JP6058107B1 - Gas water washing device - Google Patents

Gas water washing device Download PDF

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JP6058107B1
JP6058107B1 JP2015234364A JP2015234364A JP6058107B1 JP 6058107 B1 JP6058107 B1 JP 6058107B1 JP 2015234364 A JP2015234364 A JP 2015234364A JP 2015234364 A JP2015234364 A JP 2015234364A JP 6058107 B1 JP6058107 B1 JP 6058107B1
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water
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precipitate
downstream pipe
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JP2017100072A (en
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優佑 前田
優佑 前田
利雄 濱
利雄 濱
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Hitachi Zosen Corp
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Abstract

【課題】排ガス中に含まれる水溶性成分を除去する水洗塔のガス導入部が当該水溶性成分の析出により閉塞されることを防止可能とするガス水洗装置を提供する。【解決手段】加熱処理ガス中の水溶性成分を水洗により除去する水洗塔20と、水洗塔20に排ガスを導入するガス導入部25の閉塞を防止する閉塞防止装置30と、を備え、閉塞防止装置30は、加熱処理ガスを加熱する加熱部33と、水溶性成分の析出物を除去する析出物除去部36と、を有するガス水洗装置10である。【選択図】図2To provide a gas water rinsing apparatus capable of preventing a gas introduction part of a water washing tower for removing water-soluble components contained in exhaust gas from being blocked by precipitation of the water-soluble components. A water washing tower 20 that removes water-soluble components in a heat treatment gas by water washing, and a clog prevention device 30 that prevents clogging of a gas introduction part 25 that introduces exhaust gas into the water washing tower 20 are provided to prevent clogging. The apparatus 30 is a gas water washing apparatus 10 having a heating unit 33 that heats the heat treatment gas and a precipitate removing unit 36 that removes precipitates of water-soluble components. [Selection] Figure 2

Description

本発明は、廃棄物焼却炉や溶融炉等の排ガスラインで捕集された飛灰の処理装置から排出される排ガスを水洗して、排ガス中に含まれる水溶性成分を除去するガス水洗装置に関する。   The present invention relates to a gas water rinsing apparatus for rinsing exhaust gas discharged from a processing apparatus for fly ash collected in an exhaust gas line such as a waste incinerator or melting furnace to remove water-soluble components contained in the exhaust gas. .

飛灰の処理装置から排出される排ガスには、排ガス処理に適した温度で処理する際に析出するアンモニウム塩類の水溶性成分が含まれている。この水溶性成分を除去するために、排ガスラインには、排ガスに水を噴射して水溶性成分を水に溶解させて除去する水洗塔が設けられている。   The exhaust gas discharged from the fly ash treatment apparatus contains a water-soluble component of ammonium salts that precipitates when processing at a temperature suitable for exhaust gas treatment. In order to remove this water-soluble component, the exhaust gas line is provided with a water washing tower for injecting water into the exhaust gas to dissolve and remove the water-soluble component in water.

特開2001−232324号公報JP 2001-232324 A

しかしながら、水洗塔に至る排ガスラインで排ガスが冷却されると、例えば、排ガス中に含まれるアンモニアガスと塩化水素とが結びついて塩化アンモニウムが生成し、水洗塔のガス導入部付近に析出してガス導入部を閉塞させる恐れがあった。   However, when the exhaust gas is cooled in the exhaust gas line leading to the water washing tower, for example, ammonia gas and hydrogen chloride contained in the exhaust gas are combined to produce ammonium chloride, which is deposited near the gas introduction part of the water washing tower and gas There was a risk of blocking the inlet.

そこで、本発明は、水洗塔のガス導入部が析出物に閉塞されることを防止することができるガス水洗装置を提供することを目的とする。   Then, an object of this invention is to provide the gas washing apparatus which can prevent that the gas introduction part of a washing tower is obstruct | occluded by a deposit.

本発明の解決しようとする課題は以上であり、次にこの課題を解決するための手段を説明する。   The problem to be solved by the present invention is as described above. Next, means for solving the problem will be described.

即ち、本発明に係るガス水洗装置は、飛灰を処理することにより発生する排ガス中の水溶性成分を水洗により除去する水洗塔と、前記水洗塔に排ガスを導入するガス導入部の閉塞を防止する閉塞防止装置と、前記ガス導入部の開口に対向して設けられる点検口と、を備え、前記閉塞防止装置は、排ガスを加熱する加熱部と、前記水溶性成分の析出物を除去する析出物除去部と、を有し、前記ガス導入部に設けられて前記水洗塔に一端部が接続される導入下流管に、前記析出物除去部を備え、前記ガス導入部に設けられて前記導入下流管の中間部に接続される導入上流管に、前記加熱部を備え、前記点検口は、前記ガス導入部の開口或いは前記導入下流管の内壁面を目視可能に構成されるものである。 That is, the gas water washing apparatus according to the present invention prevents clogging of a water washing tower that removes water-soluble components in exhaust gas generated by treating fly ash by water washing, and a gas introduction part that introduces exhaust gas into the water washing tower. A clogging prevention device, and an inspection port provided opposite to the opening of the gas introduction unit , wherein the clogging prevention device is a heating unit that heats exhaust gas, and a precipitate that removes precipitates of the water-soluble components. A deposit removing section, and provided in the gas introducing section and having one end connected to the water washing tower, the deposit removing section being provided in the gas introducing section and the introduction The introduction upstream pipe connected to the intermediate part of the downstream pipe is provided with the heating unit, and the inspection port is configured so that the opening of the gas introduction part or the inner wall surface of the introduction downstream pipe can be visually observed .

上記構成によれば、水洗塔での水洗によるガス水洗装置の全体の温度低下によるガス導入部の温度低下を抑えるために加熱部壁面の排ガスを加熱することで、水溶性成分の析出物の発生を未然に防止できる。さらに、水洗塔の内の水洗に伴うガス導入部の温度低下に伴って水溶性成分の析出物が発生すると、この析出物を析出物除去部により除去することができる。これにより、水洗塔のガス導入部の析出物による閉塞を防止できる。   According to the above configuration, the generation of precipitates of water-soluble components is generated by heating the exhaust gas on the wall surface of the heating unit in order to suppress the temperature decrease of the gas introduction unit due to the temperature decrease of the entire gas water rinsing device by rinsing in the rinsing tower. Can be prevented. Further, when a precipitate of a water-soluble component is generated as the temperature of the gas introduction part is lowered due to the water washing in the washing tower, the precipitate can be removed by the precipitate removing part. Thereby, obstruction | occlusion by the deposit of the gas introduction part of a washing tower can be prevented.

上記構成によれば、加熱部により加熱された導入上流管壁面での析出物の発生を抑制し、析出物除去部により導入下流管で析出し付着した水溶性成分の析出物を除去することにより、水洗塔のガス導入部の閉塞を効果的に防止できる。   According to the above configuration, generation of precipitates on the wall surface of the upstream inlet pipe heated by the heating unit is suppressed, and precipitates of the water-soluble components deposited and adhered to the downstream pipe by the precipitate removal unit are removed. The blockage of the gas introduction part of the washing tower can be effectively prevented.

本発明は、上記構成において、前記析出物除去部に、前記導入下流管の他端部に設置されて、前記一端部に向かって噴射水を噴射する噴射ノズルを有するものである。   In the above-described configuration, the present invention has an injection nozzle that is installed at the other end portion of the introduction downstream pipe in the deposit removing portion and injects spray water toward the one end portion.

上記構成によれば、噴射ノズルから噴射される噴射水により、水溶性成分の析出物を効果的に除去することができる。   According to the said structure, the deposit of a water-soluble component can be effectively removed with the injection water injected from an injection nozzle.

本発明は、上記構成において、前記閉塞防止装置が、析出物除去部における噴射水の噴
射時間及び噴射間隔のうち少なくとも一つを制御する除去制御部を有し、前記除去制御部は、前記ガス導入部の開口或いは前記導入下流管の内壁面に付着した析出物の析出量に基づいて前記噴射時間及び噴射間隔を制御するものである。
The present invention having the above structure, the closure prevention device, have a removal control unit for controlling at least one of the injection time and the injection interval of the injection water in the precipitate removal unit, the removal control unit, the gas The injection time and the injection interval are controlled based on the amount of precipitate deposited on the opening of the introduction part or the inner wall surface of the introduction downstream pipe .

上記構成によれば、除去制御部により析出物除去部における噴射水の噴射時間及び噴射間隔のうち少なくとも一つを制御することで、効率よく水洗塔のガス導入部の閉塞を防止できる。   According to the said structure, obstruction | occlusion of the gas introduction part of a water-washing tower can be efficiently prevented by controlling at least one among the injection time and the injection space | interval in the deposit removal part by a removal control part.

本発明によれば、排ガスに含まれる水溶性成分の析出物によって、水洗塔のガス導入部が閉塞されるのを未然に防止できる。   According to the present invention, it is possible to prevent the gas introduction part of the washing tower from being blocked by the precipitate of the water-soluble component contained in the exhaust gas.

本発明に係るガス水洗装置を備える飛灰加熱処理設備の構成を示す概略図である。It is the schematic which shows the structure of the fly ash heat processing equipment provided with the gas water washing apparatus which concerns on this invention. 本発明に係るガス水洗装置の正面断面図である。It is front sectional drawing of the gas water washing apparatus which concerns on this invention. 本発明に係るガス水洗装置における制御システムを示すブロック図である。It is a block diagram which shows the control system in the gas water washing apparatus which concerns on this invention.

まず、本発明に係るガス水洗装置10を備える飛灰加熱処理設備1について説明する。なお、本発明に係るガス水洗装置10は、以下に説明する飛灰加熱処理設備1に備えられるものに限定されるものではなく、廃棄物焼却炉や溶融炉等から排出される排ガスを処理する排ガス処理設備に備えられるものであっても構わない。   First, the fly ash heat treatment equipment 1 provided with the gas water washing apparatus 10 which concerns on this invention is demonstrated. In addition, the gas water washing apparatus 10 which concerns on this invention is not limited to what is provided in the fly ash heat processing equipment 1 demonstrated below, The exhaust gas discharged | emitted from a waste incinerator, a melting furnace, etc. is processed. It may be provided in the exhaust gas treatment facility.

図1に示すように、飛灰加熱処理設備1は、焼却設備の焼却炉(図示せず)等の排ガスラインで捕集した飛灰を加熱処理してダイオキシン類を分解する。飛灰加熱処理設備1は、飛灰を貯留する飛灰貯留ホッパ2と、飛灰を所定温度(例えば、350℃から400℃)まで加熱してダイオキシン類を分解する加熱器4と、加熱された飛灰を冷却する冷却器5と、加熱器4に設けられたダストフィルタ8から排ガス導入ライン9を介して導入された加熱処理ガス(「排ガス」の一例)を、水洗して水溶性成分を除去するガス水洗装置10と、ガス水洗装置10で水洗された加熱処理ガスを冷却するコンデンサ6と、ガス水洗装置10及びコンデンサ6から排出されて水溶性成分が溶け込んだ排水を受けるドレインタンク7と、を具備している。   As shown in FIG. 1, the fly ash heat treatment equipment 1 decomposes dioxins by heat-treating fly ash collected in an exhaust gas line such as an incinerator (not shown) of the incineration equipment. The fly ash heat treatment equipment 1 is heated by a fly ash storage hopper 2 that stores fly ash, a heater 4 that heats the fly ash to a predetermined temperature (for example, 350 ° C. to 400 ° C.) and decomposes dioxins. The heat treatment gas (an example of “exhaust gas”) introduced through the exhaust gas introduction line 9 from the cooler 5 for cooling the fly ash and the dust filter 8 provided in the heater 4 is washed with water to obtain a water-soluble component. A water rinsing apparatus 10 for removing water, a condenser 6 for cooling the heat-treated gas washed by the gas water rinsing apparatus 10, and a drain tank 7 for receiving waste water that is discharged from the gas water rinsing apparatus 10 and the condenser 6 and into which water-soluble components are dissolved. And.

次に、本発明に係るガス水洗装置10を、図2を参照して説明する
このガス水洗装置10は、加熱処理ガス中に含まれる塩化水素、アンモニアガス等の水溶性成分を水洗により除去する。加熱器4から排出される加熱処理ガスの温度が比較的低く、排ガス導入ライン9の途中で冷却されることにより、加熱処理ガス中に含まれる塩化水素とアンモニアガスが結びついて、塩化アンモニウムの塩が析出される。そして、この析出物が水洗塔20のガス導入部25の管内周面や入口に付着固化して閉塞し、加熱処理ガスの導入を阻害する。そこで、ガス水洗装置10は、当該水溶性成分の析出物の付着固化により、ガス水洗装置10における加熱処理ガスの導入部が閉塞されることを防止する閉塞防止装置30を備える。
Next, the gas water washing apparatus 10 according to the present invention will be described with reference to FIG. 2. This gas water washing apparatus 10 removes water-soluble components such as hydrogen chloride and ammonia gas contained in the heat treatment gas by water washing. . When the temperature of the heat treatment gas discharged from the heater 4 is relatively low and is cooled in the exhaust gas introduction line 9, hydrogen chloride and ammonia gas contained in the heat treatment gas are combined to form an ammonium chloride salt. Is deposited. And this deposit adheres and solidifies on the pipe inner peripheral surface and inlet of the gas introduction part 25 of the water-washing tower 20, and blocks | blocks introduction of heat processing gas. Therefore, the gas water rinsing apparatus 10 includes a clogging prevention device 30 that prevents the introduction of the heat treatment gas in the gas water rinsing apparatus 10 from being clogged due to adhesion and solidification of the precipitate of the water-soluble component.

すなわち、ガス水洗装置10は、加熱処理ガスを水洗して水溶性成分を除去する水洗塔20と、加熱処理ガスから析出される水溶性成分の析出物によって水洗塔20のガス導入部25が閉塞されることを防止する閉塞防止装置30と、を主に備える。   That is, the gas water rinsing apparatus 10 includes a rinsing tower 20 for rinsing the heat treatment gas to remove water-soluble components, and a gas introduction portion 25 of the water rinsing tower 20 blocked by precipitates of water-soluble components precipitated from the heat treatment gas. And an occlusion prevention device 30 that prevents this from occurring.

水洗塔20は、鉛直方向に立設配置された筒状の塔本体20aを具備する。水洗塔20は、この塔本体20aの上端部から洗浄水を下方に散水する散水ノズル22を有する洗浄水導入部21と、塔本体20aの胴部に設けられて加熱処理ガスと洗浄水との接触を促進し水洗を効率よく行う接触促進用充填材(例えば、ラシヒリング等)を有する充填材層23と、塔本体20aの下端部に設けられて、加熱処理ガスに含まれる塩化水素とアンモニアガスなどの水溶性成分を溶解した洗浄水を排出する洗浄水排出部24と、塔本体20aの洗浄水排出部24より上位の下端部側で周側面に開口されて加熱処理ガスを導入するガス導入部25と、塔本体20aの上端部に設けられて水洗後の加熱処理ガスを排出するガス排出部26と、を有する。   The flush tower 20 includes a cylindrical tower main body 20a arranged upright in the vertical direction. The washing tower 20 is provided in a washing water introduction part 21 having a watering nozzle 22 for spraying washing water downward from the upper end part of the tower body 20a, and a body part of the tower body 20a. Hydrogen chloride and ammonia gas contained in the heat treatment gas, provided at the lower end of the tower body 20a, with a filler layer 23 having a contact promoting filler (for example, Raschig ring or the like) that promotes contact and efficiently performs washing with water. A cleaning water discharge unit 24 that discharges cleaning water in which water-soluble components such as water are dissolved, and a gas introduction that introduces a heat treatment gas that is opened on the peripheral side surface at the lower end side higher than the cleaning water discharge unit 24 of the tower body 20a. And a gas discharge unit 26 that is provided at the upper end of the tower body 20a and discharges the heat-treated gas after washing with water.

水洗塔20において、洗浄水導入部21で散水ノズル22から下方に洗浄水が塔本体20a内に均等に散水される。この洗浄水は、充填材層23で水膜を形成する。そしてガス導入部25から塔本体20a内に導入された加熱処理ガスが、上方に洗浄水の対抗流として送られ充填材層23を通過する。充填材層23では、加熱処理ガスと充填材層23に形成された水膜とが効果的に接触され、加熱処理ガスに含まれる水溶性成分が洗浄水に効果的に溶解される。そして、水洗された加熱処理ガスがガス排出部26から排出される。また水溶性成分を含む洗浄水が洗浄水排出部24から排出される。   In the washing tower 20, washing water is evenly sprinkled in the tower main body 20a downward from the watering nozzle 22 by the washing water introduction section 21. This washing water forms a water film with the filler layer 23. Then, the heat treatment gas introduced into the tower main body 20 a from the gas introduction part 25 is sent upward as a counter flow of the washing water and passes through the filler layer 23. In the filler layer 23, the heat treatment gas and the water film formed on the filler layer 23 are effectively brought into contact, and the water-soluble component contained in the heat treatment gas is effectively dissolved in the cleaning water. Then, the washed heat treatment gas is discharged from the gas discharge unit 26. In addition, the cleaning water containing the water-soluble component is discharged from the cleaning water discharge unit 24.

閉塞防止装置30は、一端部がガス導入部25に接続される導入下流管31と、導入下流管31の中間部に接続されて加熱処理ガスを導入下流管31に流す導入上流管32と、導入下流管31に設けられた析出物除去部36と、導入上流管32を通気する加熱処理ガスを加熱する加熱部33と、を備える。   The clogging prevention device 30 includes an introduction downstream pipe 31 having one end connected to the gas introduction section 25, an introduction upstream pipe 32 connected to an intermediate portion of the introduction downstream pipe 31 and flowing the heat treatment gas to the introduction downstream pipe 31; A precipitate removing unit 36 provided in the introduction downstream pipe 31 and a heating unit 33 that heats the heat treatment gas passing through the introduction upstream pipe 32 are provided.

導入下流管31は、ガス導入部25から塔本体20aの軸心に直交する水平方向に突出して接続された管で、他端部に析出物除去部36を構成する噴射ノズル37が設けられる。   The introduction downstream pipe 31 is a pipe connected from the gas introduction section 25 so as to protrude in the horizontal direction perpendicular to the axis of the column main body 20a, and an injection nozzle 37 constituting the precipitate removing section 36 is provided at the other end.

導入上流管32は、導入下流管31の他端部寄りの中間部から上方に突出されて鉛直方向に延びる管で、さらに水平に湾曲された上端部に、フランジ部を介して排ガス導入ライン9が接続される。   The introduction upstream pipe 32 is a pipe that protrudes upward from the intermediate portion near the other end of the introduction downstream pipe 31 and extends in the vertical direction. Further, the exhaust upstream introduction pipe 9 is connected to the horizontally curved upper end via a flange portion. Is connected.

加熱部33は、導入上流管32を加熱する電気ヒータ34と、導入上流管32の温度を測定する温度計35と、を備える。電気ヒータ34は、そのヒータ部34aが導入上流管32の外周壁に巻き付けられる。電気ヒータ34は、導入上流管32をヒータ部34aにより所定温度(析出物を生成しない温度)で加熱することで、導入上流管32に通気される加熱処理ガスを間接的に加熱する。電気ヒータ34のヒータ部34aは、温度計35により温度が監視される。   The heating unit 33 includes an electric heater 34 that heats the introduction upstream pipe 32 and a thermometer 35 that measures the temperature of the introduction upstream pipe 32. The heater 34 a is wound around the outer peripheral wall of the introduction upstream pipe 32 of the electric heater 34. The electric heater 34 indirectly heats the heat treatment gas vented to the introduction upstream pipe 32 by heating the introduction upstream pipe 32 at a predetermined temperature (a temperature at which no precipitate is generated) by the heater portion 34a. The temperature of the heater portion 34 a of the electric heater 34 is monitored by a thermometer 35.

この析出物除去部36は、噴射水を噴射して析出物を除去する噴射ノズル37と、噴射ノズル37からの噴射水の噴射を調整する手動式または電磁式の開閉弁38と、を備える。噴射ノズル37は、導入下流管31の他端部(ガス導入部25に接続される側とは反対側の端部)に設置される。噴射ノズル37は、噴射口37aが導入下流管31の一端部(導入下流管31の長手方向)に向かって設けられ、噴射口37aから噴射水が導入下流管31の内周壁及びガス導入部25の開口に向かって噴射される。   The deposit removing unit 36 includes an injection nozzle 37 that ejects the spray water to remove the deposit, and a manual or electromagnetic on-off valve 38 that adjusts the jet of the spray water from the spray nozzle 37. The injection nozzle 37 is installed at the other end of the introduction downstream pipe 31 (the end opposite to the side connected to the gas introduction unit 25). In the injection nozzle 37, the injection port 37 a is provided toward one end of the introduction downstream pipe 31 (longitudinal direction of the introduction downstream pipe 31), and the injection water is supplied from the injection port 37 a to the inner peripheral wall of the introduction downstream pipe 31 and the gas introduction unit 25. It is injected toward the opening.

次に、ガス水洗装置10の制御システムを、図3を参照して説明する。
このガス水洗装置10は、除去制御部である制御コントローラ40によりその動作が制御されている。この制御コントローラ40は、ガス水洗装置10の制御を行う主たる部分であり、例えば、CPU、メモリ、ハードディスク等の記憶装置等に構成されて、メモリに記憶された制御プログラム(又はデータテーブル)に従って制御処理を行う。
Next, the control system of the gas water rinsing apparatus 10 will be described with reference to FIG.
The operation of the gas water rinsing apparatus 10 is controlled by a controller 40 that is a removal controller. The controller 40 is a main part that controls the gas water rinsing apparatus 10. For example, the controller 40 is configured in a storage device such as a CPU, a memory, and a hard disk, and is controlled according to a control program (or data table) stored in the memory. Process.

制御コントローラ40には、加熱処理ガスの温度を導入上流管32の外周壁を介して検出する温度計35の検出データと、飛灰加熱処理設備1の各々の機器の運転データや、後述する点検口27からの目視状態に応じて作業員が操作する操作盤41の入力データと、がそれぞれ入力される。そして、制御コントローラ40では、温度計35の検出データに基づいて、電気ヒータ34の操作部34bを介して導入上流管32の加熱温度を制御する。また操作盤41の入力信号に基づいて、制御コントローラ40のタイマ42を設定し、開閉弁操作部39を介して開閉弁38を操作して、噴射ノズル37から噴射水を噴射する噴射時間及び噴射間隔のうち少なくとも一つを制御する。   The controller 40 includes detection data of a thermometer 35 that detects the temperature of the heat treatment gas via the outer peripheral wall of the introduction upstream pipe 32, operation data of each device of the fly ash heat treatment facility 1, and inspections to be described later. Input data of the operation panel 41 operated by the operator according to the visual state from the mouth 27 is input. Then, the controller 40 controls the heating temperature of the introduction upstream pipe 32 via the operation part 34 b of the electric heater 34 based on the detection data of the thermometer 35. Further, based on the input signal of the operation panel 41, the timer 42 of the controller 40 is set, and the on-off valve 38 is operated via the on-off valve operating unit 39 to inject the injection time and the injection from the injection nozzle 37. Control at least one of the intervals.

ここで温度計35により検出される加熱処理ガスの温度や流量は、飛灰加熱処理設備1の運転状態により変動するため、温度計35の検出データに基づいて、電気ヒータ34による加熱温度を制御する。   Here, the temperature and flow rate of the heat treatment gas detected by the thermometer 35 varies depending on the operating state of the fly ash heat treatment equipment 1, so the heating temperature by the electric heater 34 is controlled based on the detection data of the thermometer 35. To do.

また、作業者が塔本体20aの下端部側でガス導入部25の開口に対向して設けられる点検口27(図2)からガス導入部25の開口或いは導入下流管31の内壁面に付着した析出物の析出量(析出状態)を目視により確認し、さらに所定時間後に再度確認して、成長状態を検知する。その成長状態を操作盤41により入力することで、制御コントローラ40ではタイマ42が設定される。そして、所定時間ごとに、開閉弁操作部39を介して開閉弁38が操作され、噴射ノズル37から噴射される噴射水の噴射時間及び噴射間隔のうち少なくとも一つが制御される。 Further, an operator adheres to the opening of the gas introduction part 25 or the inner wall surface of the introduction downstream pipe 31 from the inspection port 27 (FIG. 2) provided opposite to the opening of the gas introduction part 25 on the lower end side of the tower body 20 a. The amount of precipitation (precipitation state) is confirmed by visual observation, and is confirmed again after a predetermined time to detect the growth state. By inputting the growth state through the operation panel 41, the timer 42 is set in the controller 40. And at every predetermined time, the on-off valve 38 is operated via the on-off valve operation part 39, and at least one is controlled among the injection time of the injection water injected from the injection nozzle 37, and the injection space | interval.

以上のように、ガス水洗装置10においては、閉塞防止装置30において加熱した状態の加熱処理ガスを水洗塔20に導入するため、水洗塔20のガス導入部25において、加熱処理ガスから水溶性成分が析出することを抑制できる。さらに、加熱処理ガスから水溶性成分が水洗塔20のガス導入部25において析出した場合であっても、析出した当該水溶性成分を析出物除去部36により除去することができる。そのため、加熱処理ガスから析出される水溶性成分によって水洗塔20のガス導入部25が閉塞されることを防止できる。   As described above, in the gas water rinsing apparatus 10, in order to introduce the heat treatment gas heated in the clogging prevention apparatus 30 into the water washing tower 20, the gas introduction unit 25 of the water washing tower 20 converts the water-soluble component from the heat treatment gas. Can be prevented from precipitating. Furthermore, even when a water-soluble component is precipitated from the heat treatment gas in the gas introduction part 25 of the water washing tower 20, the deposited water-soluble component can be removed by the precipitate removing part 36. Therefore, it is possible to prevent the gas introduction part 25 of the washing tower 20 from being blocked by the water-soluble component precipitated from the heat treatment gas.

なお、本実施の形態においては、ガス水洗装置10により水洗される排ガスが、飛灰加熱処理設備1の加熱器4において処理される飛灰中から生成される加熱処理ガスであるが、これに限定されるものではなく、温度低下により水溶性成分が析出される排ガスであればよい。   In the present embodiment, the exhaust gas washed by the gas flushing device 10 is a heat treatment gas generated from the fly ash treated in the heater 4 of the fly ash heat treatment equipment 1. The exhaust gas is not limited and may be any exhaust gas in which a water-soluble component is precipitated due to a decrease in temperature.

また、本実施の形態においては、加熱処理ガスを加熱する加熱部33を、導入上流管32を加熱する電気ヒータ34により構成しているが、これに限定されるものではない。例えば、導入上流管32の外周に外管を被せたジャケット構造(二重管)として、高温蒸気、高温ガス、加熱流体等を流すことにより導入上流管32を介して加熱処理ガスを加熱するものであってもよい。これにより、加熱処理ガスに含まれる水溶性成分の析出物が析出されない所定温度で加熱可能な構成であればよい。   Further, in the present embodiment, the heating unit 33 that heats the heat treatment gas is configured by the electric heater 34 that heats the introduction upstream pipe 32, but is not limited thereto. For example, as a jacket structure (double pipe) with an outer pipe on the outer periphery of the introduction upstream pipe 32, heat treatment gas is heated via the introduction upstream pipe 32 by flowing high temperature steam, high temperature gas, heating fluid, etc. It may be. Accordingly, any structure that can be heated at a predetermined temperature at which the precipitate of the water-soluble component contained in the heat treatment gas is not deposited may be used.

さらに、本実施の形態においては、水溶性成分の析出物を除去する析出物除去部36を、噴射水を噴射する噴射ノズル37により構成しているが、これに限定されるものではない。ガス導入部25或いは導入下流管31に析出し付着固化した析出物を除去可能な構成であればよい。例えば、ホールソー状の刃物を回転させつつ押し出して析出物を削り取り、導入下流管31からガス導入部25の開口を介して塔本体20a内に押し出すことができる機械式の除去装置により構成しても構わない。   Furthermore, in the present embodiment, the precipitate removing unit 36 that removes the precipitate of the water-soluble component is configured by the spray nozzle 37 that sprays the spray water, but is not limited thereto. Any structure that can remove the deposit deposited and solidified on the gas introduction section 25 or the introduction downstream pipe 31 may be used. For example, it may be constituted by a mechanical removal device that can extrude while rotating a hole saw-shaped blade to scrape deposits and extrude it from the introduction downstream pipe 31 through the opening of the gas introduction section 25 into the tower body 20a. I do not care.

さらに、本実施の形態においては、噴射ノズル37から噴射される噴射水の噴射時間及び噴射間隔の制御を、点検口27から目視した水溶性成分の析出物の析出量(析出状態)に基づいて手動で行っているが、これに限定されるものではなく、例えば、図3に示すように、ガス導入部25付近に設けられる照明器付のカメラ等の撮像装置45により作成されたガス導入部25の開口或いは導入下流管31の内壁面の画像或いは動画に基づいて、制御コントローラ40が、水溶性成分の析出物の析出量(析出状態)を算出し、その算出結果に基づいて自動的に当該制御を行っても構わない。また、導入上流管32の入口部に設けられる第1圧力計46の圧力(導入上流管32の入口部の圧力)と、水洗塔20の塔内下部に設けられる第2圧力計47の圧力(水洗塔20の塔内下部の圧力)と、を制御コントローラ40が比較し、その比較結果に基づいて当該制御を自動的に行っても構わない。さらに、ガス導入部25の開口或いは導入下流管31の内壁面において照射されるレーザ、超音波等を検出するセンサ(間接式検出器)48からの検出信号に基づいて、制御コントローラ40が水溶性成分の析出物の析出量(析出状態)を算出し、その算出結果に基づいて当該制御を自動的に行っても構わない。   Further, in the present embodiment, the control of the spray time and spray interval of the spray water sprayed from the spray nozzle 37 is based on the deposition amount (precipitation state) of the water-soluble component visually observed from the inspection port 27. Although it is performed manually, the present invention is not limited to this. For example, as shown in FIG. 3, a gas introduction unit created by an imaging device 45 such as a camera with an illuminator provided near the gas introduction unit 25. The controller 40 calculates the precipitation amount (precipitation state) of the precipitate of the water-soluble component based on the 25 openings or the inner wall image or moving image of the introduction downstream pipe 31 and automatically based on the calculation result. The control may be performed. Further, the pressure of the first pressure gauge 46 provided at the inlet of the introduction upstream pipe 32 (pressure at the inlet of the introduction upstream pipe 32) and the pressure of the second pressure gauge 47 provided at the lower part of the flush tower 20 ( The control controller 40 may compare the pressure in the lower part of the water washing tower 20 and automatically perform the control based on the comparison result. Further, the controller 40 is water-soluble based on a detection signal from a sensor (indirect detector) 48 that detects a laser, an ultrasonic wave, or the like irradiated on the opening of the gas introduction section 25 or the inner wall surface of the introduction downstream pipe 31. It is also possible to calculate the precipitation amount (deposition state) of the component precipitates and automatically perform the control based on the calculation result.

4 加熱器
10 ガス水洗装置
20 水洗塔
25 ガス導入部
30 閉塞防止装置
31 導入下流管
32 導入上流管
33 加熱部
36 析出物除去部
37 噴射ノズル
40 制御コントローラ(除去制御部)
DESCRIPTION OF SYMBOLS 4 Heater 10 Gas washing apparatus 20 Water washing tower 25 Gas introduction part 30 Blocking prevention apparatus 31 Introduction downstream pipe 32 Introduction upstream pipe 33 Heating part 36 Precipitate removal part 37 Injection nozzle 40 Control controller (removal control part)

Claims (3)

飛灰を処理することにより発生する排ガス中の水溶性成分を水洗により除去する水洗塔と、
前記水洗塔に排ガスを導入するガス導入部の閉塞を防止する閉塞防止装置と、
前記ガス導入部の開口に対向して設けられる点検口と、
を備え、
前記閉塞防止装置は、
排ガスを加熱する加熱部と、
前記水溶性成分の析出物を除去する析出物除去部と、
を有し、
前記ガス導入部に設けられて前記水洗塔に一端部が接続される導入下流管に、前記析出物除去部を備え、
前記ガス導入部に設けられて前記導入下流管の中間部に接続される導入上流管に、前記加熱部を備え、
前記点検口は、前記ガス導入部の開口或いは前記導入下流管の内壁面を目視可能に構成されること
を特徴とするガス水洗装置。
A water-washing tower that removes water-soluble components in exhaust gas generated by treating fly ash by water washing,
A clogging prevention device for preventing clogging of a gas introduction part for introducing exhaust gas into the washing tower,
An inspection port provided opposite to the opening of the gas introduction part;
With
The occlusion prevention device includes:
A heating unit for heating the exhaust gas;
A precipitate removing section for removing the precipitate of the water-soluble component;
Have
In the introduction downstream pipe provided at the gas introduction part and connected to one end of the washing tower, the precipitate removal part is provided,
The introduction upstream pipe provided in the gas introduction part and connected to the intermediate part of the introduction downstream pipe includes the heating unit,
The gas flushing device according to claim 1, wherein the inspection port is configured so that an opening of the gas introduction part or an inner wall surface of the introduction downstream pipe is visible .
前記析出物除去部に、前記導入下流管の他端部に設置されて、前記一端部に向かって噴射水を噴射する噴射ノズルを有すること
を特徴とする請求項1に記載のガス水洗装置。
The gas water rinsing apparatus according to claim 1 , further comprising an injection nozzle that is installed at the other end portion of the introduction downstream pipe and injects the injection water toward the one end portion in the precipitate removing unit .
前記閉塞防止装置は、析出物除去部における噴射水の噴射時間及び噴射間隔のうち少なくとも一つを制御する除去制御部を有し、
前記除去制御部は、前記ガス導入部の開口或いは前記導入下流管の内壁面に付着した析出物の析出量に基づいて前記噴射時間及び噴射間隔を制御すること
を特徴とする請求項1又は請求項2に記載のガス水洗装置。
The clogging prevention device has a removal control unit that controls at least one of the jetting time and jetting interval of the jet water in the deposit removing unit,
The said removal control part controls the said injection time and injection interval based on the precipitation amount of the deposit adhering to the opening of the said gas introduction part, or the inner wall face of the said introduction downstream pipe | tube. Item 3. A gas water washing apparatus according to Item 2.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001046833A (en) * 1999-08-10 2001-02-20 Sumitomo Seika Chem Co Ltd Dry etching exhaust gas treatment apparatus
JP2005087958A (en) * 2003-09-19 2005-04-07 Kanken Techno Co Ltd Exhaust gas introducing structure and exhaust gas treating apparatus using the structure
JP2013119983A (en) * 2011-12-06 2013-06-17 Mitsubishi Heavy Ind Ltd Operation management system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001046833A (en) * 1999-08-10 2001-02-20 Sumitomo Seika Chem Co Ltd Dry etching exhaust gas treatment apparatus
JP2005087958A (en) * 2003-09-19 2005-04-07 Kanken Techno Co Ltd Exhaust gas introducing structure and exhaust gas treating apparatus using the structure
JP2013119983A (en) * 2011-12-06 2013-06-17 Mitsubishi Heavy Ind Ltd Operation management system

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