JP2012082064A - Dust air flow carrying device of exhaust gas treating device in waste disposal facility - Google Patents

Dust air flow carrying device of exhaust gas treating device in waste disposal facility Download PDF

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JP2012082064A
JP2012082064A JP2010231700A JP2010231700A JP2012082064A JP 2012082064 A JP2012082064 A JP 2012082064A JP 2010231700 A JP2010231700 A JP 2010231700A JP 2010231700 A JP2010231700 A JP 2010231700A JP 2012082064 A JP2012082064 A JP 2012082064A
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dust
air flow
airflow
vacuum
exhaust gas
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JP5641865B2 (en
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Mitsumasa Todaka
光正 戸高
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Nippon Steel Engineering Co Ltd
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PROBLEM TO BE SOLVED: To provide a dust air flow carrying device that prevents pollution caused by leakage of hazardous gases and surrounding dust and is so designed as to dispense with much of its maintenance of the dust carrying device without restricting the layouts of each device that discharges dust.SOLUTION: In the dust air flow carrying device that conveys the dust in the air flows each discharged from a plurality of devices 3 to 6 disposed in the emission treating device of a waste disposal facility to a dust treating device through an air flow conveying pipe line 18, discharging valves 16 of devices 3 to 6 are coupled directly to the air flow conveying pipe line 18, each of the discharging valves 16 is connected to the air flow conveying pipe line 18 in series, the air flow conveying pipe line 18 generates the carrying air flow with a vacuum evacuation pump 13 that evacuates a vacuum tank 12, and the vacuum evacuation pump 13 discharges the exhaust gas into a dust collecting device 6 in the waste disposal treating device.

Description

本発明は、廃棄物処理設備で発生するダストをダスト処理設備へ搬送するダスト気流搬送装置に関する。   The present invention relates to a dust airflow conveying device that conveys dust generated in a waste treatment facility to the dust treatment facility.

廃棄物溶融処理設備、例えば、廃棄物溶融処理設備においては、図3に示すように、ごみピットからごみクレーン10によりごみ11が溶融炉1に装入され、装入物は炉内降下とともに乾燥・予熱され、熱分解し、燃焼・溶融し、溶融物として排出される。   In a waste melting treatment facility, for example, a waste melting treatment facility, as shown in FIG. 3, the waste 11 is charged into the melting furnace 1 from the waste pit by the waste crane 10, and the charge is dried along with the descent in the furnace. -Preheated, pyrolyzed, combusted and melted, and discharged as a melt.

溶融炉1の上部から排出される排ガスは、排ガス処理装置の燃焼室3で燃焼され、ボイラー4で熱回収が行われ、ボイラー4の排ガスは水噴霧式ガス冷却塔5で冷却された後、バグフィルタ6で固気分離され、ブロワ7により煙突から排出される。   The exhaust gas discharged from the upper part of the melting furnace 1 is combusted in the combustion chamber 3 of the exhaust gas treatment device, heat recovery is performed in the boiler 4, and the exhaust gas in the boiler 4 is cooled in the water spray type gas cooling tower 5, It is separated into solid and gas by the bag filter 6 and discharged from the chimney by the blower 7.

排ガス中のダストは燃焼室3、ボイラー4、水噴霧式ガス冷却塔5、バグフィルタ6の底部に沈降し、沈降したダストは各機器3〜6からダスト切出弁16を通じて切り出す。このダスト切出弁16には、炉内と連通状態となるのを防ぐため、二重シール方式やシール機能を有するロータリー式切出弁16が設けられている。   Dust in the exhaust gas settles at the bottom of the combustion chamber 3, boiler 4, water spray type gas cooling tower 5 and bag filter 6, and the dust that has settled is cut out from each device 3-6 through a dust extraction valve 16. The dust cut-off valve 16 is provided with a rotary cut-off valve 16 having a double seal method or a seal function in order to prevent communication with the inside of the furnace.

切出弁16から排出されたダストは、機械搬送方式コンベア20に案内され、集合してダスト処理設備のダスト貯留ホッパ21に搬送される。機械搬送方式コンベア20には、主にスクリューコンベアやスクレーパー式コンベアが用いられる。ダスト貯留ホッパ21に搬送されたダストは、その後、無害化処理されたりあるいは、造粒されて廃棄物溶融炉1に戻されて溶融処理されたりしている(引用文献1〜3参照)。   The dust discharged from the cut-off valve 16 is guided to the mechanical transfer type conveyor 20 and is collected and transferred to the dust storage hopper 21 of the dust processing facility. A screw conveyor or a scraper type conveyor is mainly used as the mechanical conveyance type conveyor 20. The dust transported to the dust storage hopper 21 is subsequently detoxified or granulated and returned to the waste melting furnace 1 and melted (see Cited Documents 1 to 3).

特開2000−117224号公報JP 2000-117224 A 特開2000−117223号公報JP 2000-117223 A 特開平11−221545号公報Japanese Patent Laid-Open No. 11-221545

各機器から切り出されたダストを搬送するために使用される機械搬送方式コンベアでは、各機器からダスト処理設備までに多数のコンベアを並べて搬送路が形成される。これは、機械搬送方式コンベアがその機構上、直線性を必要とするためである。このため、機械搬送方式コンベアがダストを排出する機器の配置に対して大きな制約条件となり且つこれらのコンベア群が占めるスペースが大きくなるため、設備コストに大きな影響を与えている。   In a mechanical conveyance type conveyor used for conveying dust cut out from each device, a large number of conveyors are arranged from each device to a dust treatment facility to form a conveyance path. This is because the mechanical conveyance type conveyor requires linearity due to its mechanism. For this reason, since a mechanical conveyance system conveyor becomes a big constraint condition with respect to arrangement | positioning of the apparatus which discharges dust, and the space which these conveyor groups occupy becomes large, it has a big influence on installation cost.

また、機械搬送方式コンベアを使用する場合、多数のコンベア群で構成されるため、メンテナンスコストも多大となっている。その上、メンテナンスが必要なため、デッキ面上を横断することになり、デッキ上の通行障害となっている。さらに、メンテナンス時には、ケーシングを開放するため、ダストの飛散により周囲がダストで汚染されるという課題もあった。   Moreover, when using a mechanical conveyance system conveyor, since it is comprised by many conveyor groups, the maintenance cost is also large. In addition, since maintenance is required, the deck surface is traversed, resulting in a traffic obstacle on the deck. Furthermore, since the casing is opened at the time of maintenance, there is a problem that the surroundings are contaminated with dust due to dust scattering.

また、通常、ダストを切り出す機器は、誘引送風機により負圧で運転されているが、ダスト切出弁からは大気開放されているため、溶融炉で処理される廃棄物の性状変化により、燃焼ガス量が一時的に急増して負圧から正圧となる場合があり、その際にダスト切出弁から炉内の有害ガスがリークして環境を汚染する危険があった。   In addition, although the equipment that cuts out dust is normally operated at a negative pressure by an induction blower, it is open to the atmosphere from the dust extraction valve. There is a case where the amount increases temporarily from negative pressure to positive pressure, and at that time, there is a danger that harmful gas in the furnace leaks from the dust extraction valve and pollutes the environment.

そこで、本発明は、廃棄物処理設備において、有害ガスのリーク及び周囲のダストによる汚染を防止するとともに、ダストを切り出す各機器の配置を制約することがなく、ダスト搬送装置のメンテナンスが多大とならないようにしたダスト気流搬送装置を提供するものである。   Therefore, the present invention prevents the leakage of harmful gas and contamination by surrounding dust in the waste treatment facility, does not restrict the arrangement of each device for cutting out dust, and does not significantly increase the maintenance of the dust transfer device. The dust airflow conveying device thus provided is provided.

本願請求項1の発明は、廃棄物処理設備の排ガス処理装置に配置されている複数の機器からそれぞれ切り出されるダストを気流搬送管路によりダスト処理設備に気流搬送するダスト気流搬送装置であって、気流搬送管路に各機器の切出弁をそれぞれ直結するとともに、各切出弁どうしが気流搬送管路に対して直列に連結されていることを特徴とする。   The invention of claim 1 of the present application is a dust airflow conveying device that conveys the dust cut out from each of a plurality of devices disposed in the exhaust gas treatment device of a waste treatment facility to the dust treatment facility by an airflow conveyance line, The cut-out valves of the respective devices are directly connected to the airflow conveyance pipes, and the cutout valves are connected in series to the airflow conveyance pipes.

本願請求項2の発明は、気流搬送管路の上流の端部に空気導入口を設け、気流搬送管路下流の端部のダスト処理設備側には真空タンクが設けられ、真空による誘引により搬送空気流を発生させることを特徴とする。   In the invention of claim 2 of the present application, an air introduction port is provided at the upstream end of the airflow conveyance pipe, and a vacuum tank is provided at the dust treatment facility side at the downstream end of the airflow conveyance pipe, which is conveyed by vacuum induction. It is characterized by generating an air flow.

本願請求項3の発明は、ダストフィルタを介して真空タンクを誘引する真空引用真空ポンプの排気先を廃棄物処理設備の集塵装置内としたことを特徴とする。   The invention of claim 3 of the present application is characterized in that the exhaust destination of the vacuum quotation vacuum pump for attracting the vacuum tank through the dust filter is in the dust collector of the waste treatment facility.

本願請求項4の発明は、気流搬送管路の上流の端部の空気導入口部分に、吸込み空気流量の検出手段及び流量制御手段を設けたことを特徴とする。   The invention of claim 4 of the present application is characterized in that a suction air flow rate detection means and a flow rate control means are provided in the air inlet port portion at the upstream end of the airflow conveying pipeline.

本願請求項5の発明は、請求項4において、気流搬送管と各機器のダスト切出弁の直結部分の上流側に真空圧力検出手段を設け、気流搬送管路の上流の端部の空気導入口部分の空気流量が低下し且つ真空度が低下した場合に、空気流量及び真空度が回復するまで直結部分のダスト切り出しを一時停止又はダスト切り出し速度を低下させる手段を設けたことを特徴とする。   The invention of claim 5 of the present application is that in claim 4, a vacuum pressure detecting means is provided on the upstream side of the direct connection portion between the airflow conveying pipe and the dust extraction valve of each device, and air is introduced into the upstream end of the airflow conveying pipe. When the air flow rate in the mouth portion is reduced and the degree of vacuum is reduced, means is provided for temporarily stopping the dust cutting of the directly connected portion or reducing the dust cutting speed until the air flow rate and the vacuum degree are restored. .

本発明では、ダスト搬送手段を気流輸送とすることにより、その機構上から搬送路が制約される機械搬送方式コンベアに比べて、気流搬送管路により自由度を持たせることができるので、任意のルートでダスト搬送が可能である。また、気流輸送によりデッキ上の通行障害の問題がなくなる。   In the present invention, since the dust transport means is air transport, the air transport pipe can have a degree of freedom as compared to a mechanical transport conveyor in which the transport path is restricted from the top of the mechanism. Dust can be transported along the route. In addition, the problem of traffic obstruction on the deck is eliminated by air transport.

本発明では、ダストを切り出す各機器のダスト切出弁と気流搬送管路を直結し、大気との連通状態をなくし、真空引きした排気は廃棄物処理装置内に導入することにより工場内での放散をなくして密閉で完全クローズドとなっているため、ダスト切出弁から炉内の有害ガスがリークするのを防止しできるので、工場内へのダスト、有害ガスによる汚染の問題がなくなった。また、メンテナンス時のダスト飛散による汚染を防止することができる。   In the present invention, the dust extraction valve of each device that cuts out dust and the air flow conveyance line are directly connected, the state of communication with the atmosphere is eliminated, and the evacuated exhaust is introduced into the waste treatment apparatus so that it can be used in the factory. Since it is sealed and completely closed without any emission, it is possible to prevent leakage of harmful gas in the furnace from the dust extraction valve, eliminating the problem of contamination by dust and harmful gas into the factory. Further, contamination due to dust scattering during maintenance can be prevented.

本発明では、気流搬送管路であり、1本の気流搬送管に各機器からの払出弁を直列に接続する構造なので、各機器の接続が単純となってメンテナンス性も向上する。   In the present invention, since it is an airflow conveyance pipe and a discharge valve from each device is connected in series to one airflow conveyance tube, the connection of each device is simplified and the maintainability is improved.

本発明では、気流輸送方式として真空誘引方式することにより、加圧圧送方式の場合に発生する可能性のあるダスト切出弁を通じて管路内空気、ダストが炉内に逆流あるいはリークしてダスト払い出しが正常に行われなくなるのを防ぐことができる。   In the present invention, the vacuum attraction method is used as the air flow transportation method, so that air in the pipeline, dust flows back into the furnace or leaks through the dust extraction valve that may be generated in the case of the pressure and pressure feeding method. Can be prevented from being performed normally.

また、本発明では、真空引きした排気は、廃棄物処理装置内に導入することにより工場内での放散をなくしたので、環境汚染を防止することができる。   Further, in the present invention, since the exhaust gas that has been evacuated is introduced into the waste treatment apparatus to eliminate the emission in the factory, environmental pollution can be prevented.

また、本発明では、流量あるいは真空度検出手段で輸送媒体である空気の流量及び真空度を常に監視し、制御することにより、安定した気流搬送を行うことができるとともに、閉塞を防ぐことができる。   Further, in the present invention, by constantly monitoring and controlling the flow rate and the degree of vacuum of the air that is the transport medium by the flow rate or the degree of vacuum detection means, it is possible to carry out stable air flow and prevent blockage. .

廃棄物ガス化溶融設備に本発明のダスト搬送を適用した例を示す図である。It is a figure which shows the example which applied the dust conveyance of this invention to the waste gasification melting equipment. 本発明で使用するインジェクタの一例を示す断面図である。It is sectional drawing which shows an example of the injector used by this invention. 廃棄物ガス化溶融設備の従来の灰搬送の例を示す図である。It is a figure which shows the example of the conventional ash conveyance of a waste gasification melting equipment.

本発明の実施例について図を参照しながら説明する。   Embodiments of the present invention will be described with reference to the drawings.

図1において、ごみピットからごみクレーン10によりごみ11が溶融炉1に装入され、装入物は炉内降下とともに乾燥・予熱され、熱分解し、燃焼・溶融し、溶融物として排出される。   In FIG. 1, waste 11 is charged into a melting furnace 1 from a waste pit by a garbage crane 10, and the charged material is dried and preheated as the furnace descends, thermally decomposed, combusted and melted, and discharged as a melt. .

溶融炉1からの排ガスは、燃焼室3、ボイラー4、水噴霧式ガス冷却塔5、バグフィルタ6が配置された排ガス処理装置で処理される。排ガスは、発生ガス管2から燃焼室3に導入され、燃焼空気ファン9で燃焼空気が吹き込まれる燃焼バーナ8で燃焼され、ボイラー4で熱回収が行われ、ボイラー4の排ガスは水噴霧式ガス冷却塔5で冷却された後、バグフィルタ6で固気分離され、誘引送風機7により煙突から排出される。   The exhaust gas from the melting furnace 1 is processed by an exhaust gas processing device in which a combustion chamber 3, a boiler 4, a water spray type gas cooling tower 5 and a bag filter 6 are arranged. The exhaust gas is introduced into the combustion chamber 3 from the generated gas pipe 2 and burned by the combustion burner 8 into which the combustion air is blown by the combustion air fan 9, heat recovery is performed by the boiler 4, and the exhaust gas of the boiler 4 is water spray type gas After being cooled by the cooling tower 5, it is separated into solid and gas by the bag filter 6 and discharged from the chimney by the induction blower 7.

燃焼室3、ボイラ4、水噴霧式ガス冷却塔5、バグフィルタ6の底部にはそれぞれ底部に落下したダストを切り出すダスト切出弁16が設けられ、それぞれのダスト切出弁16が一本の気流搬送管路18に直列に連結されている。   The bottoms of the combustion chamber 3, the boiler 4, the water spray type gas cooling tower 5, and the bag filter 6 are each provided with a dust extraction valve 16 for cutting out dust that has fallen to the bottom. It is connected in series with the airflow conveyance pipe line 18.

気流搬送管路18には、一般の管材料を使用することができるが、曲管部には耐摩耗性を考慮した管材を使用する。ごみ処理能力150〜200t/日規模であれば、ダスト搬送量は125〜1170kg/hであり、気流搬送管路18は50A〜80A程度となり、固気比としては平均2〜3kg/kgで搬送される。   A general pipe material can be used for the airflow conveyance pipe 18, but a pipe material considering wear resistance is used for the curved pipe portion. If the waste treatment capacity is 150 to 200 t / day, the dust conveyance amount is 125 to 1170 kg / h, the air flow conveyance line 18 is about 50 A to 80 A, and the average solid-gas ratio is 2 to 3 kg / kg. Is done.

各機器3〜6から切り出されたダストは、ダスト切出弁16を介してインジェクタ17にて気流搬送管路18に送られる。図2に示すように、インジェクタ17では切り出されたダストを搬送気流に滞留させることなく混合させるため、ダストの混合部直前で管路断面を縮小し、気流を高速化し、ダストを加速する。   The dust cut out from each of the devices 3 to 6 is sent to the air flow conveying pipe 18 by the injector 17 through the dust cutting valve 16. As shown in FIG. 2, in the injector 17, the cut out dust is mixed without staying in the conveying airflow, so that the pipe cross section is reduced immediately before the dust mixing portion, the airflow is speeded up, and the dust is accelerated.

気流搬送管路18はダスト処理設備の近傍に設けられた真空タンク12に連結し、気流搬送されたダストは、この真空タンク12に貯留される。真空タンク12内の圧力は、−30kPa程度となる。真空タンク18の真空引きはフィルタ12aを介して真空ポンプ13により行われ、バグフィルタ6内に排気される。   The air flow conveying pipe 18 is connected to a vacuum tank 12 provided in the vicinity of the dust treatment facility, and the dust carried by the air flow is stored in the vacuum tank 12. The pressure in the vacuum tank 12 is about −30 kPa. The vacuum tank 18 is evacuated by the vacuum pump 13 through the filter 12 a and exhausted into the bag filter 6.

一方、搬送用空気は、気流搬送管路18の上流の端部に設けた空気取り込み口15から取り込まれる。搬送用空気の管路内流速は、20〜25m/s程度に設定する。この部分には、空気流量計(FI)、空気流量調節指示計(FIC)及び、空気流量調節指示計(FIC)により調整される空気流量調整弁19が設けられている。空気流量調整弁19は、ダスト濃度変化による管路圧損の変化にかかわらず、一定の空気を流すように開度が制御される。   On the other hand, the air for conveyance is taken in from the air intake port 15 provided at the upstream end of the airflow conveyance pipeline 18. The in-pipe flow velocity of the conveying air is set to about 20 to 25 m / s. In this portion, an air flow meter (FI), an air flow rate adjustment indicator (FIC), and an air flow rate adjustment valve 19 adjusted by the air flow rate adjustment indicator (FIC) are provided. The air flow rate adjusting valve 19 is controlled in opening degree so that a constant amount of air flows regardless of the change in the pipe pressure loss due to the change in the dust concentration.

さらに、各機器3〜6からのダスト切出量が一時的に増大する場合には気流搬送管路18の閉塞が問題になるが、気流搬送管路18が閉塞する傾向となった場合には、空気流量が低下することで検出できる。   Further, when the amount of dust cut out from each device 3 to 6 temporarily increases, the blockage of the airflow conveyance line 18 becomes a problem, but when the airflow conveyance line 18 tends to be blocked, It can be detected by a decrease in the air flow rate.

また、気流搬送管路18が閉塞した場合を想定し、インジェクタ17の上流側に真空圧力検出器(PI)22を設け、空気流量が低下し且ついずれかの真空度が低下した場合には、真空度の低下を検出した真空圧力検出器(PI)22の直下流側のダスト切り出しを一時停止又は、ダスト切り出し速度を低下させることで気流搬送管路18の閉塞を防止できる。前記ダスト切り出し速度を低下させる場合、切り出し速度を低下させるダスト切出弁の直上流側の真空圧力検出器(P2)の真空度に応じて、真空度が上がれば切り出し速度を上げ、真空度が下がれば切り出し速度を下げるというように制御することができる。   In addition, assuming that the airflow conveyance pipe line 18 is blocked, a vacuum pressure detector (PI) 22 is provided on the upstream side of the injector 17, and when the air flow rate is reduced and any of the vacuum degrees is reduced, It is possible to prevent clogging of the airflow conveyance line 18 by temporarily stopping dust cutting immediately downstream of the vacuum pressure detector (PI) 22 that has detected a decrease in the degree of vacuum or by reducing the dust cutting speed. When reducing the dust cutting speed, if the vacuum level rises according to the degree of vacuum of the vacuum pressure detector (P2) immediately upstream of the dust cutting valve that reduces the cutting speed, the cutting speed is increased and the vacuum level is increased. If it falls, it can control to reduce the cutting-out speed.

気流搬送管路18は炉別に構成されるが、途中、他炉から合流させることも可能である。又、空気取り込み口15にホース類を接続して、炉停止中における真空掃除用として活用することもできる。   Although the airflow conveyance line 18 is configured for each furnace, it can be joined from another furnace in the middle. Further, a hose can be connected to the air intake port 15 to be used for vacuum cleaning while the furnace is stopped.

1:溶融炉 2:発生ガス管
3:燃焼室 4:ボイラー
5:水噴霧式ガス冷却塔 6:バグフィルタ
7:誘引送風機 8:燃焼バーナ
9:燃焼空気ファン 10:ごみクレーン
11:ごみ 12:真空タンク
13:真空ポンプ 14:ダスト切出弁
15:空気吸い込み口 16:ダスト切出弁
17:インジェクタ 18:気流搬送管路
19:吸い込み空気流調弁 20:機械搬送式コンベア
21:ダスト貯留ホッパ 22:真空圧力検出器
1: Melting furnace 2: Generated gas pipe 3: Combustion chamber 4: Boiler 5: Water spray type gas cooling tower 6: Bag filter 7: Induction fan 8: Combustion burner 9: Combustion air fan 10: Waste crane 11: Waste 12: Vacuum tank 13: Vacuum pump 14: Dust extraction valve 15: Air suction port 16: Dust extraction valve 17: Injector 18: Air flow conveyance line 19: Suction air flow adjustment valve 20: Machine conveyance type conveyor 21: Dust storage hopper 22: Vacuum pressure detector

Claims (5)

廃棄物処理設備の排ガス処理装置に配置されている複数の機器からそれぞれ切り出されるダストを気流搬送管路によりダスト処理設備に気流搬送するダスト気流搬送装置であって、気流搬送管路に各機器の切出弁をそれぞれ直結するとともに、各切出弁どうしが気流搬送管路に対して直列に連結されていることを特徴とする廃棄物処理設備における排ガス処理装置のダスト気流搬送装置。   A dust airflow conveying device that conveys dust cut out from a plurality of devices disposed in an exhaust gas treatment device of a waste treatment facility to a dust treatment facility by an airflow conveying pipe, A dust airflow conveyance device for an exhaust gas treatment apparatus in a waste treatment facility, wherein the cutout valves are directly connected to each other, and the cutout valves are connected in series to an airflow conveyance pipe line. 気流搬送管路の上流の端部に空気導入口を設け、気流搬送管路下流の端部のダスト処理設備側には真空タンクが設けられ、真空による誘引により搬送空気流を発生させることを特徴とする請求項1に記載の廃棄物処理設備における排ガス処理装置のダスト気流搬送装置。   An air inlet is provided at the upstream end of the airflow conveyance pipeline, and a vacuum tank is provided at the dust treatment facility side at the downstream end of the airflow conveyance pipeline, which generates a conveyance air flow by vacuum induction. The dust airflow conveying apparatus of the exhaust gas treatment apparatus in the waste treatment facility according to claim 1. ダストフィルタを介して真空タンクを誘引する真空引用真空ポンプの排気先を廃棄物処理設備の集塵装置内としたことを特徴とする請求項2に記載の廃棄物処理設備における排ガス処理装置のダスト気流搬送装置。   The dust of the exhaust gas treatment apparatus in the waste treatment facility according to claim 2, wherein the exhaust destination of the vacuum citation vacuum pump that attracts the vacuum tank through the dust filter is in the dust collector of the waste treatment facility. Airflow transfer device. 気流搬送管路の上流の端部の空気導入口部分に、吸込み空気流量の検出手段及び流量制御手段を設けたことを特徴とする請求項3に記載の廃棄物処理設備における排ガス処理装置のダスト気流搬送装置。   4. The dust of the exhaust gas treatment apparatus in the waste treatment facility according to claim 3, wherein a suction air flow rate detecting means and a flow rate control means are provided at an air inlet port portion at an upstream end of the air flow conveying pipe. Airflow transfer device. 気流搬送管と各機器のダスト切出弁の直結部分の上流側に真空圧力検出手段を設け、気流搬送管路の上流の端部の空気導入口部分の空気流量が低下し且つ真空度が低下した場合に、空気流量及び真空度が回復するまで直結部分のダスト切り出しを一時停止又はダスト切り出し速度を低下させる手段を設けたことを特徴とする請求項4に記載の廃棄物処理設備における排ガス処理装置のダスト気流搬送装置。   A vacuum pressure detection means is provided upstream of the direct connection between the airflow transfer pipe and the dust extraction valve of each device, and the air flow rate at the air inlet at the upstream end of the airflow transfer line is reduced and the degree of vacuum is reduced The exhaust gas treatment in the waste treatment facility according to claim 4, further comprising means for temporarily stopping the dust cutting of the directly connected portion or reducing the dust cutting speed until the air flow rate and the degree of vacuum are recovered. Dust airflow conveying device of the device.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109353825A (en) * 2018-12-11 2019-02-19 鞍钢集团工程技术有限公司 A kind of granular material preheating Pneumatic conveyer and technique
CN112124972A (en) * 2019-06-24 2020-12-25 中国石油天然气股份有限公司 Device for unloading demercuration agent in demercuration tower

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109353825A (en) * 2018-12-11 2019-02-19 鞍钢集团工程技术有限公司 A kind of granular material preheating Pneumatic conveyer and technique
CN112124972A (en) * 2019-06-24 2020-12-25 中国石油天然气股份有限公司 Device for unloading demercuration agent in demercuration tower

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