND OF THE INVENTION
The present invention heats and melts the surface of ash, which is a material to be melted, such as incineration ash and fly ash discharged from municipal incinerators and industrial waste incinerators, and ash discharged from coal fired boilers, etc. In addition, the present invention relates to an ash melting furnace having an efficient brewing portion with improved molten slag discharge fluidity in an ash melting furnace for discharging molten ash as molten slag.
[0002]
[Prior art]
The generally used burner type ash melting furnace includes a circular rotary surface melting furnace and a square fixed surface melting furnace, but the rough functions of the square fixed surface melting furnace to which the present invention is applied are described. Will be explained.
As shown in FIG. 5, the square fixed surface ash melting furnace has an
[0003]
The fixed
The ash on the outer surface of the
[0004]
[Problems to be solved by the invention]
The
[0005]
The present invention has been made to solve such a problem, and has a high fluidity in the flow of molten slag made of molten ash stored in the slag pond to the slag discharge port, thereby improving the discharge rate of the molten slag. The purpose of the present invention is to provide an ash melting furnace , particularly a square fixed surface ash melting furnace .
[0006]
[Means for Solving the Problems]
Therefore, the ash melting furnace of the present invention is provided with an ash supply port on one end side of the furnace body, a discharge port for molten slag is formed on the other end side, and the ash supplied from the ash supply port is inclined to the bottom of the furnace. to together with heating and fusing the burner while moving to the discharge port side along, stored as a molten slag in slag pond formed by weir having a molten molten ash at the other end of the furnace bottom, and the reservoir In the ash melting furnace configured to discharge the molten slag provided at the furnace bottom end and discharged from the slag outlet provided in the center of the weir ,
Forming the bottom of the furnace of the slag pond in a direction toward the slag outlet,
And, forming both side walls of the weir provided on the other end side of the furnace bottom as a guide surface that converges on the tap hole provided at the furnace bottom end,
Both side walls forming the guide surface have a straight or curved surface shape in which the inflow width of the molten slag toward the slag outlet is gradually sandwiched .
[0007]
The guide surface may have a linear or curved surface shape in which the inflow width of the molten slag toward the slag outlet is gradually narrowed .
[0008]
The ash melting furnace according to claim 1 is heated and melted by a burner provided on a central axis of the furnace body, and the molten ash is provided in the center of a weir provided on the other end side of the furnace bottom. In the case of an ash melting furnace configured to be discharged from the slag outlet,
The slag tap outlet is provided at the center of the weir, and the bottom end of the furnace is preferably formed in a concave shape with its central shaft core portion directed toward the slag tap outlet, preferably gradually descending.
[0009]
[Action]
According to the above Symbol onset bright, due to the provision of the guiding surface in order to induce a smooth flow of the molten slag on the weir sidewall slag pond that stores the molten slag into the slag tapping port, is heated and melted by the burner The molten ash can move toward the slag outlet, which is the outlet of the slag pond, without stagnation without forming a stagnant part, and the molten ash can be efficiently concentrated at the slag outlet, Smooth discharge can be made possible.
[0010]
Further, according to the invention, in order the guide surface is a surface shaped to gradually narrow the width of the inlet breadth of molten slag toward the slag tapping port, toward the shape of the slag pool to slag tapping port It can be formed in a funnel shape, and the cause of stagnation can be eliminated by removing the two square corners on the weir side. Moreover, the flow velocity in the direction of hitting the wall is reduced, and erosion can be reduced.
[0011]
According to the invention described in claim 2, the ash melting furnace according to claim 1 is heated and melted by the burner provided on the center axis of the furnace body, and the molten ash is melted in addition to the furnace bottom. In the case of an ash melting furnace configured to be discharged from the slag tap outlet provided in the center of the weir provided on the end side, since the slag tap outlet is provided in the central portion of the weir, A smooth flow can be imparted to the flow of molten ash that is heated and melted by a burner provided on the center axis and forms the center of the flow on the center axis of the furnace bottom.
Further, since the central shaft core at the end of the furnace bottom is formed in a concave shape that gradually descends, the flow of the molten ash to the slag outlet is easily directed and concentrated from a position away from the outlet. Can be made.
In addition, the notch shape of the slag outlet may be formed into a ship bottom shape so that the movement of the molten slag at the outlet is smooth.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the form of the Example of this invention is demonstrated with the example of illustration. However, the dimensions, shapes, relative positions, etc. of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, and are merely illustrative examples. Absent. In addition, the same code | symbol is used about the same member as drawing which shows a prior art example.
[0013]
Figure 1 is a diagram showing the schematic structure of rectangular stationary surface ash-melting furnace to which the present invention is applied, the square fixed surface ash melting furnace of the present invention, at one end of the furnace body main
[0014]
The
[0015]
Moreover, the structure seen from the side surface of the said
As shown in the figure, as shown in FIG. 3, the shape of the bottom is a ship bottom shape in which the minimum recess is formed at the center axis ZZ, and the center axis Y- It is constituted by a ship bottom type furnace bottom 13 (shown by a corner line) lowered for a while along Y (see FIG. 2). By the ship bottom furnace bottom 13, the flow of the molten slag is converged to the central axis YY.
In addition, the notch shape of the slag outlet may be formed into a ship bottom shape so that the movement of the molten slag at the outlet is smooth.
[0016]
【The invention's effect】
As described above, according to the rectangular fixed surface ash melting furnace of the present invention, the molten ash heated and melted by the burner forms a staying portion toward the slag outlet that is the outlet of the slag pond. It can be moved without stagnation, the molten ash can be efficiently converged at the slag outlet, the slag can be discharged smoothly, the molten slag discharge speed is increased, and Since the contact surface is small and the surface area is small, the heat loss is small.
[0017]
Further, according to the present invention, the shape of the slag pond is formed in a funnel shape toward the slag outlet, so the two square corners on the weir side are eliminated to eliminate the cause of stagnation, and the flow of molten slag Can be converged without difficulty toward the slag outlet. Furthermore, since the flow velocity toward the wall is small, the erosion of the refractory material in the weir is reduced.
[0018]
According to the invention described in claim 2 , since the slag outlet is provided in the central part of the weir, it is heated and melted by the burner provided on the central axis of the furnace body body, A smooth flow can be imparted to the flow of molten ash that forms the center of flow on the core.
Further, since the end of the furnace bottom is lowered for a while along the central axis of the furnace bottom and formed into a concave shape, the flow of molten ash to the slag outlet is easily directed from a position away from the outlet. And converge.
[Brief description of the drawings]
FIG. 1 is a diagram showing a schematic configuration of an ash melting furnace according to the present invention.
2 is a diagram showing an example of a plan view seen from above the slag pond in FIG. 1, (A) shows a triangular slag pond, (B) shows a parabolic slag pond, and (C) a funnel shape. It is a figure which shows a slag pond.
FIG. 3 is a view taken along the line III-III in FIG.
4 is a longitudinal sectional view of the slag pond in FIG. 1. FIG.
FIG. 5 is a diagram showing a schematic configuration of a conventional ash melting furnace.
6 is a view taken along the line IV-IV in FIG. 5;
[Explanation of symbols]
DESCRIPTION OF
Claims (2)
前記スラグ池の炉底面をスラグ出滓口に向かう方向に下降させて形成し、
且つ、前記炉底の他端側に設けた堰の両側壁を炉底末端に設けた出滓口に収束する案内面として形成するとともに、
該案内面を形成する両側壁が前記スラグ出滓口へ向けての溶融スラグの流入幅を除々に挟幅とする直線若しくは曲線状面形状であることを特徴とする灰溶融炉。While providing an ash supply port on one end side of the furnace body, forming a discharge port for molten slag on the other end side, moving the ash supplied from the ash supply port to the discharge port side along the inclined furnace bottom The molten ash is heated and melted by a burner, and the molten ash is stored as molten slag in a slag pond formed by a weir provided at the other end of the furnace bottom , and the stored molten slag is provided at the furnace bottom end. And in the ash melting furnace configured to be discharged from the slag outlet at the center of the weir ,
Forming the bottom of the furnace of the slag pond in a direction toward the slag outlet,
And, forming both side walls of the weir provided on the other end side of the furnace bottom as a guide surface that converges on the tap opening provided at the furnace bottom end,
An ash melting furnace characterized in that both side walls forming the guide surface have a straight or curved surface shape with the inflow width of the molten slag toward the slag tap opening gradually sandwiched .
前記スラグ出滓口が前記堰の中央部に設けられ、前記炉底末端がその中央軸芯部をスラグ出滓口に向け下降する凹状に形成されていることを特徴とする請求項1記載の灰溶融炉。 A slag provided in the center of a weir provided in the other end side of the furnace bottom, wherein the ash melting furnace according to claim 1 is heated and melted by a burner provided on a central axis of the furnace body. In the case of an ash melting furnace configured to be discharged from the tap,
The slag tapping port provided in the center of the weir, the furnace bottom end according to claim 1, characterized in that the central axis portion are formed in a concave shape descending toward the slag tapping port Ash melting furnace.
Priority Applications (14)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10038298A JP3891685B2 (en) | 1998-03-27 | 1998-03-27 | Ash melting furnace |
| TW88104341A TW468021B (en) | 1998-03-27 | 1999-03-19 | Ash melting furnace and ash melting method thereof |
| PCT/JP1999/001501 WO1999050600A1 (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and ash melting method thereof |
| EP19990909334 EP0990847B1 (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and ash melting method thereof |
| CNB2004100953668A CN1289855C (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and method |
| CNB2004100953687A CN1289856C (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and method |
| US09/424,063 US6193503B1 (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and ash melting method thereof |
| DE1999631322 DE69931322T2 (en) | 1998-03-27 | 1999-03-25 | ASHELMING OVEN AND METHOD FOR OPERATING THE SAME |
| DE1999634921 DE69934921T2 (en) | 1998-03-27 | 1999-03-25 | Ash smelting furnace and process |
| CNB2004100953672A CN100356105C (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and method |
| CNB99800393XA CN1223792C (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and ash melting method thereof |
| EP20050004941 EP1550827B1 (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and method |
| EP04029905A EP1522789A3 (en) | 1998-03-27 | 1999-03-25 | Ash melting furnace and method |
| KR1019997010915A KR100313635B1 (en) | 1998-03-27 | 1999-11-24 | Ash melting furnace and ash melting method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10038298A JP3891685B2 (en) | 1998-03-27 | 1998-03-27 | Ash melting furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH11281036A JPH11281036A (en) | 1999-10-15 |
| JP3891685B2 true JP3891685B2 (en) | 2007-03-14 |
Family
ID=14272472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10038298A Expired - Lifetime JP3891685B2 (en) | 1998-03-27 | 1998-03-27 | Ash melting furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3891685B2 (en) |
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1998
- 1998-03-27 JP JP10038298A patent/JP3891685B2/en not_active Expired - Lifetime
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| Publication number | Publication date |
|---|---|
| JPH11281036A (en) | 1999-10-15 |
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