JPH04115234U - Garbage incinerator exhaust equipment - Google Patents
Garbage incinerator exhaust equipmentInfo
- Publication number
- JPH04115234U JPH04115234U JP2135391U JP2135391U JPH04115234U JP H04115234 U JPH04115234 U JP H04115234U JP 2135391 U JP2135391 U JP 2135391U JP 2135391 U JP2135391 U JP 2135391U JP H04115234 U JPH04115234 U JP H04115234U
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- air
- temperature
- temperature adjustment
- dust collector
- 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.)
- Granted
Links
- 239000000428 dust Substances 0.000 claims abstract description 43
- 238000001816 cooling Methods 0.000 claims abstract description 35
- 239000002699 waste material Substances 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000007789 gas Substances 0.000 claims description 96
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract 1
- 239000012717 electrostatic precipitator Substances 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 5
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 206010021143 Hypoxia Diseases 0.000 description 2
- 150000002013 dioxins Chemical class 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- YEBIHIICWDDQOL-YBHNRIQQSA-N polyoxin Chemical compound O[C@@H]1[C@H](O)[C@@H](C(C=O)N)O[C@H]1N1C(=O)NC(=O)C(C(O)=O)=C1 YEBIHIICWDDQOL-YBHNRIQQSA-N 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Chimneys And Flues (AREA)
- Treating Waste Gases (AREA)
Abstract
(57)【要約】
【目的】 既存の設備に対しても僅かな改良によってダ
イオキシンの発生を抑制・防止し得るようにする。
【構成】 ごみ焼却炉1で発生した排ガスを煙突3へ導
く排ガスダクト2の途中に、水5を噴射して排ガスを冷
却するガス冷却室4を設け、排ガスダクト2のガス冷却
室4の出側に、ごみ焼却炉1へ送る一次空気と排ガスと
の間で熱交換を行う空気予熱器11を設け、排ガスダク
ト2の空気予熱器11の出側に集塵機21を設け、空気
予熱器11と集塵機21との間に温度調整用空気調節弁
14を備えて温度調整用空気を送給するようにした温度
調整用空気送給路13を接続すると共に、集塵機21入
側の排ガスの温度を検出して温度調整用空気調節弁14
の開度を調節する温度調節計15を設ける。
(57) [Summary] [Purpose] To suppress and prevent the generation of dioxin by making slight improvements to existing equipment. [Structure] A gas cooling chamber 4 that injects water 5 to cool the exhaust gas is provided in the middle of the exhaust gas duct 2 that guides the exhaust gas generated in the garbage incinerator 1 to the chimney 3. An air preheater 11 is provided on the side to perform heat exchange between the primary air sent to the waste incinerator 1 and exhaust gas, and a dust collector 21 is provided on the outlet side of the air preheater 11 of the exhaust gas duct 2. A temperature adjustment air supply path 13 equipped with a temperature adjustment air control valve 14 to supply temperature adjustment air is connected between the dust collector 21 and the temperature of the exhaust gas on the inlet side of the dust collector 21 is detected. Air control valve 14 for temperature adjustment
A temperature controller 15 is provided to adjust the degree of opening.
Description
【0001】0001
本考案は、ごみ焼却炉の排気設備に関するものである。 The present invention relates to exhaust equipment for waste incinerators.
【0002】0002
一般に、ごみ焼却炉で都市ごみなどを燃やして生成された750〜950℃の 排ガスは、排ガスダクトを通って先ずガス冷却室へ導かれ、該ガス冷却室で排気 設備の高温腐食を防止するため水を噴射されて300〜350℃まで冷却され、 次に空気予熱器へ導かれて、該空気予熱器で焼却炉へ供給される燃焼用の一次空 気との間で熱交換され一次空気を200〜250℃まで昇温すると共に自らは3 00℃まで降温され、続いて電気集塵機で集塵された後、煙突から排出されてい る。 Generally, the temperature of 750 to 950℃ is generated by burning municipal waste in a garbage incinerator. The exhaust gas is first led to the gas cooling chamber through the exhaust gas duct, and is exhausted in the gas cooling chamber. In order to prevent high-temperature corrosion of equipment, water is sprayed to cool it to 300-350℃, The primary air for combustion is then led to an air preheater, where it is supplied to the incinerator. Heat is exchanged with the air, raising the temperature of the primary air to 200 to 250℃, and increasing the temperature of the primary air to 3 The temperature is lowered to 00℃, the dust is collected using an electrostatic precipitator, and then discharged from the chimney. Ru.
【0003】 尚、電気集塵機の入口における排ガスの温度を300℃としているのは、空気 予熱器において一次空気を200〜250℃まで予熱し得るようにするため及び ダストの固有抵抗値の関係から300℃付近で最も性能を発揮する電気集塵機を 使用しているためである。0003 The temperature of the exhaust gas at the inlet of the electrostatic precipitator is set at 300°C because the air To enable primary air to be preheated to 200 to 250°C in a preheater and An electrostatic precipitator that performs best at around 300℃ is selected based on the specific resistance value of dust. This is because it is used.
【0004】 ところで、環境汚染物質として有名であり非常に毒性の強いダイオキシンは、 都市ごみなどの不完全燃焼生成物からもダスト成分の触媒作用を受けて新たに合 成されるものと考えられており、該ダイオキシンは図2に示すように、電気集塵 機内の300℃付近の温度で最も発生量が多いことが近年わかってきた。0004 By the way, dioxin is a highly toxic and well-known environmental pollutant. Incomplete combustion products such as municipal waste are also synthesized under the catalytic action of dust components. As shown in Figure 2, the dioxins are In recent years, it has been discovered that the highest amount of dust is generated at temperatures around 300 degrees Celsius inside aircraft cabins.
【0005】 しかるに、上記従来のごみ焼却炉の排気設備では電気集塵機の入口における排 ガスの温度を300℃と設定しているので、この部分がダイオキシンの発生原因 となるおそれがある。[0005] However, with the conventional waste incinerator exhaust equipment mentioned above, the exhaust at the entrance of the electrostatic precipitator is Since the gas temperature is set at 300℃, this part is the cause of dioxin generation. There is a risk that
【0006】 そこで、電気集塵機の入口における排ガスの温度が300℃以下となるように するために、ガス冷却室内部に噴射する水の量を増やし、ガス冷却室で排ガスの 温度を大幅に降下させることが検討されている。[0006] Therefore, the temperature of the exhaust gas at the inlet of the electrostatic precipitator is kept below 300℃. In order to increase the amount of water injected into the gas cooling chamber, Consideration is being given to significantly lowering the temperature.
【0007】[0007]
しかしながら、電気集塵機の入口における排ガスの温度を300℃以下とする ために、単にガス冷却室内部に噴射する水の量を増やすようにした場合には、以 下のような問題があった。 However, the temperature of the exhaust gas at the inlet of the electrostatic precipitator should be 300℃ or less. If you simply increase the amount of water injected into the gas cooling chamber in order to I had the following problem.
【0008】 即ち、噴射する水の量を増やすためにはガス冷却室やポンプ、ノズル等の容量 を増やさなければならず、しかも、ガス冷却室内部に噴射する水の量を増やすと 噴射した多量の水を排ガスで完全に蒸発させることが困難となってダストが湿っ てガス冷却室の運転に支障を生じたり排気設備に結露を生じたりする。[0008] In other words, in order to increase the amount of water injected, the capacity of the gas cooling chamber, pump, nozzle, etc. In addition, if the amount of water injected into the gas cooling chamber is increased, It becomes difficult for the exhaust gas to completely evaporate the large amount of water that is injected, and the dust becomes damp. This may interfere with the operation of the gas cooling room or cause condensation on the exhaust equipment.
【0009】 又、空気予熱器入口における排ガス温度も大幅に下がるので、ガス冷却室で排 ガスの温度を大幅に下げてしまうと、後段の空気予熱器で一次空気を200〜2 50℃まで予熱することができなくなってしまう。[0009] In addition, the exhaust gas temperature at the air preheater inlet also drops significantly, so the exhaust gas temperature in the gas cooling room is If the gas temperature is significantly lowered, the air preheater in the latter stage will heat the primary air to 200~200℃. It becomes impossible to preheat to 50°C.
【0010】 更に、ガス冷却室内部に噴射する水の量を増やすと排ガス中の水分の量或いは 割合が大幅に増加することになるので、排気設備が腐食を起こし易くなり、しか も、煙突から排出される排ガスが白煙となっていわゆる可視公害を引起こし易く なる。0010 Furthermore, if the amount of water injected into the gas cooling chamber is increased, the amount of moisture in the exhaust gas or The proportion will increase significantly, making the exhaust equipment more susceptible to corrosion and However, the exhaust gas emitted from chimneys becomes white smoke and easily causes so-called visible pollution. Become.
【0011】 従って、既設のごみ焼却炉に適用する場合には、上記問題が解決されるよう排 気設備全体を大幅に改造しなければならない。[0011] Therefore, when applying it to an existing waste incinerator, it is necessary to The entire air system would have to be significantly remodeled.
【0012】 本考案は、上述の実情に鑑み、既存の設備に対しても僅かな改良によってダイ オキシンの発生を抑制・防止し得るようにしたごみ焼却炉の排気設備を提供する ことを目的とするものである。0012 In view of the above-mentioned circumstances, the present invention has been developed to improve the efficiency of existing equipment by making slight improvements. To provide exhaust equipment for waste incinerators that can suppress and prevent the generation of oxins. The purpose is to
【0013】[0013]
請求項1の考案は、ごみ焼却炉で発生した排ガスを煙突へ導く排ガスダクトの 途中に、水を噴射して排ガスを冷却するガス冷却室を設け、排ガスダクトのガス 冷却室の出側に、ごみ焼却炉へ送給する一次空気と排ガスとの間で熱交換を行う 空気予熱器を設け、排ガスダクトの空気予熱器の出側に集塵機を設け、空気予熱 器と集塵機との間に温度調整用空気調節弁を備えて温度調整用空気を送給するよ うにした温度調整用空気送給路を接続すると共に、集塵機入側の排ガスの温度を 検出して温度調整用空気調節弁の開度を調節する温度調節計を設けたことを特徴 とするごみ焼却炉の排気設備にかかるものである。 The invention of claim 1 is based on an exhaust gas duct that guides exhaust gas generated in a garbage incinerator to a chimney. A gas cooling chamber is installed in the middle of the exhaust gas duct to cool the exhaust gas by injecting water. At the exit side of the cooling room, heat exchange is performed between the primary air sent to the waste incinerator and the exhaust gas. An air preheater is installed, and a dust collector is installed on the outlet side of the air preheater in the exhaust gas duct to prevent air preheating. A temperature adjustment air control valve is installed between the dust collector and the dust collector to supply temperature adjustment air. In addition to connecting the air supply path for temperature adjustment, the temperature of the exhaust gas at the entrance of the dust collector is Features a temperature controller that detects the temperature and adjusts the opening of the air control valve. This is related to exhaust equipment for waste incinerators.
【0014】 請求項2の考案は、温度調整用空気送給路の吸引側を高温になりやすい部屋や 酸欠になりやすい部屋やばい塵が発生する部屋やばい塵対策が必要な機器等のう ち少くとも一つに接続したごみ焼却炉の排気設備にかかるものである。[0014] The invention of claim 2 is such that the suction side of the air supply path for temperature adjustment is located in a room where the temperature tends to be high. Rooms that are prone to oxygen deficiency, rooms that generate dust, and equipment that requires dust countermeasures. This applies to the exhaust equipment of at least one connected waste incinerator.
【0015】[0015]
請求項1の考案によれば、ごみ焼却炉で発生した排ガスは、先ず、ガス冷却室 へ導かれてガス冷却室で水を噴射されることにより冷却され、次に、空気予熱器 へ導かれて空気予熱器でごみ焼却炉へ送給される一次空気との間で熱交換され、 更に、温度調整用空気送給路を介して送給される温度調整用空気を混合されて冷 却された後、集塵機で集塵され、最後に煙突から大気へ放出される。 According to the invention of claim 1, the exhaust gas generated in the waste incinerator is first passed through the gas cooling chamber. It is cooled by injecting water in the gas cooling chamber, and then the air preheater The air is guided through the air preheater and exchanged heat with the primary air that is sent to the waste incinerator. Furthermore, the temperature adjustment air sent through the temperature adjustment air supply path is mixed and cooled. After that, the dust is collected by a dust collector and finally released into the atmosphere through the chimney.
【0016】 この際、集塵機入側の排ガスの温度が温度調節計により検出され、温度調節計 が温度調整用空気調節弁の開度を調節することにより、集塵機入側の排ガスの温 度が200℃以下に制御される。[0016] At this time, the temperature of the exhaust gas on the inlet side of the dust collector is detected by the temperature controller; The temperature of the exhaust gas on the inlet side of the dust collector is adjusted by adjusting the opening degree of the temperature adjustment air control valve. temperature is controlled to below 200°C.
【0017】 請求項2記載の考案によれば、高温になりやすい部屋や酸欠になりやすい部屋 やばい塵が発生する部屋やばい塵対策が必要な機器等のうちの少くとも一つから 温度調整用空気送給路を介して温度調整用空気が排ガスダクトへ送給される。[0017] According to the invention described in claim 2, a room that tends to get high temperature or a room that tends to lack oxygen. From at least one of the rooms where hazardous dust is generated or equipment that requires dust countermeasures. Temperature-adjusting air is fed to the exhaust gas duct via the temperature-adjusting air supply path.
【0018】[0018]
以下、本考案の実施例を図面を参照しつつ説明する。 Embodiments of the present invention will be described below with reference to the drawings.
【0019】 図1は、本考案の一実施例である。[0019] FIG. 1 shows an embodiment of the present invention.
【0020】 図中1は都市ごみなどを燃やすためのごみ焼却炉、2はごみ焼却炉1で都市ご みなどを燃やして生成された排ガスを煙突3へ導く排ガスダクトである。[0020] In the figure, 1 is a garbage incinerator for burning municipal waste, and 2 is a garbage incinerator 1 for urban use. This is an exhaust gas duct that guides exhaust gas generated by burning ash, etc. to the chimney 3.
【0021】 排ガスダクト2の途中にガス冷却室4を設け、ガス冷却室4にガス冷却室4内 部へ排ガス冷却用の水を噴射するための水供給路6を接続し、水供給路6の途中 に水供給路6を流れる水5の量を調節する水量調節弁7を設け、排ガスダクト2 のガス冷却室4出側に、ガス冷却室4を出た排ガスの温度に基づいて水量調節弁 7の開度を調節する温度調節計8を設ける。[0021] A gas cooling chamber 4 is provided in the middle of the exhaust gas duct 2. A water supply path 6 for injecting water for exhaust gas cooling is connected to the A water flow control valve 7 is provided in the exhaust gas duct 2 to adjust the amount of water 5 flowing through the water supply path 6. A water flow control valve is installed on the outlet side of the gas cooling chamber 4 based on the temperature of the exhaust gas exiting the gas cooling chamber 4. A temperature controller 8 is provided to adjust the opening degree of 7.
【0022】 又、排ガスダクト2の温度調節計8接続部分よりも排ガスの流れ方向下流側に 、一次送風機9から一次空気供給路10を介してごみ焼却炉1へ送給される燃焼 用の一次空気と排ガスとの間で熱交換を行い、一次空気を予熱する空気予熱器1 1を設け、排ガスダクト2の空気予熱器11出側に温度調整用送風機12からの 温度調整用空気を供給する温度調整用空気供給路13を接続し、温度調整用空気 供給路13の途中に温度調整用空気供給路13を流れる温度調整用空気の量を調 節する温度調整用空気調整弁14を設け、排ガスダクト2の温度調整用空気供給 路13接続部分よりも排ガスの流れ方向下流側に、排ガスダクト2を流れる排ガ スの温度に基づいて温度調整用空気調整弁14の開度を調節する温度調節計15 を設けると共に、温度調整用送風機12の吸引側を、ごみ焼却炉1を収容する炉 室16等の高温になりやすい部屋や、排水処理室17等の酸欠になりやすい部屋 や、灰出し室18等のばい塵が発生する部屋や、灰コンベヤ19及び灰バンカ2 0等のばい塵対策が必要な機器などへ接続する。[0022] Also, on the downstream side in the flow direction of exhaust gas from the connection part of temperature controller 8 of exhaust gas duct 2. , combustion is supplied from the primary blower 9 to the waste incinerator 1 via the primary air supply path 10. Air preheater 1 that performs heat exchange between primary air and exhaust gas to preheat primary air. 1 is installed, and a temperature adjustment blower 12 is installed on the outlet side of the air preheater 11 of the exhaust gas duct 2. Connect the temperature adjustment air supply path 13 that supplies temperature adjustment air, and The amount of temperature adjustment air flowing through the temperature adjustment air supply path 13 is adjusted in the middle of the supply path 13. A temperature regulating air regulating valve 14 is provided to control the temperature regulating air supply to the exhaust gas duct 2. The exhaust gas flowing through the exhaust gas duct 2 is located on the downstream side in the flow direction of the exhaust gas than the connecting portion of the passage 13. A temperature controller 15 that adjusts the opening degree of the temperature adjusting air regulating valve 14 based on the temperature of the In addition, the suction side of the temperature adjustment blower 12 is connected to the furnace that houses the waste incinerator 1. Rooms that tend to get hot, such as room 16, and rooms that tend to be oxygen deficient, such as wastewater treatment room 17. , rooms where dust is generated such as the ash removal room 18, the ash conveyor 19 and the ash bunker 2. Connect to equipment that requires measures against dust such as zero.
【0023】 排ガスダクト2の温度調節計15接続部分よりも排ガスの流れ方向下流側に、 バグフィルタ式の集塵機21を設ける。[0023] On the downstream side in the exhaust gas flow direction from the temperature controller 15 connection part of the exhaust gas duct 2, A bag filter type dust collector 21 is provided.
【0024】 尚、図中22は二次送風機23からごみ焼却炉1へ、ごみ焼却炉1内の都市ご みの燃焼を助長すると共に焼却炉1内の温度が極端に上昇しないようにするため の二次空気を送給する二次空気供給路である。[0024] In addition, 22 in the figure is from the secondary blower 23 to the garbage incinerator 1, and the city inside the garbage incinerator 1. In order to promote the combustion of waste and to prevent the temperature inside the incinerator 1 from rising excessively. This is a secondary air supply path that supplies secondary air.
【0025】 次に、作動について説明する。[0025] Next, the operation will be explained.
【0026】 先ず、温度調節計8の設定温度を350℃程度とし、温度調節計15の設定温 度を200℃以下とする。[0026] First, the set temperature of the temperature controller 8 is set to about 350°C, and the set temperature of the temperature controller 15 is set to about 350°C. The temperature should be 200℃ or less.
【0027】 そして、一次送風機9から一次空気供給路10を介してごみ焼却炉1へ送給し ごみ焼却炉1で都市ごみなどを燃焼させる。[0027] Then, the air is supplied from the primary blower 9 to the waste incinerator 1 via the primary air supply path 10. Municipal waste, etc. is burned in the waste incinerator 1.
【0028】 ごみ焼却炉1で都市ごみなどが燃焼されて生成された排ガスの温度は750〜 950℃となり、該750〜950℃の排ガスは、排ガスダクト2を通って先ず ガス冷却室4へ導かれ、該ガス冷却室4で排気設備の高温腐食を防止するため、 水供給路6からの水5を噴射されて300〜350℃即ち300℃以上の温度ま で冷却される。[0028] The temperature of the exhaust gas generated when municipal waste is burned in the garbage incinerator 1 is 750~ 950℃, and the exhaust gas at 750 to 950℃ first passes through the exhaust gas duct 2. In order to prevent high-temperature corrosion of exhaust equipment in the gas cooling chamber 4, The water 5 from the water supply path 6 is injected to a temperature of 300 to 350℃, that is, 300℃ or more. cooled down.
【0029】 この時、温度調節計8がガス冷却室4出側の排ガスの温度を検出して水量調節 弁7の開度を調整することによって、該ガス冷却室4出側の排ガスの温度が30 0〜350℃となるようガス冷却室4へ噴射される水5の量が制御される。[0029] At this time, the temperature controller 8 detects the temperature of the exhaust gas on the outlet side of the gas cooling chamber 4 and adjusts the water amount. By adjusting the opening degree of the valve 7, the temperature of the exhaust gas on the outlet side of the gas cooling chamber 4 can be adjusted to 30°C. The amount of water 5 injected into the gas cooling chamber 4 is controlled so that the temperature is 0 to 350°C.
【0030】 このように、ガス冷却室4出側の排ガスの温度を従来と同様300〜350℃ まで冷却するに止めているので、ガス冷却室4へ噴射する水5の量を増やさずに 済み、その結果、ガス冷却室4の容量を大きくする必要をなくすことができ、且 つ、従来通り噴射した水5をガス冷却室4内部で完全に蒸発させることができる 。[0030] In this way, the temperature of the exhaust gas on the outlet side of the gas cooling chamber 4 is kept at 300 to 350°C, the same as before. The amount of water 5 injected into the gas cooling chamber 4 does not need to be increased. As a result, it is possible to eliminate the need to increase the capacity of the gas cooling chamber 4, and First, the water 5 injected as before can be completely evaporated inside the gas cooling chamber 4. .
【0031】 ガス冷却室4で300〜350℃即ち300℃以上まで冷却された排ガスは、 次に空気予熱器11へ導かれて、該空気予熱器11で一次送風機9から一次空気 供給路10を介してごみ焼却炉1へ供給される燃焼用の一次空気との間で熱交換 され、従来と同様、一次空気を200〜250℃まで昇温すると共に自らは30 0℃まで降温される。[0031] The exhaust gas cooled to 300 to 350°C, that is, 300°C or more in the gas cooling chamber 4, is Next, the primary air is guided to the air preheater 11 from the primary blower 9 in the air preheater 11. Heat exchange with primary air for combustion supplied to the waste incinerator 1 via the supply path 10 As before, the temperature of the primary air is raised to 200 to 250℃, and the temperature of the primary air is increased to 30℃. The temperature is lowered to 0°C.
【0032】 空気予熱器11で300℃まで降温された排ガスは、その後、温度調整用送風 機12から温度調整用空気供給路13を介して送給される温度調整用空気を混合 されて直ちに200℃以下まで冷却され、且つ冷却により排ガス及び温度調整用 空気の混合ガスが減容される。[0032] The exhaust gas whose temperature has been lowered to 300°C by the air preheater 11 is then sent to a temperature-adjusting air blower. The temperature adjustment air sent from the machine 12 through the temperature adjustment air supply path 13 is mixed. It is immediately cooled down to 200℃ or less, and is used for exhaust gas and temperature adjustment by cooling. The air mixture is reduced in volume.
【0033】 この時、排ガスダクト2へ噴射される温度調整用空気の量は、温度調節計15 が排ガスダクト2の温度調整用空気供給路13接続部下流側の排ガスの温度を検 出して、接続部下流側の排ガスの温度が200℃以下となるよう温度調整用空気 調整弁14の開度を調整することによって制御される。[0033] At this time, the amount of temperature adjustment air injected into the exhaust gas duct 2 is determined by the temperature controller 15. detects the temperature of the exhaust gas on the downstream side of the connection part of the temperature adjustment air supply path 13 of the exhaust gas duct 2. Temperature adjusting air is supplied so that the temperature of the exhaust gas on the downstream side of the connection is 200℃ or less. It is controlled by adjusting the opening degree of the regulating valve 14.
【0034】 又、温度調整用送風機12の吸引側を、ごみ焼却炉1を収容する炉室16等の 高温になりやすい部屋や、排水処理室17等の酸欠になりやすい部屋や、灰出し 室18等のばい塵が発生する部屋や、灰コンベヤ19及び灰バンカ20等のばい 塵対策が必要な機器などへ接続しているので、これら各部屋や機器に独立して設 けていた換気装置や集塵機が集約されて不要化される。[0034] In addition, the suction side of the temperature adjustment blower 12 is connected to the furnace chamber 16 etc. that accommodates the waste incinerator 1. Rooms that are prone to high temperatures, rooms that are prone to oxygen deficiency such as wastewater treatment room 17, and ash removal Rooms where dust is generated such as room 18, dust conveyor 19 and ash bunker 20, etc. Since it is connected to equipment that requires dust countermeasures, it is necessary to install it separately in each room and equipment. Ventilators and dust collectors that were previously installed will be consolidated and become unnecessary.
【0035】 200℃以下まで冷却された排ガスは、従来の電気集塵機では充分な集塵性能 が得られないため、バグフィルタ式の集塵機21を設け、排ガスと温度調整用空 気の混合ガスを集塵機21へ導いて集塵機21で集塵するようにした後、煙突3 から排出させる。[0035] Exhaust gas cooled to below 200°C has sufficient dust collection performance with conventional electrostatic precipitators. Since this is not possible, a bag filter type dust collector 21 is installed to collect exhaust gas and air After the mixed gas is guided to the dust collector 21 and collected by the dust collector 21, the chimney 3 discharge from.
【0036】 このように、空気予熱器11から出て集塵機21へ導入される排ガスを温度調 整用空気で直ちに200℃以下まで冷却するようにしたことにより、集塵機21 内でのダイオキシンの発生が抑制・防止され、且つ、この時の冷却によって温度 調整用空気及び排ガスの体積は減少されるので、実ガス量は増えても従来に比べ て集塵機21の容量をそれほど大きくする必要がない。[0036] In this way, the temperature of the exhaust gas that comes out of the air preheater 11 and is introduced into the dust collector 21 is controlled. By immediately cooling the dust collector to below 200°C with maintenance air, the dust collector 21 The generation of dioxin is suppressed and prevented, and the cooling at this time reduces the temperature. The volumes of conditioning air and exhaust gas are reduced, so even if the actual gas volume increases, it will be smaller than before. Therefore, there is no need to increase the capacity of the dust collector 21 so much.
【0037】 しかも、排ガスに温度調整用空気を混合したことにより、ガス中の水分濃度が 低下する傾向になるので、結露や腐食や白煙による可視公害などが発生しにくく なる。[0037] Moreover, by mixing temperature-adjusting air with the exhaust gas, the moisture concentration in the gas is reduced. As the temperature tends to decrease, visible pollution due to condensation, corrosion, and white smoke is less likely to occur. Become.
【0038】 尚、本考案は、上述の実施例にのみ限定されるものではなく、既設炉に対して は空気で250℃程度に冷却することにより電気集塵機を使用することも可能で あること、その他、本考案の要旨を逸脱しない範囲内において種々変更を加え得 ることは勿論である。[0038] Note that the present invention is not limited to the above-mentioned embodiments, and can be applied to existing furnaces. It is also possible to use an electrostatic precipitator by cooling it with air to about 250℃. However, other changes may be made without departing from the gist of the invention. Of course.
【0039】[0039]
以上説明したように、請求項1の考案にかかるごみ焼却炉の排気設備によれば 、集塵機入口において排ガスに温度調整用空気を混合することにより集塵機入口 温度を200℃程度まで下げられるようにしたので、既設の設備をほとんど改造 することなくダイオキシンの発生を抑制・防止することができ、しかも、ガス冷 却室内部に噴射する水の量を増やした場合に比べて、一次空気を200〜250 ℃まで予熱することができ、且つ、結露や腐食や可視公害などの問題を防止する ことができるという優れた効果を奏し得る。 As explained above, according to the waste incinerator exhaust equipment according to the invention of claim 1, , by mixing temperature-adjusting air with the exhaust gas at the dust collector inlet. Since the temperature can be lowered to around 200℃, most of the existing equipment has to be modified. It is possible to suppress and prevent the generation of dioxins without Compared to increasing the amount of water injected into the cooling chamber, the primary air Can be preheated to ℃ and prevents problems such as condensation, corrosion, and visible pollution. This has the excellent effect of being able to.
【0040】 請求項2の考案にかかるごみ焼却炉の排気設備によれば、換気装置や集塵機を 集約して不要化できるという優れた効果を奏し得る。[0040] According to the waste incinerator exhaust equipment according to the invention of claim 2, a ventilation system and a dust collector are not required. It has the excellent effect of being able to consolidate and eliminate the need.
【図1】本考案の一実施例の全体系統図である。FIG. 1 is an overall system diagram of an embodiment of the present invention.
【図2】温度とダイオキシン発生量との関係を示すグラ
フである。FIG. 2 is a graph showing the relationship between temperature and amount of dioxin generated.
1 ごみ焼却炉 2 排ガスダクト 3 煙突 4 ガス冷却室 5 水 10 一次空気供給路 11 空気予熱器 13 温度調整用空気送給路 14 温度調整用空気調節弁 15 温度調節計 16 炉室 17 排水処理室 18 灰出し室 19 灰コンベヤ 20 灰バンカ 21 集塵機 1 Garbage incinerator 2 Exhaust gas duct 3 chimney 4 Gas cooling room 5 Water 10 Primary air supply path 11 Air preheater 13 Air supply path for temperature adjustment 14 Air control valve for temperature adjustment 15 Temperature controller 16 Furnace room 17 Wastewater treatment room 18 Ash removal room 19 Ash conveyor 20 Ash Banka 21 Dust collector
Claims (2)
く排ガスダクトの途中に、水を噴射して排ガスを冷却す
るガス冷却室を設け、排ガスダクトのガス冷却室の出側
に、ごみ焼却炉へ送給する一次空気と排ガスとの間で熱
交換を行う空気予熱器を設け、排ガスダクトの空気予熱
器の出側に集塵機を設け、空気予熱器と集塵機との間に
温度調整用空気調節弁を備えて温度調整用空気を送給す
るようにした温度調整用空気送給路を接続すると共に、
集塵機入側の排ガスの温度を検出して温度調整用空気調
節弁の開度を調節する温度調節計を設けたことを特徴と
するごみ焼却炉の排気設備。[Claim 1] A gas cooling chamber that injects water to cool the exhaust gas is provided in the middle of the exhaust gas duct that leads the exhaust gas generated in the garbage incinerator to the chimney, and a garbage incineration chamber is provided on the outlet side of the gas cooling chamber of the exhaust gas duct. An air preheater is installed to exchange heat between the primary air fed to the furnace and the exhaust gas, a dust collector is installed on the outlet side of the air preheater in the exhaust gas duct, and temperature adjustment air is installed between the air preheater and the dust collector. In addition to connecting a temperature adjustment air supply path equipped with a control valve to supply temperature adjustment air,
1. Exhaust equipment for a waste incinerator, characterized by being equipped with a temperature controller that detects the temperature of exhaust gas on the inlet side of a dust collector and adjusts the opening degree of an air control valve for temperature adjustment.
なりやすい部屋や酸欠になりやすい部屋やばい塵が発生
する部屋やばい塵対策が必要な機器等のうち少くとも一
つに接続した請求項1記載のごみ焼却炉の排気設備。[Claim 2] Connect the suction side of the air supply path for temperature adjustment to at least one of the following: a room that tends to get hot, a room that tends to lack oxygen, a room that generates dust, a device that requires dust countermeasures, etc. The exhaust equipment for a waste incinerator according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2135391U JPH0749231Y2 (en) | 1991-03-11 | 1991-03-11 | Exhaust equipment for refuse incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2135391U JPH0749231Y2 (en) | 1991-03-11 | 1991-03-11 | Exhaust equipment for refuse incinerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04115234U true JPH04115234U (en) | 1992-10-13 |
JPH0749231Y2 JPH0749231Y2 (en) | 1995-11-13 |
Family
ID=31907127
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2135391U Expired - Lifetime JPH0749231Y2 (en) | 1991-03-11 | 1991-03-11 | Exhaust equipment for refuse incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0749231Y2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002079029A (en) * | 2000-09-07 | 2002-03-19 | Daido Steel Co Ltd | Method for cooling exhaust gas from melting furnace |
JP2023017514A (en) * | 2021-07-26 | 2023-02-07 | 株式会社タクマ | Exhaust gas treatment facility and exhaust gas treatment method |
-
1991
- 1991-03-11 JP JP2135391U patent/JPH0749231Y2/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002079029A (en) * | 2000-09-07 | 2002-03-19 | Daido Steel Co Ltd | Method for cooling exhaust gas from melting furnace |
JP4701485B2 (en) * | 2000-09-07 | 2011-06-15 | 大同特殊鋼株式会社 | Melting furnace exhaust gas cooling method |
JP2023017514A (en) * | 2021-07-26 | 2023-02-07 | 株式会社タクマ | Exhaust gas treatment facility and exhaust gas treatment method |
Also Published As
Publication number | Publication date |
---|---|
JPH0749231Y2 (en) | 1995-11-13 |
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