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JP5326193B2 - Power generation method and power generation apparatus using exhaust gas, and exhaust gas oxidation treatment method and oxidation treatment apparatus - Google Patents
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JP5326193B2 - Power generation method and power generation apparatus using exhaust gas, and exhaust gas oxidation treatment method and oxidation treatment apparatus - Google Patents

Power generation method and power generation apparatus using exhaust gas, and exhaust gas oxidation treatment method and oxidation treatment apparatus Download PDF

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JP5326193B2
JP5326193B2 JP2006178527A JP2006178527A JP5326193B2 JP 5326193 B2 JP5326193 B2 JP 5326193B2 JP 2006178527 A JP2006178527 A JP 2006178527A JP 2006178527 A JP2006178527 A JP 2006178527A JP 5326193 B2 JP5326193 B2 JP 5326193B2
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exhaust gas
oxygen
flue
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furnace
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JP2008010276A (en
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和直 高橋
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    • YGENERAL 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
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    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Description

本発明は、製鉄所の転炉ガスやコークス炉ガスなどの所定量以上のHまたはCOを含む排ガスを用いた発電方法および発電装置、ならびに当該排ガスの酸化処理方法および酸化処理装置に関するものである。 The present invention relates to a power generation method and a power generation apparatus using an exhaust gas containing a predetermined amount or more of H 2 or CO, such as converter gas and coke oven gas of a steel mill, and an oxidation treatment method and an oxidation treatment apparatus for the exhaust gas. is there.

一般に、製鉄所の転炉やコークス炉からは、所定濃度以上のHまたはCOを含む高温の排ガスが大量に発生するが、従来このような排ガスは、その後酸素付加によりHまたはCOを燃焼(酸化)処理して無害化してから大気に排出している(2H+O→2HO、2CO+O→2CO
そして、このような所定濃度以上のHまたはCOを含む排ガスの燃焼処理に際しては、その燃焼熱を有効利用することが試みられているが、その燃焼熱の発生箇所は転炉やコークス炉などの炉尻や煙道であるため、利用し難くかつ回収効率も芳しくない。
In general, large amounts of high-temperature exhaust gas containing H 2 or CO at a predetermined concentration or more are generated from converters and coke ovens in steelworks. Conventionally, such exhaust gas burns H 2 or CO by oxygen addition thereafter. (Oxidation) treated to detoxify and then discharged to the atmosphere (2H 2 + O 2 → 2H 2 O, 2CO + O 2 → 2CO 2 )
In the combustion treatment of the exhaust gas containing H 2 or CO having a predetermined concentration or more, attempts have been made to effectively use the combustion heat, and the location where the combustion heat is generated is a converter, coke oven, etc. It is difficult to use and the collection efficiency is not good because of the furnace bottom and flue.

すなわち、燃焼処理時に発生する熱エネルギーを有効に活用できない原因の1つとして、熱エネルギーは移送に伴いロスが多く、発生源の近くで使用する以外はそのエネルギー形態を変化させる必要があることが挙げられる。さらに、その熱エネルギー形態を電気エネルギーなどに変換させる設備には膨大な投資を要するといった問題がある。さらに、燃焼処理することによって大量のCOを発生してしまう結果となる。 That is, as one of the reasons why the thermal energy generated during the combustion process cannot be used effectively, the thermal energy has a lot of loss due to the transfer, and it is necessary to change its energy form except for use near the generation source. Can be mentioned. Furthermore, there is a problem that a large amount of investment is required for equipment that converts the thermal energy form into electrical energy. Furthermore, the combustion process results in a large amount of CO 2 being generated.

そのため、例えば、以下の特許文献1および2などでは、転炉やコークス炉などで発生するHまたはCOを含む高温の排ガスを高温燃料電池の燃料ガスとして用い、電気エネルギーとして回収するような方法を提案している。
特開昭60−177571号公報 特開昭63−62160号公報
Therefore, for example, in Patent Documents 1 and 2 below, a method of using high-temperature exhaust gas containing H 2 or CO generated in a converter or coke oven as fuel gas of a high-temperature fuel cell and recovering it as electric energy Has proposed.
JP-A-60-177571 Japanese Unexamined Patent Publication No. 63-62160

ところで、前記特許文献1および2では、転炉やコークス炉で発生した高温の排ガスを一旦ガスホルダーなどに溜めておき、精製処理や余熱処理などを行ってからこれを燃料電池に供給して発電に用いるようにしているため、そのための専用の設備が新たに必要となり、その建設や処理に膨大な費用を要するといった問題がある。
そこで、本発明はこのような課題を有効に解決するために案出されたものであり、その目的は、転炉やコークス炉で発生する高温の排ガス中のHまたはCOを少ないコストで活用または酸化処理できる新規な排ガスを用いた発電方法および発電装置、ならびに排ガスの酸化処理方法および酸化処理装置を提供するものである。
By the way, in Patent Documents 1 and 2, high-temperature exhaust gas generated in a converter or coke oven is once stored in a gas holder or the like, subjected to refining treatment or post-heat treatment, and then supplied to a fuel cell to generate power. Therefore, there is a problem that a dedicated facility for that purpose is newly required and a huge amount of money is required for its construction and processing.
Accordingly, the present invention has been devised to effectively solve such problems, and its purpose is to utilize H 2 or CO in high-temperature exhaust gas generated in a converter or coke oven at a low cost. Alternatively, the present invention provides a power generation method and power generation apparatus using a novel exhaust gas that can be oxidized, and an exhaust gas oxidation treatment method and oxidation treatment apparatus.

前記課題を解決するために第一の発明は、
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを用いた発電方法であって、転炉またはコークス炉で発生した700〜1000℃の排ガスをそのまま直接用い、前記燃焼処理に代えて、前記排ガスが通過する煙道または炉内に、イオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させて当該煙道または炉内を通過する前記排ガスと接触させると共に、当該燃料電池の酸素極側に酸素を供給して発電を行うようにしたことを特徴とする排ガスを用いた発電方法である。
In order to solve the above problems, the first invention is:
A power generation method using exhaust gas containing H 2 and / or CO having a predetermined concentration or more, generated from a converter or coke oven, and burned for detoxification and discharged to the atmosphere. In addition, the exhaust gas at 700 to 1000 ° C. generated in a converter or coke oven is directly used as it is, and instead of the combustion treatment, a fuel having an ion conductive oxide as a solid electrolyte in a flue or furnace through which the exhaust gas passes An exhaust gas characterized in that a fuel electrode of a battery is positioned and brought into contact with the exhaust gas passing through the flue or furnace, and oxygen is supplied to the oxygen electrode side of the fuel cell to generate electric power. This is the power generation method used.

また、第二の発明は、
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを用いた発電装置であって、前記排ガスが通過する煙道または炉内に設けられ、当該煙道または炉内を通過する前記排ガスと接触するようにイオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させると共に、当該燃料電池の酸素極側に酸素を供給する酸素供給手段を備えたことを特徴とする排ガスを用いた発電装置である。
In addition, the second invention,
One specific concentration or more of H 2 and CO or either only contains, and, a power generation apparatus using the exhaust gas is discharged to the atmosphere from the combustion process for detoxifying generated from a converter furnace or the coke oven The fuel electrode of the fuel cell is provided in a flue or furnace through which the exhaust gas passes, and the ion conductive oxide is used as a solid electrolyte so as to be in contact with the exhaust gas passing through the flue or furnace. In addition, there is provided a power generation apparatus using exhaust gas, characterized in that oxygen supply means for supplying oxygen to the oxygen electrode side of the fuel cell is provided.

また、第三の発明は、
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを酸化処理する方法であって、転炉またはコークス炉で発生した700〜1000℃の排ガスをそのまま直接用い、前記燃焼処理に代えて、前記排ガスが通過する煙道または炉内に、イオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させて当該煙道または炉内を通過する前記排ガスと接触させると共に、当該燃料電池の酸素極側に酸素を供給して前記排ガス中のH2 およびCOまたはいずれか一方を酸化処理するようにした排ガスの酸化処理方法である。
In addition, the third invention,
A method of oxidizing an exhaust gas containing H 2 and / or CO having a predetermined concentration or more and being emitted from a converter or a coke oven and burned for detoxification and discharged into the atmosphere. In addition, the exhaust gas at 700 to 1000 ° C. generated in a converter or coke oven is directly used as it is, and instead of the combustion treatment, a fuel having an ion conductive oxide as a solid electrolyte in a flue or furnace through which the exhaust gas passes A fuel electrode of the battery is positioned and brought into contact with the exhaust gas passing through the flue or the furnace, and oxygen is supplied to the oxygen electrode side of the fuel cell so that H 2 and / or CO in the exhaust gas is supplied. This is an exhaust gas oxidation method for oxidizing treatment.

また、第四の発明は、
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを酸化処理する装置であって、前記排ガスが通過する煙道または炉内に設けられ、当該煙道または炉内を通過する前記排ガスと接触するようにイオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させると共に、当該燃料電池の酸素極側に酸素を供給する酸素供給手段を備えたことを特徴とする排ガスの酸化処理装置である。
In addition, the fourth invention is
One specific concentration or more of H 2 and CO or either only contains, and, there in apparatus for oxidizing the exhaust gas is discharged to the atmosphere from the combustion process for generated from the converter or coke oven harmless The fuel electrode of the fuel cell is provided in a flue or furnace through which the exhaust gas passes, and the ion conductive oxide is used as a solid electrolyte so as to be in contact with the exhaust gas passing through the flue or furnace. In addition, an exhaust gas oxidation apparatus comprising oxygen supply means for supplying oxygen to the oxygen electrode side of the fuel cell.

第一および第二の発明によれば、燃料電池をその排ガスが通過する煙道または炉内に設置したため、その排ガス中に含まれている所定濃度以上のH2 およびCOまたはいずれか一方と空気(酸素)とをその排ガスの高温を利用して効率的に反応させて発電することができる。また、その排ガスを利用するための大がかりな専用設備も不要となるため、その排ガス中のH2 またはCOを少ないコストで有効活用できる。 According to the first and second inventions, since the fuel cell is installed in a flue or furnace through which the exhaust gas passes, H 2 and / or CO having a predetermined concentration or more and either one contained in the exhaust gas and air Electricity can be generated by efficiently reacting (oxygen) with the high temperature of the exhaust gas. In addition, since a large dedicated facility for using the exhaust gas is not required, H 2 or CO in the exhaust gas can be effectively used at a low cost.

また、第三および第四の発明によれば、前記第一または第二の発明と同様に、燃料電池をその排ガスが通過する煙道または炉内に設置したため、その排ガス中に含まれている所定濃度以上のH2 およびCOまたはいずれか一方と空気(酸素)とをその排ガスの高温を利用して効率的に反応させて排ガス中から除去することができる。また、その排ガス中のH2 またはCOを除去するための大がかりな専用設備も不要となるため、その排ガス中のH2 またはCOを少ないコストで酸化処理することができる。
According to the third and fourth inventions, as in the first or second invention , since the fuel cell is installed in a flue or furnace through which the exhaust gas passes, it is included in the exhaust gas. H 2 and / or CO having a predetermined concentration or higher and air (oxygen) can be efficiently reacted using the high temperature of the exhaust gas and removed from the exhaust gas. In addition, since a large dedicated facility for removing H 2 or CO in the exhaust gas is not necessary, H 2 or CO in the exhaust gas can be oxidized at a low cost.

以下、本発明を実施するための最良の形態を添付図面を参照しながら詳述する。
図1は、本発明に係る発電装置100の実施の一形態を示したものである。
図示するようにこの発電装置100は、所定濃度以上のHおよびCOまたはいずれか一方を含む高温(例えば700〜1000℃)の排ガスが通過する煙道S内に設けられた燃料電池ユニット10と、当該燃料電池ユニット10に空気(酸素)を供給する酸素供給ファン20と、この燃料電池ユニット10で発電された電気を利用または蓄電する負荷部30とから主に構成されている。
Hereinafter, the best mode for carrying out the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 shows an embodiment of a power generator 100 according to the present invention.
As shown in the figure, the power generation apparatus 100 includes a fuel cell unit 10 provided in a flue S through which a high-temperature (for example, 700 to 1000 ° C.) exhaust gas containing H 2 and / or CO having a predetermined concentration or higher passes. The oxygen supply fan 20 that supplies air (oxygen) to the fuel cell unit 10 and a load unit 30 that uses or stores electricity generated by the fuel cell unit 10 are mainly configured.

この燃料電池ユニット10は、図2に示すように公知のそれと同様の構成となっており、発電機能を有するセル40を複数積層したセルスタック50にガスを案内するためのヘッダ(図示せず)を取り付けてなるものであり、各セル40間を仕切る各セパレータ41のスリット状の流路にそれぞれ前記排ガスと大気中の空気を交互に通過させることで発電を行うようになっている。   As shown in FIG. 2, the fuel cell unit 10 has a configuration similar to that of a known one, and a header (not shown) for guiding gas to a cell stack 50 in which a plurality of cells 40 having a power generation function are stacked. And the exhaust gas and the air in the atmosphere are alternately passed through the slit-like flow paths of the separators 41 that partition the cells 40 to generate power.

すなわち、このセルスタック50を構成する各セル40は、図3に示すように高温下で活性な固体電解質、例えばイオン導電性酸化物として代表的なイットリア安定化ジルコニア(Yttria Stabilized Zirconia:YSZ)を電解質として用いた固体電解質層42を、気体が通過可能なシートまたは板状の燃料極(カソード:例えばNi−YSZサーメットなど)43と、同じく気体が通過可能なシートまたは板状の酸素極(カソード:例えばLa(Sr)MnOなど)44で挟むと共に、その上下をそれぞれ一対のセパレータ41a,41bで挟んで積層した構造としたものである。なお、これら燃料極43および酸素極44の固体電解質層42にはこの固体電解質層42における反応(発電)を促進するための触媒層45、45がそれぞれ形成されいる。 That is, as shown in FIG. 3, each cell 40 constituting the cell stack 50 is made of a solid electrolyte that is active at a high temperature, for example, yttria stabilized zirconia (YSZ), which is a typical ion conductive oxide. The solid electrolyte layer 42 used as the electrolyte includes a sheet or plate-shaped fuel electrode (cathode: for example, Ni-YSZ cermet) 43 through which gas can pass, and a sheet or plate-shaped oxygen electrode (cathode) through which gas can also pass. : La (Sr) MnO 3 or the like) 44, and the upper and lower sides are sandwiched between a pair of separators 41a and 41b, respectively. Note that catalyst layers 45 and 45 for promoting a reaction (power generation) in the solid electrolyte layer 42 are formed on the solid electrolyte layer 42 of the fuel electrode 43 and the oxygen electrode 44, respectively.

そして、図示するように一方のセパレータ41a側に、前述したように所定濃度以上のHおよびCOまたはいずれか一方を含む高温の排ガスを通過させると共に、他方のセパレータ41b側に空気(酸素)を通過させると、図4に示すように燃料極43側では、燃料が水素(H)である場合は、このHが燃料極43側の触媒45の働きによって電子を切り離して水素イオン(2H)となる(H→2H+2e)。この固体電解質層42はイオンしか通さないという性質を持っているため、切り離された電子は電線30aから外に出て負荷部30側に流れる。 Then, as shown in the figure, high-temperature exhaust gas containing H 2 and / or CO having a predetermined concentration or higher or one of them is passed to one separator 41a side, and air (oxygen) is passed to the other separator 41b side as described above. As shown in FIG. 4, when the fuel is hydrogen (H 2 ) on the fuel electrode 43 side as shown in FIG. 4, the H 2 separates electrons by the action of the catalyst 45 on the fuel electrode 43 side to generate hydrogen ions (2H + ) (H 2 → 2H + + 2e ). Since the solid electrolyte layer 42 has a property of allowing only ions to pass therethrough, the separated electrons flow out from the electric wire 30a and flow to the load portion 30 side.

その後、この水素イオン(2H)は、固体電解質層42内を移動して反対側の酸素極44に到達し、ここで酸素極44に浸入してきた酸素(O)と負荷部30を通じて戻ってきた電子と反応(酸化)して水(HO)になり(1/2O+2H+2e→HO)、残りの空気と共に外部に排出されることになる。
なお、燃料極43側に供給される燃料が一酸化炭素(CO)である場合は、酸素極44側の酸素(O)と反応(酸化)して二酸化炭素(CO)となって残りの空気と共に外部に排出されることになる。
Thereafter, the hydrogen ions (2H + ) move in the solid electrolyte layer 42 and reach the opposite oxygen electrode 44, where they return to the oxygen (O 2 ) that has entered the oxygen electrode 44 and the load portion 30. It reacts (oxidizes) with the incoming electrons to form water (H 2 O) (1 / 2O 2 + 2H + + 2e → H 2 O), and is discharged to the outside together with the remaining air.
When the fuel supplied to the fuel electrode 43 side is carbon monoxide (CO), it reacts (oxidizes) with oxygen (O 2 ) on the oxygen electrode 44 side and remains as carbon dioxide (CO 2 ). It will be discharged to the outside along with the air.

従って、本発明は図1に示すようにこの発電装置100の燃料電池ユニット10をそのセルスタック50の燃料極43側を、所定濃度以上のHおよびCOまたはいずれか一方を含む高温の排ガスと常に接するようにその煙道S内に設置すると共に、そのセルスタック50の酸素極44に、酸素供給ファン20によって常に十分な空気を供給するようにしたものであり、これにより、その煙道Sを通過する排ガス中のHやCOを確実に酸化除去すると共に十分な電気を供給することが可能となる。 Therefore, in the present invention, as shown in FIG. 1, the fuel cell unit 10 of the power generation apparatus 100 is disposed on the fuel electrode 43 side of the cell stack 50 with high-temperature exhaust gas containing H 2 and / or CO having a predetermined concentration or higher. It is installed in the flue S so that it is always in contact, and sufficient oxygen is always supplied to the oxygen electrode 44 of the cell stack 50 by the oxygen supply fan 20. It is possible to reliably oxidize and remove H 2 and CO in the exhaust gas passing through the gas and to supply sufficient electricity.

また、この固体電解質層42は、1000℃付近で最も高い活性を示すイットリア安定化ジルコニアなどのイオン導電性酸化物からなるため、高温下でも使用可能であり、製鉄所の転炉やコークス炉で発生した直後の高温の排ガスをそのまま直接処理することができるため、専用の処理設備やハンドリングが不要となり、少ないコストで本発明を実現することが可能となる。   The solid electrolyte layer 42 is made of an ion conductive oxide such as yttria-stabilized zirconia that exhibits the highest activity around 1000 ° C., and can be used at high temperatures. Since the high-temperature exhaust gas immediately after generation can be directly processed, dedicated processing equipment and handling become unnecessary, and the present invention can be realized at a low cost.

なお、本実施の形態では、この発電装置100の燃料電池ユニット10を、所定濃度以上のHおよびCOまたはいずれか一方を含む高温の排ガスが流れる煙道Sに設けた例で説明したが、例えばその排ガス中の熱を回収した後(冷却後)に煙道Sに流すようなケース(設備)では、その排ガス温度が低くて反応が芳しくない。そのため、このようなケースでは、煙道Sではなく、高温の排ガスが発生する炉内に直接この発電装置100の燃料電池ユニット10を設けるようにしても良い。 In the present embodiment, the fuel cell unit 10 of the power generation apparatus 100 has been described as an example in which the fuel cell unit 10 is provided in the flue S through which high-temperature exhaust gas containing H 2 and / or CO having a predetermined concentration or more flows. For example, in a case (equipment) in which the heat in the exhaust gas is recovered (after cooling) and flows into the flue S, the exhaust gas temperature is low and the reaction is not good. Therefore, in such a case, the fuel cell unit 10 of the power generation apparatus 100 may be provided directly in the furnace where the high-temperature exhaust gas is generated instead of the flue S.

本発明に係る発電装置100の実施の一形態を示す説明図である。It is explanatory drawing which shows one Embodiment of the electric power generating apparatus 100 which concerns on this invention. 本発明に係る発電装置100の一部を構成する燃料電池ユニット10を示す斜視図である。It is a perspective view which shows the fuel cell unit 10 which comprises a part of electric power generating apparatus 100 which concerns on this invention. 燃料電池ユニット10を構成するセル40の構造を示す分解斜視図である。3 is an exploded perspective view showing a structure of a cell 40 constituting the fuel cell unit 10. FIG. セル40による発電の原理を示す説明図である。3 is an explanatory diagram showing the principle of power generation by a cell 40. FIG.

符号の説明Explanation of symbols

100…発電装置(酸化処理装置)
10…燃料電池ユニット
20…酸素供給ファン(酸素供給手段)
30…負荷部
30a…電線
40…セル
41…セパレータ
42…固体電解質層
43…燃料極
44…酸素極
45…触媒
50…セルスタック
S…煙道
100 ... Power generation device (oxidation treatment device)
DESCRIPTION OF SYMBOLS 10 ... Fuel cell unit 20 ... Oxygen supply fan (oxygen supply means)
DESCRIPTION OF SYMBOLS 30 ... Load part 30a ... Electric wire 40 ... Cell 41 ... Separator 42 ... Solid electrolyte layer 43 ... Fuel electrode 44 ... Oxygen electrode 45 ... Catalyst 50 ... Cell stack S ... Flue

Claims (4)

所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを用いた発電方法であって、
転炉またはコークス炉で発生した700〜1000℃の排ガスをそのまま直接用い、前記燃焼処理に代えて、前記排ガスが通過する煙道または炉内に、イオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させて当該煙道または炉内を通過する前記排ガスと接触させると共に、当該燃料電池の酸素極側に酸素を供給して発電を行うようにしたことを特徴とする排ガスを用いた発電方法。
A power generation method using exhaust gas containing H 2 and / or CO having a predetermined concentration or more, generated from a converter or coke oven, and burned for detoxification and discharged to the atmosphere. ,
A fuel cell in which an exhaust gas of 700 to 1000 ° C. generated in a converter or a coke oven is directly used as it is, and instead of the combustion treatment, an ion conductive oxide is used as a solid electrolyte in a flue or furnace through which the exhaust gas passes. The exhaust gas is characterized in that the fuel electrode is positioned and brought into contact with the exhaust gas passing through the flue or furnace and oxygen is supplied to the oxygen electrode side of the fuel cell to generate power. Was the power generation method.
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを用いた発電装置であって、
前記排ガスが通過する煙道または炉内に設けられ、当該煙道または炉内を通過する前記排ガスと接触するようにイオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させると共に、当該燃料電池の酸素極側に酸素を供給する酸素供給手段を備えたことを特徴とする排ガスを用いた発電装置。
A power generator using exhaust gas containing H 2 and / or CO having a predetermined concentration or more, and generated from a converter or a coke oven and subjected to combustion treatment for detoxification and then discharged to the atmosphere ,
The fuel electrode of the fuel cell is provided in a flue or furnace through which the exhaust gas passes, and an ion conductive oxide is used as a solid electrolyte so as to be in contact with the exhaust gas passing through the flue or furnace, and A power generator using exhaust gas, characterized by comprising oxygen supply means for supplying oxygen to the oxygen electrode side of the fuel cell.
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを酸化処理する方法であって、
転炉またはコークス炉で発生した700〜1000℃の排ガスをそのまま直接用い、前記燃焼処理に代えて、前記排ガスが通過する煙道または炉内に、イオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させて当該煙道または炉内を通過する前記排ガスと接触させると共に、当該燃料電池の酸素極側に酸素を供給して前記排ガス中のH2 およびCOまたはいずれか一方を酸化処理するようにした排ガスの酸化処理方法。
A method of oxidizing an exhaust gas containing H 2 and / or CO having a predetermined concentration or more and being emitted from a converter or a coke oven and burned for detoxification and discharged into the atmosphere. ,
A fuel cell in which an exhaust gas of 700 to 1000 ° C. generated in a converter or a coke oven is directly used as it is, and instead of the combustion treatment, an ion conductive oxide is used as a solid electrolyte in a flue or furnace through which the exhaust gas passes. The fuel electrode is placed in contact with the exhaust gas passing through the flue or furnace, and oxygen is supplied to the oxygen electrode side of the fuel cell to oxidize H 2 and / or CO in the exhaust gas. An exhaust gas oxidation method for treating exhaust gas.
所定濃度以上のH2 およびCOまたはいずれか一方を含み、且つ、転炉またはコークス炉から発生し無害化のために燃焼処理してから大気に排出されている排ガスを酸化処理する装置であって、
前記排ガスが通過する煙道または炉内に設けられ、当該煙道または炉内を通過する前記排ガスと接触するようにイオン導電性酸化物を固体電解質とした燃料電池の燃料極を位置させると共に、当該燃料電池の酸素極側に酸素を供給する酸素供給手段を備えたことを特徴とする排ガスの酸化処理装置。
An apparatus for oxidizing exhaust gas that contains H 2 and / or CO at a predetermined concentration or any one of them and that is generated from a converter or coke oven and burned for detoxification and then discharged to the atmosphere. ,
The fuel electrode of the fuel cell is provided in a flue or furnace through which the exhaust gas passes, and an ion conductive oxide is used as a solid electrolyte so as to be in contact with the exhaust gas passing through the flue or furnace, and An exhaust gas oxidation apparatus comprising oxygen supply means for supplying oxygen to the oxygen electrode side of the fuel cell.
JP2006178527A 2006-06-28 2006-06-28 Power generation method and power generation apparatus using exhaust gas, and exhaust gas oxidation treatment method and oxidation treatment apparatus Expired - Fee Related JP5326193B2 (en)

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