JP2003148719A - Exhaust gas treatment device for melting furnace - Google Patents

Exhaust gas treatment device for melting furnace

Info

Publication number
JP2003148719A
JP2003148719A JP2001341045A JP2001341045A JP2003148719A JP 2003148719 A JP2003148719 A JP 2003148719A JP 2001341045 A JP2001341045 A JP 2001341045A JP 2001341045 A JP2001341045 A JP 2001341045A JP 2003148719 A JP2003148719 A JP 2003148719A
Authority
JP
Japan
Prior art keywords
exhaust gas
melting furnace
fuel
dust collector
temperature
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
Application number
JP2001341045A
Other languages
Japanese (ja)
Inventor
Shogo Kuwashiro
省吾 桑代
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP2001341045A priority Critical patent/JP2003148719A/en
Publication of JP2003148719A publication Critical patent/JP2003148719A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an exhaust gas treatment device which reduces an operating cost and equipment expenses by feeding an exhaust gas including ash dust, NOx, and SO2 which is exhausted from a melting furnace such as ash melting furnaces to a dust collector and a denitration equipment to clean the gas. SOLUTION: The temperature of an exhaust gas is reduced by diluting with an external air fed to an exhaust pipe 2 of a melting furnace 1, and the exhaust gas is then fed to a dust collector 4. In addition, some amounts of the secondary exhaust gas of the dust collector are bypassed to a burner 5 in which the exhaust gas and a fuel is mixed and burned. By burning the fuel using oxygen including in the exhaust gas which is mixed with an external air, the temperature of the exhaust gas increases again, and the exhaust gas is then fed to a denitration equipment 7.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は灰溶融炉等の溶融炉
から排出される煤塵,NOx、およびSOを含んだ排
ガスを集塵機および脱硝装置に通すことにより清浄化し
て排出する排ガス処理装置に関するものである。 【0002】 【従来の技術】灰溶融炉等の溶融炉から排出される10
00℃前後の排ガスには、多量の煤塵が含まれているほ
か、NOx,SO等の刺激性の酸性ガスが含まれてい
る。従来、これらを除去するための排ガス処理装置は、
図3に示したように、溶融炉1の排気道2に外気を導入
して該排ガスを希釈するとともに水を噴霧して気化熱を
奪う冷却手段3を設けることで該排ガスの温度をバッグ
フィルタの耐熱温度である150℃程度まで下げ、該排
ガスに吸収剤として消石灰を吹き込んだ後、該排ガスを
バッグフィルタ集塵機4に導いて該排ガス中から煤塵を
捕集する。その後、燃料と燃焼用空気とを適宜比率で混
合して燃焼させるバーナ5が備えられた熱風発生炉6に
より発生させた熱風を該排気道に導いて該排ガスと混合
させることにより、該排ガスを還元脱硝反応が可能な2
10℃程度に再加熱し、これを脱硝装置7に導いて脱
硝,脱硫し、煙突8より大気中に排出するものであっ
た。 【0003】また、図4に示した湿式の排ガス処理装置
では、集塵機4の二次側に洗塩塔9を設けナトリウム塩
やアンモニウム塩等に各種塩を吸収させることで、該洗
塩塔9の二次側で排ガス温度は50℃程度まで下がるの
で、該排ガスを熱風発生炉6により発生させた熱風によ
り再び210℃程度に昇温させ、脱硝装置7に導くよう
にしている。 【0004】 【発明が解決しようとする課題】ところで従来の上記排
ガス処理装置では、バーナ5にて燃料に燃焼用空気が添
加されこれにより発生された熱風が排ガスに混合される
ので、脱硝装置7にて処理を要する排ガスの量が増大
し、脱硝装置7の所要処理能力も大きくならざるを得な
いものであった。また、バーナ5によって消費される燃
料費用も多くを要するものであった。なお、上記再加熱
には高圧蒸気や自家発電電力を熱源として使用できる環
境であることもあるが、溶融炉が単独で設置されている
場合はそのような環境ではなく、また例えその環境にあ
っても売電能力等が下がるのでその使用は得策でないこ
とが多い。そこで本発明は上記問題点を解消し、ランニ
ングコストおよび設備費を軽減できる溶融炉の排ガス処
理装置を提供しようとするものである。 【0005】 【課題を解決するための手段】そのために本発明に係る
溶融炉の排ガス処理装置は、溶融炉の排気道に外気を導
入し排ガスを希釈することで該排ガスの温度を下げてか
ら集塵機に導くとともに、該集塵機の二次側の排ガスの
一部を迂回させ該排ガスと燃料とを混合燃焼させるバー
ナを設け前記外気によって導入された排ガス中の酸素を
基に該燃料を燃焼させることで該排ガスの温度を再上昇
させた後、該排ガスを脱硝装置に導くことを特徴とす
る。 【0006】 【発明の実施の形態】次に本発明の実施形態を図1に従
い説明する。同図において、1は溶融炉、2はその排気
道、3は外気を導入して該排気道の排ガスを希釈すると
ともに水を噴霧して気化熱を奪う冷却手段、4は該冷却
手段によって150℃に冷却された排ガスから煤塵を除
去するために設けられたバッグフィルタ集塵機である。
6はバーナ5が備えられた熱風発生炉で、該バーナ5に
都市ガス等の燃料を供給するとともに、集塵機4と脱硝
装置7とを繋いでいる排気道10にバイパス路11を設
け、集塵機4の二次側から排ガスの一部をバーナ5に導
いて燃料と混合させ、該排ガス中に含まれる酸素によっ
て該熱風発生炉6中で該燃料を燃焼させる。なお、該排
ガスには上記のように冷却のために外気を導入したこと
から燃焼に必要な酸素が充分に含まれている。こうして
該熱風発生炉6で生じた熱風をバイパス路12により排
気道10に戻して他の排ガスと混合させることでその排
ガス温度が還元脱硝反応が可能な210℃程度になるよ
うにし、該排ガスを脱硝装置7に導いて脱硝,脱硫し、
煙突8より大気中に排出する。 【0007】このように排ガスの一部をバーナ5に導い
て燃焼用空気の代りとなるようにすることで、脱硝装置
7にて処理すべき排ガス量を無用に増大させることがな
いとともに、燃料も節減される。ちなみに、表1は図3
に示した従来の装置と図1に示した本発明の装置との熱
収支の算出結果を示すものである。なお、ここで、各気
体の比熱を0.34(kcal/Nm・℃)とし、燃
料は都市ガス13A(低位発熱量9940(kcal/
Nm))を使用、理論空気量を10.95(m/m
燃料ガス)、燃焼生成物を12.05(m/m
料ガス)、処理排ガス量は17000(Nm/h)を
使用、空気比を1.2とした。集塵後排ガス温度はダイ
オキシン再合成を考慮し150℃、脱硝装置入口温度は
一般的な脱硝可能温度210℃とした。室温は20℃と
し計算の基準温度とした。この結果、この装置では、3
3307kcal/h(8.7%)の少エネルギー化が
達成された。 【表1】 【0008】また、図2は本発明を集塵機4の二次側に
洗塩塔9が設けられた湿式の排ガス処理装置に実施した
態様を示すものである。この場合、該洗塩塔9の二次側
の排ガス温度が50℃と低いため、バーナ5における燃
料節減率は一層顕著なものとなる。表2は同様に図4に
示した従来の装置と図2に示した本発明の装置との熱収
支を表1と同一条件の基で算出した結果を示す。この結
果、この装置では、88820kcal/h(8.7
%)の少エネルギー化が達成された。 【表2】 【0009】なお、図1,図2に示した実施形態では熱
風発生炉6を設けているが、本発明では熱風発生炉を用
いずにバーナ5を直接排気道10に取付け、排気道内に
て燃焼させるようにしてもよい。 【0010】 【発明の効果】このように本発明に係る溶融炉の排ガス
処理装置は、集塵機の二次側の排ガスの一部を迂回させ
該排ガスと燃料とを混合燃焼させるバーナを設け、外気
によって導入された排ガス中の酸素を基に該燃料を燃焼
させることで該排ガスの温度を再上昇させるものである
ので、再加熱のための燃料が節減されランニングコスト
が軽減できるとともに、脱硝装置にて処理を要する排ガ
スの量を従来のように増大させないので設備費も軽減さ
れるなど有益な効果がある。
DETAILED DESCRIPTION OF THE INVENTION [0001] The present invention relates to the passing dust discharged from the melting furnace ash melting furnace, NOx, and an exhaust gas containing SO 2 in a dust collector and a denitration device The present invention relates to an exhaust gas treatment device for purifying and discharging exhaust gas. 2. Description of the Related Art 10 discharged from a melting furnace such as an ash melting furnace.
Exhaust gas at about 00 ° C. contains a large amount of dust and also contains irritating acidic gases such as NOx and SO 2 . Conventionally, exhaust gas treatment equipment for removing these
As shown in FIG. 3, a cooling means 3 for introducing outside air into the exhaust path 2 of the melting furnace 1 to dilute the exhaust gas and spray water to remove heat of vaporization is provided to reduce the temperature of the exhaust gas by a bag filter. After the lime is blown into the exhaust gas as an absorbent, the exhaust gas is guided to a bag filter dust collector 4 to collect dust from the exhaust gas. Thereafter, the hot air generated by the hot air generating furnace 6 provided with the burner 5 for mixing and burning the fuel and the combustion air at an appropriate ratio is guided to the exhaust path to be mixed with the exhaust gas, thereby reducing the exhaust gas. Reducing denitration reaction is possible 2
It was reheated to about 10 ° C., guided to a denitration device 7 for denitration and desulfurization, and discharged from the chimney 8 to the atmosphere. Further, in the wet exhaust gas treatment apparatus shown in FIG. 4, a salt washing tower 9 is provided on the secondary side of the dust collector 4, and various salts are absorbed by sodium salts, ammonium salts, etc. Since the temperature of the exhaust gas drops to about 50 ° C. on the secondary side of the above, the temperature of the exhaust gas is raised again to about 210 ° C. by the hot air generated by the hot air generating furnace 6, and the exhaust gas is led to the denitration device 7. [0004] In the above-mentioned conventional exhaust gas treatment apparatus, the combustion air is added to the fuel by the burner 5 and the hot air generated thereby is mixed with the exhaust gas. Therefore, the amount of exhaust gas that needs to be treated increases, and the required treatment capacity of the denitration device 7 must be increased. Further, the fuel cost consumed by the burner 5 is also large. Note that the reheating may be in an environment where high-pressure steam or in-house generated power can be used as a heat source.However, when the melting furnace is installed alone, such an environment is not used. However, it is often not advisable to use it because the power selling ability etc. is reduced. SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to solve the above problems and to provide an exhaust gas treatment apparatus for a melting furnace which can reduce running costs and equipment costs. [0005] For this purpose, an exhaust gas treatment apparatus for a melting furnace according to the present invention reduces the temperature of the exhaust gas by introducing outside air into the exhaust path of the melting furnace and diluting the exhaust gas. Providing a burner that guides the dust collector and bypasses a part of the exhaust gas on the secondary side of the dust collector to mix and burn the exhaust gas and the fuel; and burns the fuel based on oxygen in the exhaust gas introduced by the outside air. After the temperature of the exhaust gas is raised again, the exhaust gas is guided to a denitration apparatus. Next, an embodiment of the present invention will be described with reference to FIG. In the figure, 1 is a melting furnace, 2 is an exhaust passage thereof, 3 is a cooling means for introducing outside air to dilute exhaust gas from the exhaust passage and spraying water to take away heat of vaporization. It is a bag filter dust collector provided for removing dust from exhaust gas cooled to ° C.
Reference numeral 6 denotes a hot-air generating furnace provided with a burner 5, which supplies a fuel such as city gas to the burner 5, and also provides a bypass 11 in an exhaust path 10 connecting the dust collector 4 and the denitration device 7, and A part of the exhaust gas is guided from the secondary side to the burner 5 and mixed with the fuel, and the fuel is burned in the hot air generator 6 by the oxygen contained in the exhaust gas. The exhaust gas contains sufficient oxygen necessary for combustion since the outside air is introduced for cooling as described above. Thus, the hot air generated in the hot air generating furnace 6 is returned to the exhaust path 10 by the bypass path 12 and mixed with other exhaust gas so that the exhaust gas temperature becomes about 210 ° C. at which reductive denitration reaction is possible. It is led to the denitration device 7 for denitration and desulfurization.
The chimney 8 discharges into the atmosphere. As described above, a part of the exhaust gas is guided to the burner 5 so as to substitute for the combustion air, so that the amount of the exhaust gas to be treated by the denitration device 7 is not unnecessarily increased, and the fuel is not increased. Is also saved. By the way, Table 1 is shown in FIG.
2 shows the calculation results of the heat balance between the conventional apparatus shown in FIG. 1 and the apparatus of the present invention shown in FIG. Here, the specific heat of each gas is set to 0.34 (kcal / Nm 3 · ° C.), and the fuel is city gas 13A (lower calorific value 9940 (kcal /
Nm 3 )) and the theoretical air amount is 10.95 (m 3 / m
3 fuel gas), a combustion product of 12.05 (m 3 / m 3 fuel gas), a treatment exhaust gas amount of 17000 (Nm 3 / h), and an air ratio of 1.2. After dust collection, the exhaust gas temperature was set at 150 ° C. in consideration of dioxin resynthesis, and the temperature at the denitration apparatus was set at a general denitrification enable temperature of 210 ° C. The room temperature was set to 20 ° C., which was used as a reference temperature for calculation. As a result, in this device, 3
Energy reduction of 3307 kcal / h (8.7%) was achieved. [Table 1] FIG. 2 shows an embodiment in which the present invention is applied to a wet exhaust gas treatment apparatus provided with a salt washing tower 9 on the secondary side of the dust collector 4. In this case, since the exhaust gas temperature on the secondary side of the salt washing tower 9 is as low as 50 ° C., the fuel saving rate in the burner 5 becomes more remarkable. Table 2 also shows the results of calculating the heat balance between the conventional apparatus shown in FIG. 4 and the apparatus of the present invention shown in FIG. 2 under the same conditions as in Table 1. As a result, in this apparatus, 88820 kcal / h (8.7)
%). [Table 2] In the embodiment shown in FIGS. 1 and 2, the hot air generator 6 is provided, but in the present invention, the burner 5 is directly attached to the exhaust path 10 without using the hot air generator, and You may make it burn. As described above, the exhaust gas treatment apparatus for a melting furnace according to the present invention is provided with a burner for bypassing a part of the exhaust gas on the secondary side of the dust collector and mixing and burning the exhaust gas and the fuel. Since the temperature of the exhaust gas is raised again by burning the fuel based on the oxygen in the exhaust gas introduced by the above, the fuel for reheating can be saved, the running cost can be reduced, and the denitration apparatus can be used. Since the amount of exhaust gas requiring treatment is not increased as in the conventional case, there is a beneficial effect such as a reduction in equipment costs.

【図面の簡単な説明】 【図1】本発明に係る溶融炉の排ガス処理装置の実施形
態を示した排ガス系統図。 【図2】本発明に係る溶融炉の排ガス処理装置の他の実
施形態を示した排ガス系統図。 【図3】従来の溶融炉の排ガス処理装置の排ガス系統
図。 【図4】従来の溶融炉の排ガス処理装置の排ガス系統
図。 【符号の説明】 1 溶融炉 2 排気道 3 冷却手段 4 集塵機 5 バーナ 6 熱風発生炉 7 脱硝装置 9 洗塩塔 10 排気道 11 バイパス路
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an exhaust gas system diagram showing an embodiment of an exhaust gas treatment device for a melting furnace according to the present invention. FIG. 2 is an exhaust gas system diagram showing another embodiment of the exhaust gas treatment device for a melting furnace according to the present invention. FIG. 3 is an exhaust gas system diagram of a conventional exhaust gas treatment device for a melting furnace. FIG. 4 is an exhaust gas system diagram of a conventional exhaust gas treatment device for a melting furnace. [Description of Signs] 1 Melting furnace 2 Exhaust passage 3 Cooling means 4 Dust collector 5 Burner 6 Hot air generating furnace 7 Denitration device 9 Salt washing tower 10 Exhaust passage 11 Bypass passage

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3K065 AA24 AB03 HA01 HA02 HA03 3K070 DA02 DA03 DA07 DA09 DA22 DA23 DA27 DA37 DA47 DA56 3K078 BA03 CA02 CA07 CA24 4D048 AA02 AA06 CC26 CC52 CD02 CD03 CD08 DA01 DA06    ────────────────────────────────────────────────── ─── Continuation of front page    F term (reference) 3K065 AA24 AB03 HA01 HA02 HA03                 3K070 DA02 DA03 DA07 DA09 DA22                       DA23 DA27 DA37 DA47 DA56                 3K078 BA03 CA02 CA07 CA24                 4D048 AA02 AA06 CC26 CC52 CD02                       CD03 CD08 DA01 DA06

Claims (1)

【特許請求の範囲】 【請求項1】 溶融炉の排気道に外気を導入し排ガスを
希釈することで該排ガスの温度を下げてから集塵機に導
くとともに、該集塵機の二次側の排ガスの一部を迂回さ
せ該排ガスと燃料とを混合燃焼させるバーナを設け前記
外気によって導入された排ガス中の酸素を基に該燃料を
燃焼させることで該排ガスの温度を再上昇させた後、該
排ガスを脱硝装置に導くことを特徴とした溶融炉の排ガ
ス処理装置。
Claims 1. An outside air is introduced into an exhaust passage of a melting furnace to dilute the exhaust gas, thereby lowering the temperature of the exhaust gas, leading the exhaust gas to a dust collector, and extracting one of the exhaust gas on the secondary side of the dust collector. After providing a burner for bypassing the section and mixing and burning the exhaust gas and the fuel, the temperature of the exhaust gas is raised again by burning the fuel based on the oxygen in the exhaust gas introduced by the outside air, and then removing the exhaust gas. An exhaust gas treatment device for a melting furnace, which is led to a denitration device.
JP2001341045A 2001-11-06 2001-11-06 Exhaust gas treatment device for melting furnace Pending JP2003148719A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001341045A JP2003148719A (en) 2001-11-06 2001-11-06 Exhaust gas treatment device for melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001341045A JP2003148719A (en) 2001-11-06 2001-11-06 Exhaust gas treatment device for melting furnace

Publications (1)

Publication Number Publication Date
JP2003148719A true JP2003148719A (en) 2003-05-21

Family

ID=19155152

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001341045A Pending JP2003148719A (en) 2001-11-06 2001-11-06 Exhaust gas treatment device for melting furnace

Country Status (1)

Country Link
JP (1) JP2003148719A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007127355A (en) * 2005-11-04 2007-05-24 Takuma Co Ltd Rubbish incinerating/melting method and device therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007127355A (en) * 2005-11-04 2007-05-24 Takuma Co Ltd Rubbish incinerating/melting method and device therefor

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