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JP6906232B2 - Wet particulate matter processing equipment - Google Patents
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JP6906232B2 - Wet particulate matter processing equipment - Google Patents

Wet particulate matter processing equipment Download PDF

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JP6906232B2
JP6906232B2 JP2018007588A JP2018007588A JP6906232B2 JP 6906232 B2 JP6906232 B2 JP 6906232B2 JP 2018007588 A JP2018007588 A JP 2018007588A JP 2018007588 A JP2018007588 A JP 2018007588A JP 6906232 B2 JP6906232 B2 JP 6906232B2
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gaseous substance
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JP2019126743A (en
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大進 西出
大進 西出
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Neive Heat Co Ltd
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Description

本発明は、飲食店を含む店舗、製造工場や化学工場、プラントなどから排出される排ガス、塗料粉塵、黒煙などの環境に影響を与えるガス状物質を分離除去するようにした湿式の排ガス処理・除塵などが可能なガス状物質処理装置に関し、特に灯油、重油等の燃焼から発生するカーボン系超微粒子及び塗装などの微細粉塵を効率良く分離回収する湿式ガス状物質処理装置に関する。 The present invention is a wet exhaust gas treatment that separates and removes gaseous substances that affect the environment such as exhaust gas, paint dust, and black smoke emitted from stores including restaurants, manufacturing plants, chemical plants, and plants. -Regarding a gaseous substance treatment device capable of removing dust, in particular, a wet gaseous substance processing device that efficiently separates and recovers carbon-based ultrafine particles generated from combustion of kerosene, heavy oil, etc. and fine dust such as coating.

従来、水を使った湿式の排ガス処理装置として、スクラバー装置が知られている。従来のスクラバー装置としては、水や脱臭剤液を排ガスに噴霧するタイプの装置や、排ガスと水を吸上げて滝のように逆流させ排ガスを水に当てて通過させるタイプの装置や、噴霧ノズルにより噴霧水層を作り、排ガスを噴霧水層とフィルター層とに交互に通すタイプの装置などがある。また、ロックウール、不織布、金網等に水を散布させながら、排ガスを通過させて粉塵や水溶性気体を水中に取り込む方式なども採用されているが、排ガス中に霧状の水分が排出されていて環境上の点からも好ましくないものであった。 Conventionally, a scrubber device is known as a wet exhaust gas treatment device using water. Conventional scrubber devices include a type of device that sprays water or deodorant liquid onto the exhaust gas, a type of device that sucks up the exhaust gas and water and causes it to flow back like a waterfall, and the exhaust gas is exposed to water and passed through. There is a type of device that creates a spray water layer and allows exhaust gas to pass through the spray water layer and the filter layer alternately. In addition, a method is also adopted in which water is sprayed on rock wool, non-woven fabric, wire mesh, etc., and the exhaust gas is passed through to take in dust and water-soluble gas into the water, but mist-like moisture is discharged into the exhaust gas. It was also unfavorable from the environmental point of view.

上記のような従来の装置では、装置が複雑となるため故障し易いという問題などがあった。また、フィルターを使うタイプの装置ではフィルターを交換する必要があるし、また、上記のような従来の水を使う装置では、スプレーや送水ポンプなどの個々の装置が必要となり、メンテナンスにも手間がかかるという問題があった。また、上記のような従来の水を使う装置では、水を大量に使用する必要があった。そこで、本願出願人は、特許文献1に示す湿式ガス状物質処理装置を提案し、好評を得ている。 In the conventional device as described above, there is a problem that the device is complicated and easily breaks down. In addition, it is necessary to replace the filter in the type of device that uses a filter, and in the conventional device that uses water as described above, individual devices such as a spray and a water pump are required, and maintenance is troublesome. There was a problem that it took. Further, in the conventional device using water as described above, it is necessary to use a large amount of water. Therefore, the applicant of the present application has proposed a wet particulate matter treatment apparatus shown in Patent Document 1, which has been well received.

しかしながら、特許文献1に示す湿式ガス状物質処理装置において、吸気ファンを貯水槽よりもガス状物質吸入口側に設置した装置の場合(前方吸引型の湿式ガス状物質処理装置の場合)、ガス状物質吸入口からの風量を上げるために風量の大きな吸気ファンを用いて、吸引力を強力にしようとすると、次のような問題点があった。 However, in the wet gaseous substance processing apparatus shown in Patent Document 1, in the case of the apparatus in which the intake fan is installed closer to the gaseous substance suction port side than the water storage tank (in the case of the front suction type wet gaseous substance processing apparatus), gas. When an attempt was made to increase the suction force by using an intake fan having a large air volume in order to increase the air volume from the gas suction port, there were the following problems.

前方吸引型の湿式ガス状物質処理装置の場合、吸引されたガス状物質は、ガス状物質吸入口側の貯水槽の水面に大きな風圧でぶつかるので、汚れた空気を含むガス状物質が、僅かな隙間や穴から装置の外に吹きだしてしまうという問題があった。 In the case of a forward suction type wet gaseous substance treatment device, the sucked gaseous substance collides with the water surface of the water tank on the gaseous substance suction port side with a large wind pressure, so that the amount of gaseous substance containing dirty air is small. There was a problem that it was blown out of the device through a large gap or hole.

また、前方吸引型の湿式ガス状物質処理装置の場合、風量の大きな吸気ファンを用いると、大きな風圧によってガス状物質吸入口側の貯水槽の水面が押し下げられ過ぎてしまい、前記ガス状物質吸入口から吸入された、汚れた空気を含むガス状物質が前記貯水槽の水とあまり接触しないまま、ガス状物質排出口から排出されてしまうという問題があった。 Further, in the case of a forward suction type wet gaseous substance processing device, if an intake fan having a large air volume is used, the water surface of the water storage tank on the gaseous substance suction port side is pushed down too much by the large wind pressure, and the gaseous substance is sucked. There is a problem that the gaseous substance including dirty air sucked from the mouth is discharged from the gaseous substance discharge port without much contact with the water in the water storage tank.

特開2017−104843JP-A-2017-104843

本発明は、上記した従来技術の問題に鑑みなされたもので、ガス状物質吸入口側に設置した吸気ファンの風量を上げても、処理室内に吸入されたガス状物質が貯水槽の水と確実に接触することができるようにした、湿式ガス状物質処理装置を提供することを目的とする。 The present invention has been made in view of the above-mentioned problems of the prior art, and even if the air volume of the intake fan installed on the gaseous substance suction port side is increased, the gaseous substance sucked into the treatment chamber becomes water in the water tank. It is an object of the present invention to provide a wet gaseous substance processing apparatus capable of ensuring contact.

上記課題を解決するため、本発明の湿式ガス状物質処理装置は、処理室と、前記処理室上部に設けられ、装置外部のガス状物質を前記処理室内に吸入させるための吸気ファンと、前記処理室に形成され前記処理室内にガス状物質を吸入させるためのガス状物質吸入口と、前記処理室に形成され前記処理室内に吸入されたガス状物質を前記処理室外に排出させるガス状物質排出口と、前記処理室内に設けられた貯水槽と、前記ガス状物質吸入口から吸入されるガス状物質と前記ガス状物質排出口から排出されるガス状物質とを前記処理室内で仕切るように、前記貯水槽の静止水面の上方に垂設せしめられてなる垂設仕切板と、前記ガス状物質排出口側の前記貯水槽の静止水面と平行して、前記貯水槽の静止水面の上方に設置され、前記貯水槽の水面に奔流を発生せしめるための波状多孔質奔流発生板と、前記波状多孔質奔流発生板の上方に設置され、前記奔流により生じる飛沫を受けるための少なくとも一つの多孔質邪魔板と、前記垂設仕切板に、下端に行くに従って前記垂設仕切板から離間するように傾斜して設けられた傾斜規制板と、を有し、前記垂設仕切板よりも前記傾斜規制板の方が下方に延出せしめられてなり、前記処理室内に吸入されたガス状物質が前記貯水槽の水と接触することによって浄化されるようにした、湿式ガス状物質処理装置である。 In order to solve the above problems, the wet gaseous substance processing apparatus of the present invention includes a processing chamber, an intake fan provided in the upper part of the processing chamber for sucking a gaseous substance outside the apparatus into the processing chamber, and the above. A gaseous substance suction port formed in the treatment chamber for sucking a gaseous substance into the treatment chamber, and a gaseous substance formed in the treatment chamber and sucked into the treatment chamber to be discharged to the outside of the treatment chamber. The discharge port, the water storage tank provided in the treatment chamber, the gaseous substance sucked from the gaseous substance suction port, and the gaseous substance discharged from the gaseous substance discharge port are partitioned in the treatment chamber. Above the static water surface of the water storage tank, in parallel with the stationary partition plate vertically installed above the static water surface of the water storage tank and the static water surface of the water storage tank on the gaseous substance discharge port side. A wavy porous torrent generating plate for generating a torrent on the water surface of the water storage tank, and at least one porous plate installed above the wavy porous torrent generating plate for receiving droplets generated by the torrent. It has an obstruction plate and an inclination restricting plate provided on the vertical partition plate so as to be inclined away from the vertical partition plate toward the lower end, and the inclination is higher than that of the vertical partition plate. It is a wet gaseous substance treatment device in which the regulation plate is extended downward so that the gaseous substance sucked into the treatment chamber is purified by coming into contact with the water in the water storage tank. ..

前記多孔質邪魔板が、前記貯水槽の静止水面に対して傾斜して設けられ、且つ複数枚設けられてなるのが好ましい。 It is preferable that the porous baffle plate is provided so as to be inclined with respect to the static water surface of the water storage tank, and a plurality of the porous baffle plates are provided.

前記傾斜規制板が、前記垂設仕切板に対して15°〜40°傾斜して設けられてなるのが好ましく、20°〜30°がさらに好ましい。 The inclination control plate is preferably provided at an inclination of 15 ° to 40 ° with respect to the vertical partition plate, and more preferably 20 ° to 30 °.

本明細書において、ガス状物質には、排ガス、塗料粉塵、黒煙、有毒ガスなどの環境に影響を与えるガス状物質が含まれ、灯油、重油等の燃焼から発生するカーボン系超微粒子及び塗装などの微細粉塵も含まれる。 In the present specification, gaseous substances include gaseous substances that affect the environment such as exhaust gas, paint dust, black smoke, and toxic gas, and carbon-based ultrafine particles and coatings generated from combustion of kerosene, heavy oil, etc. Fine dust such as is also included.

前記波状多孔質奔流発生板及び前記多孔質邪魔板が、パンチングメタルによって構成されてなるのが好適である。 It is preferable that the wavy porous torrent generation plate and the porous obstruction plate are made of punching metal.

本発明の湿式ガス状物質処理装置を用いることで、前記処理室内に吸入されたガス状物質が前記貯水槽の水と接触することによって浄化されるようにした湿式ガス状物質処理方法を行うことができる。 By using the wet gaseous substance treatment apparatus of the present invention, a wet gaseous substance treatment method is performed in which the gaseous substance sucked into the treatment chamber is purified by coming into contact with the water in the water storage tank. Can be done.

本発明によれば、ガス状物質吸入口側に設置した吸気ファンの風量を上げても、処理室内に吸入されたガス状物質が貯水槽の水と確実に接触することができるようにした、湿式ガス状物質処理装置を提供することができるという著大な効果を奏する。 According to the present invention, even if the air volume of the intake fan installed on the side of the gaseous substance suction port is increased, the gaseous substance sucked into the treatment chamber can be surely brought into contact with the water in the water tank. It has a great effect of being able to provide a wet gaseous substance processing apparatus.

本発明に係る湿式ガス状物質処理装置の一つの実施の形態を示す一部透視斜視図である。It is a partial perspective perspective view which shows one Embodiment of the wet particulate matter processing apparatus which concerns on this invention. 図1の湿式ガス状物質処理装置を別の方向からみた一部透視斜視図である。It is a partial perspective perspective view of the wet particulate matter processing apparatus of FIG. 1 as viewed from another direction. 図1の湿式ガス状物質処理装置の模式的説明図であって、静止水面の状態を示す。It is a schematic explanatory view of the wet particulate matter processing apparatus of FIG. 1, and shows the state of the static water surface. 図3の一部拡大説明図であって、奔流が発生している様子を示す。It is a partially enlarged explanatory view of FIG. 3 and shows a state in which a torrent is occurring.

以下、本発明の実施形態を添付図面を参照しながら説明する。図1に本発明に係る湿式ガス状物質処理装置の一つの実施の形態を示す。 Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. FIG. 1 shows one embodiment of the wet particulate matter treatment apparatus according to the present invention.

図1〜図4において、符号10は本発明の湿式ガス状物質処理装置である。 In FIGS. 1 to 4, reference numeral 10 is a wet particulate matter processing apparatus of the present invention.

湿式ガス状物質処理装置10は、処理室12と、前記処理室上部に設けられ、装置外部のガス状物質を前記処理室12内に吸入させるための吸気ファン14と、前記処理室12に形成され前記処理室12内にガス状物質を吸入させるためのガス状物質吸入口16と、前記処理室12に形成され前記処理室12内に吸入されたガス状物質を前記処理室12外に排出させるガス状物質排出口18と、前記処理室12内に設けられた貯水槽20と、前記ガス状物質吸入口16から吸入されるガス状物質と前記ガス状物質排出口18から排出されるガス状物質とを前記処理室12内で仕切るように、前記貯水槽20の静止水面の上方に垂設せしめられてなる垂設仕切板22と、前記ガス状物質排出口18側の前記貯水槽20の静止水面と平行して、前記貯水槽20の静止水面の上方に設置され、前記貯水槽20の水面に奔流を発生せしめるための波状多孔質奔流発生板24と、前記波状多孔質奔流発生板24の上方に設置され、前記奔流により生じる飛沫を受けるための少なくとも一つの多孔質邪魔板26a,26b,26cと、前記垂設仕切板22に、下端に行くに従って前記垂設仕切板22から離間するように傾斜して設けられた傾斜規制板28と、を有している。そして、前記垂設仕切板22よりも前記傾斜規制板28の方が下方に延出せしめられてなり、前記処理室12内に吸入されたガス状物質が前記貯水槽20の水と接触することによって浄化されるようにした、湿式ガス状物質処理装置である。 The wet gaseous substance processing apparatus 10 is formed in the processing chamber 12, the intake fan 14 provided in the upper part of the processing chamber and for sucking the gaseous substance outside the apparatus into the processing chamber 12, and the processing chamber 12. The gaseous substance suction port 16 for sucking the gaseous substance into the processing chamber 12 and the gaseous substance formed in the processing chamber 12 and sucked into the processing chamber 12 are discharged to the outside of the processing chamber 12. The gaseous substance discharge port 18 to be caused, the water storage tank 20 provided in the treatment chamber 12, the gaseous substance sucked from the gaseous substance suction port 16, and the gas discharged from the gaseous substance discharge port 18. A vertical partition plate 22 vertically provided above the static water surface of the water storage tank 20 so as to partition the state substance in the treatment chamber 12, and the water storage tank 20 on the gaseous substance discharge port 18 side. A wavy porous torrent generator 24, which is installed above the static water surface of the water storage tank 20 in parallel with the static water surface of the water storage tank 20 to generate a torrent on the water surface of the water storage tank 20, and a wavy porous torrent generator. At least one porous obstruction plate 26a, 26b, 26c installed above the 24 and for receiving the droplets generated by the torrent, and the vertical partition plate 22 are separated from the vertical partition plate 22 toward the lower end. It has an inclination control plate 28 provided so as to be inclined. Then, the inclination control plate 28 extends downward from the vertical partition plate 22, and the gaseous substance sucked into the treatment chamber 12 comes into contact with the water in the water storage tank 20. It is a wet gaseous substance treatment device that has been made to be purified by.

図示例では、処理室12の下部が貯水槽20とされている。貯水槽20には、弁付きの給排水口30が備わっているので、給水や排水を行うことができる。また、多孔質邪魔板は、図示例では、多孔質邪魔板26a,26b,26cの三枚設けた例を示した。多孔質邪魔板は少なくとも一つ設ければよいが、複数枚設けるのが好適である。 In the illustrated example, the lower part of the treatment chamber 12 is a water storage tank 20. Since the water storage tank 20 is provided with a water supply / drainage port 30 with a valve, water can be supplied and drained. Further, in the illustrated example, three porous baffle plates 26a, 26b, and 26c are provided as the porous baffle plate. At least one porous baffle plate may be provided, but it is preferable to provide a plurality of porous baffle plates.

また、前記多孔質邪魔板26a,26b,26cは、図3によく示されるように、前記貯水槽20の静止水面に対して傾斜して設けられている。静止水面の水位は、図示例では、図3に示すようにT1の位置である。また、図示例では、波状多孔質奔流発生板24及び多孔質邪魔板26a,26b,26cは、パンチングメタルで作製した例を示した。 Further, as shown in FIG. 3, the porous baffle plates 26a, 26b, and 26c are provided so as to be inclined with respect to the static water surface of the water storage tank 20. In the illustrated example, the water level on the static water surface is the position of T1 as shown in FIG. Further, in the illustrated example, the wavy porous torrent generation plate 24 and the porous obstruction plates 26a, 26b, and 26c are shown as examples made of punching metal.

波状多孔質奔流発生板24は、波状とされており、多数の孔が開穿されている。図示例では波状多孔質奔流発生板24は、SUS製のパンチングメタルを使用した例を示した。例えば、孔の直径が3mm〜5mm程度、開口率が50%〜60%程度、波高が10mm〜20mm程度のパンチングメタルが好適に使用できる。但し、波状多孔質奔流発生板24は、処理する風量、集塵されるゴミ種類や大きさなどによって、孔の直径を変えたり、波高或いは、折数(波の周期数)を変化させる。 The wavy porous torrent generation plate 24 is wavy and has a large number of holes. In the illustrated example, the corrugated porous torrent generating plate 24 shows an example in which a punching metal made of SUS is used. For example, a punching metal having a hole diameter of about 3 mm to 5 mm, an aperture ratio of about 50% to 60%, and a wave height of about 10 mm to 20 mm can be preferably used. However, the wavy porous torrent generation plate 24 changes the diameter of the hole, the wave height, or the number of folds (the number of wave periods) depending on the amount of air to be treated, the type and size of dust collected, and the like.

吸気ファン14は駆動モータ32で駆動されている。また、傾斜規制板28は、前記垂設仕切板22に対して傾斜して設けられているが、15°〜40°傾斜して設けるのが好適である。図示例では、図4に示すように傾斜規制板28の傾斜角度θは30°とされている。また、傾斜規制板28は垂設仕切板22に支持プレート34によっても支持されている。 The intake fan 14 is driven by a drive motor 32. Further, although the inclination control plate 28 is provided so as to be inclined with respect to the vertical partition plate 22, it is preferable that the inclination regulation plate 28 is provided so as to be inclined by 15 ° to 40 °. In the illustrated example, as shown in FIG. 4, the inclination angle θ of the inclination control plate 28 is 30 °. The inclination control plate 28 is also supported by the vertical partition plate 22 by the support plate 34.

図1〜3では、貯水槽20の水は静止水面の状態を示しており、湿式ガス状物質処理装置10のスイッチはOFFの状態である。図3には、ガス状物質の流れを示してある。ガス状物質吸入口16から湿式ガス状物質処理装置10の外の雰囲気が処理室12に吸入されることになるので、飲食店を含む店舗、製造工場や化学工場或いはプラントなどに湿式ガス状物質処理装置10を設置する場合、ガス状物質はガス状物質を含む空気となる。 In FIGS. 1 to 3, the water in the water storage tank 20 shows the state of the static water surface, and the switch of the wet particulate matter treatment device 10 is in the OFF state. FIG. 3 shows the flow of gaseous substances. Since the air outside the wet gaseous substance processing device 10 is sucked into the processing chamber 12 from the gaseous substance suction port 16, the wet gaseous substance is introduced into stores including restaurants, manufacturing factories, chemical factories, plants, and the like. When the processing device 10 is installed, the gaseous substance becomes air containing the gaseous substance.

処理室12には、ガス状物質吸入口16と連通する連通吸入開口部36と、ガス状物質排出口18と連通する連通排出開口部38とが形成されている。 The processing chamber 12 is formed with a communication suction opening 36 communicating with the gaseous substance suction port 16 and a communication discharge opening 38 communicating with the gaseous substance discharge port 18.

図3に、湿式ガス状物質処理装置10における貯水槽20の水は静止水面としたままで、ガス状物質の流れを示した。ガス状物質吸入口16からガス状物質が吸入されると(吸気)、処理室12へと送られて、貯水槽20の水と接触し、波状多孔質奔流発生板24及び多孔質邪魔板26a,26b,26cを通過して、ガス状物質排出口18から排出される(排気)。 FIG. 3 shows the flow of gaseous substances while the water in the water storage tank 20 in the wet gaseous substance treatment apparatus 10 remains on the static water surface. When the gaseous substance is sucked from the gaseous substance suction port 16 (intake), it is sent to the treatment chamber 12 and comes into contact with the water in the water storage tank 20, and the wavy porous torrent generation plate 24 and the porous obstruction plate 26a , 26b, 26c, and is discharged from the gaseous substance discharge port 18 (exhaust).

湿式ガス状物質処理装置10の外の汚れた空気を含むガス状物質は、ガス状物質吸入口16から処理室12に吸入され、垂設仕切板22によって貯水槽20へと送られて水を潜り抜けて貯水槽20を通り抜けてガス状物質排出口18から排出されるまで、貯水槽20は空気が漏れない構造とされている。 The gaseous substance containing dirty air outside the wet gaseous substance treatment device 10 is sucked into the treatment chamber 12 from the gaseous substance suction port 16 and sent to the water tank 20 by the vertical partition plate 22 to discharge water. The water tank 20 has a structure in which air does not leak until it passes through the water tank 20 and is discharged from the gaseous substance discharge port 18.

湿式ガス状物質処理装置10のスイッチをONとした状態の模式図を図4に示す。図4に示すように、湿式ガス状物質処理装置10のスイッチをONとすると、吸気ファン14によってガス状物質吸入口16からガス状物質が強制的に処理室12内に吸入されるため、貯水槽20内のガス状物質吸入口16側の水の水位が、図4の水位T2ぐらいまで下がる。 FIG. 4 shows a schematic view of a state in which the switch of the wet particulate matter processing apparatus 10 is turned on. As shown in FIG. 4, when the switch of the wet gaseous substance processing device 10 is turned on, the gaseous substance is forcibly sucked into the processing chamber 12 from the gaseous substance suction port 16 by the intake fan 14, so that water is stored. The water level of the water on the gaseous substance suction port 16 side in the tank 20 drops to about the water level T2 in FIG.

一方、ガス状物質はガス状物質排出口18から排出されるため、貯水槽20内のガス状物質排出口18の水Wの水位が上昇せしめられ、波状多孔質奔流発生板24に接触する水位T3となる。 On the other hand, since the gaseous substance is discharged from the gaseous substance discharge port 18, the water level of the water W of the gaseous substance discharge port 18 in the water tank 20 is raised, and the water level in contact with the wavy porous torrent generation plate 24. It becomes T3.

また、傾斜規制板28は、垂設仕切板22よりも下方に延出せしめられていることから、傾斜規制板28の裏側にはガス状物質の渦流40が出来る。そして、貯水槽20内の水Wは、ガス状物質とあわさって、波状多孔質奔流発生板24の孔にぶつかり、抜けようとして激しく奔流となって、波状多孔質奔流発生板24の全面から吹き上がる。この際に、気泡や飛沫も生じる。このように、吸気した汚れた空気を含むガス状物質の全てが水流に接触するようにされている。 Further, since the inclination control plate 28 extends downward from the vertical partition plate 22, a vortex 40 of a gaseous substance is formed on the back side of the inclination regulation plate 28. Then, the water W in the water storage tank 20 collides with the gaseous substance, collides with the holes of the wavy porous torrent generation plate 24, becomes a violent torrent trying to escape, and blows from the entire surface of the wavy porous torrent generation plate 24. Go up. At this time, bubbles and droplets are also generated. In this way, all of the gaseous substances including the inhaled dirty air are brought into contact with the water stream.

そのため、本発明の湿式ガス状物質処理装置10は、吸気ファンを貯水槽よりもガス状物質吸入口側に設置した装置(前方吸引型の湿式ガス状物質処理装置)であるが、吸気ファン14として風量が大きく、強力に外気を吸引する力を発揮するタイプのファンを使用しても、吸気した汚れた空気を含むガス状物質の全てが水流に接触し浄化される。従って、従来のように、汚れた空気を含むガス状物質が、僅かな隙間や穴から装置の外に吹きだしてしまうという問題や前記ガス状物質吸入口から吸入された汚れた空気を含むガス状物質が前記貯水槽の水とあまり接触しないまま、ガス状物質排出口から排出されてしまうという問題は発生しないのである。また、傾斜規制板28を設けたことで、従来よりも貯水槽20内の水Wが少なくて済むという利点もある。 Therefore, the wet gaseous substance processing apparatus 10 of the present invention is an apparatus (front suction type wet gaseous substance processing apparatus) in which the intake fan is installed closer to the gaseous substance suction port side than the water storage tank, but the intake fan 14 Even if a fan of the type that has a large air volume and exerts a strong force to suck in the outside air is used, all the gaseous substances including the intake dirty air come into contact with the water flow and are purified. Therefore, as in the conventional case, there is a problem that the gaseous substance containing dirty air is blown out of the device through a slight gap or hole, and the gaseous substance containing dirty air sucked from the gaseous substance suction port. The problem that the substance is discharged from the gaseous substance discharge port without being in much contact with the water in the water tank does not occur. Further, by providing the inclination control plate 28, there is an advantage that the amount of water W in the water storage tank 20 can be reduced as compared with the conventional case.

発生した奔流により、飛沫が生じるが飛沫の水滴42は、水面の上方に設置された多孔質邪魔板26a,26b,26cに当たって跳ね返され、貯水槽20へと戻される。 The generated torrent causes droplets to be generated, but the water droplets 42 are repelled by the porous baffle plates 26a, 26b, 26c installed above the water surface and returned to the water storage tank 20.

このようにして、ガス状物質は、貯水槽20の水Wと接触することによって浄化される。黒煙や油煙、塗料など粒子の大きいものは水Wによって除去される。そして、ガス状物質はガス状物質排出口16から排出される。 In this way, the gaseous substance is purified by coming into contact with the water W of the water tank 20. Large particles such as black smoke, oil smoke, and paint are removed by water W. Then, the gaseous substance is discharged from the gaseous substance discharge port 16.

また、ガス状物質排出口16には、脱臭装置を取付けても良く、例えば、特許文献1に示されるような加熱ヒータを用いた脱臭装置を取付けても良い。 Further, a deodorizing device may be attached to the gaseous substance discharge port 16, and for example, a deodorizing device using a heater as shown in Patent Document 1 may be attached.

本発明の湿式ガス状物質処理装置によれば、灯油、重油等の燃焼から発生するカーボン系超微粒子なども効率良く分離回収することができ、除塵も可能である。 According to the wet gaseous substance treatment apparatus of the present invention, carbon-based ultrafine particles generated from combustion of kerosene, heavy oil, etc. can be efficiently separated and recovered, and dust can be removed.

また、特許文献1に示すように、本発明の湿式ガス状物質処理装置には、循環ポンプによって貯水槽の水を循環水タンクへと循環させるように構成した循環濾過装置を取付けてもよい。 Further, as shown in Patent Document 1, the wet gaseous substance treatment device of the present invention may be equipped with a circulation filtration device configured to circulate the water in the water storage tank to the circulating water tank by a circulation pump.

飲食店などの店舗の厨房に設置する場合には、本発明の湿式ガス状物質処理装置のサイズを小さくしたものを用いるようにし、製造工場や化学工場、プラントに設置する場合には、湿式ガス状物質処理装置のサイズを大きくしたものを用いるようにすればよい。飲食店などの店舗に設置する場合には、調理に伴い生じる排煙などを効果的に分離除去することができる。また、湿式ガス状物質処理装置のサイズを小さくすれば、飲食店でも或いは工場や施設でも、卓上に置いて卓上用としての使用も可能である。このように、本発明の湿式ガス状物質処理装置は、排煙や排ガスが生じる様々な場所に設置することで、浄化処理を行うことが可能である。 When installing in the kitchen of a store such as a restaurant, use a smaller size of the wet gaseous substance processing device of the present invention, and when installing in a manufacturing factory, chemical factory, or plant, wet gas. It is sufficient to use a larger size of the state substance processing apparatus. When installed in a store such as a restaurant, it is possible to effectively separate and remove flue gas and the like generated by cooking. Further, if the size of the wet particulate matter processing apparatus is reduced, it can be placed on a tabletop and used as a tabletop in a restaurant, a factory or a facility. As described above, the wet gaseous substance treatment apparatus of the present invention can perform purification treatment by installing it in various places where flue gas and exhaust gas are generated.

なお、本発明は上記実施形態に限定されるものではない。上記形態は例示であり、本発の特許請求の範囲に記載された技術的思想と実質的に同一な構成を有し、かつ同様な作用効果を奏するものは、いかなるものであっても本発明の技術的範囲に包含される。 The present invention is not limited to the above embodiment. The above embodiment is an example, and any one having substantially the same structure as the technical idea described in the claims of the present invention and exhibiting the same effect and effect is the present invention. It is included in the technical scope of.

10:湿式ガス状物質処理装置、12:処理室、14:吸気ファン、16:ガス状物質吸入口、18:ガス状物質排出口、20:貯水槽、22:垂設仕切板、24:波状多孔質奔流発生板、26a,26b,26c:多孔質邪魔板、28:傾斜規制板、30:給排水口、32:駆動モータ、34:支持プレート、36:連通吸入開口部、38:連通排出開口部、40:渦流、42:水滴、T1,T2,T3:水位、W:水。 10: Wet gaseous substance treatment device, 12: Treatment chamber, 14: Intake fan, 16: Gastric substance inlet, 18: Gastric substance discharge port, 20: Water storage tank, 22: Vertical partition plate, 24: Wavy Porous torrent generator, 26a, 26b, 26c: Porous obstruction plate, 28: Tilt control plate, 30: Water supply / drainage port, 32: Drive motor, 34: Support plate, 36: Communication suction opening, 38: Communication discharge opening Part, 40: vortex, 42: water droplet, T1, T2, T3: water level, W: water.

Claims (3)

処理室と、
前記処理室上部に設けられ、装置外部のガス状物質を前記処理室内に吸入させるための吸引ファンと、
前記処理室に形成され前記処理室内にガス状物質を吸入させるためのガス状物質吸入口と、
前記処理室に形成され前記処理室内に吸入されたガス状物質を前記処理室外に排出させるガス状物質排出口と、
前記処理室内に設けられた貯水槽と、
前記ガス状物質吸入口から吸入されるガス状物質と前記ガス状物質排出口から排出されるガス状物質とを前記処理室内で仕切るように、前記貯水槽の静止水面の上方に垂設せしめられてなる垂設仕切板と、
前記ガス状物質排出口側の前記貯水槽の静止水面と平行して、前記貯水槽の静止水面の上方に設置され、前記貯水槽の水面に奔流を発生せしめるための波状多孔質奔流発生板と、
前記波状多孔質奔流発生板の上方に設置され、前記奔流により生じる飛沫を受けるための少なくとも一つの多孔質邪魔板と、
前記垂設仕切板に、下端に行くに従って前記垂設仕切板から離間するように傾斜して設けられた傾斜規制板と、
を有し、
前記垂設仕切板よりも前記傾斜規制板の方が下方に延出せしめられてなり、
前記処理室内に吸入されたガス状物質が前記貯水槽の水と接触することによって浄化されるようにした、湿式ガス状物質処理装置。
Processing room and
A suction fan provided in the upper part of the processing chamber for sucking gaseous substances outside the apparatus into the processing chamber,
A gaseous substance suction port formed in the processing chamber for sucking a gaseous substance into the processing chamber,
A gaseous substance discharge port formed in the treatment chamber and sucked into the treatment chamber to discharge the gaseous substance to the outside of the treatment chamber,
A water tank provided in the treatment chamber and
The gaseous substance sucked from the gaseous substance suction port and the gaseous substance discharged from the gaseous substance discharge port are vertically installed above the static water surface of the water storage tank so as to partition the gaseous substance discharged from the gaseous substance discharge port in the treatment chamber. With a vertical partition plate
A wavy porous torrent generator plate installed above the static water surface of the water tank in parallel with the static water surface of the water tank on the gaseous substance discharge port side to generate a torrent on the water surface of the water tank. ,
At least one porous obstruction plate installed above the wavy porous torrent generation plate to receive droplets generated by the torrent, and
An inclination control plate provided on the vertical partition plate so as to be inclined away from the vertical partition plate toward the lower end.
Have,
The inclination control plate is extended downward rather than the vertical partition plate.
A wet gaseous substance treatment apparatus in which a gaseous substance sucked into the treatment chamber is purified by coming into contact with water in the water storage tank.
前記多孔質邪魔板が、前記貯水槽の静止水面に対して傾斜して設けられ、且つ複数枚設けられてなる、請求項1記載の湿式ガス状物質処理装置。 The wet gaseous substance treatment apparatus according to claim 1, wherein the porous baffle plate is provided so as to be inclined with respect to the static water surface of the water storage tank, and a plurality of the porous baffle plates are provided. 前記傾斜規制板が、前記垂設仕切板に対して15°〜40°傾斜して設けられてなる、請求項1又は2記載の湿式ガス状物質処理装置。 The wet gaseous substance treatment apparatus according to claim 1 or 2, wherein the inclination control plate is provided at an inclination of 15 ° to 40 ° with respect to the vertical partition plate.
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