TW201932184A - Wet-type processing device for a gaseous substance for the gaseous substance sucked into the processing chamber to reliably contact with the water in the water storage tank even if the air volume of the air-intaking fan provided on the gaseous substance suction inlet side is increased - Google Patents
Wet-type processing device for a gaseous substance for the gaseous substance sucked into the processing chamber to reliably contact with the water in the water storage tank even if the air volume of the air-intaking fan provided on the gaseous substance suction inlet side is increased Download PDFInfo
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- TW201932184A TW201932184A TW107106347A TW107106347A TW201932184A TW 201932184 A TW201932184 A TW 201932184A TW 107106347 A TW107106347 A TW 107106347A TW 107106347 A TW107106347 A TW 107106347A TW 201932184 A TW201932184 A TW 201932184A
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- gaseous substance
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- 239000000126 substance Substances 0.000 title claims abstract description 131
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 120
- 238000003860 storage Methods 0.000 title claims abstract description 50
- 238000005192 partition Methods 0.000 claims abstract description 21
- 238000007599 discharging Methods 0.000 claims abstract 2
- 239000000463 material Substances 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 21
- 239000000428 dust Substances 0.000 description 8
- 239000000779 smoke Substances 0.000 description 5
- 239000002184 metal Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003973 paint Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 239000011882 ultra-fine particle Substances 0.000 description 3
- 239000010425 asbestos Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000001877 deodorizing effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- -1 etc. Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
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- Gas Separation By Absorption (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
Description
[0001] 本發明是關於：可將從包含飲食店在內的店舖、製造工場或化學工場、工廠等所排出的會對於環境造成不良影響的排氣、塗料粉塵、黑煙等的氣體狀物質進行分離去除之可進行濕式的排氣處理暨除塵處理之氣體狀物質處理裝置，尤其是關於：可有效地將因為燃燒煤油、重油等而產生的碳系超細微粒子以及因為塗裝等而產生的細微粉塵予以進行分離回收的氣體狀物質之濕式處理裝置。[0001] The present invention relates to a gaseous substance such as exhaust gas, paint dust, or black smoke which can be adversely affected from the environment discharged from a shop, a manufacturing plant, a chemical factory, a factory, or the like including a restaurant. A gas-like substance treatment apparatus capable of performing a wet exhaust treatment and a dust removal treatment, in particular, relates to: carbon-based ultrafine particles which are generated by burning kerosene, heavy oil, etc., and coating, etc. The resulting fine dust is subjected to a wet processing apparatus for separating and recovering gaseous substances.
[0002] 已知的使用水來進行排氣處理的濕式排氣處理裝置，係有：排氣洗淨塔裝置。以往的排氣洗淨塔裝置，係有各種形式，例如：將水或脫臭劑液體對於排氣進行噴霧的形式的裝置；將排氣與水往上吸之後，宛如形成水瀑布這樣地使得排氣衝撞通過水幕的形式的裝置；利用噴霧噴嘴形成噴霧水層，並且使排氣交替地通過噴霧水層與過濾層的形式的裝置。此外，也有的方式是採用：將水散佈於石棉、不織布、鐵絲網等的同時，使得排氣通過該石棉、不織布、鐵絲網，而將粉塵、水溶性氣體溶入水中的方式，然而，在其排氣中會排出霧狀的水分，因此就環保上的觀點而言，並不太好。 [0003] 上述之這種習知的裝置，因為裝置趨於複雜而會有容易發生故障的問題。此外，如果是使用過濾芯的形式的裝置，必須更換過濾芯，而且上述的那種習知的使用水的裝置，則必須用到噴霧器和供水泵浦之類的個別的裝置，在維修保養上也會有費工費時的問題。此外，上述的那種習知的使用水的裝置，必須使用大量的水。因此，本案的申請人，曾經提出一種技術方案係如專利文獻1所揭示的氣體狀物質之濕式處理裝置，且獲得好評。 [0004] 然而，專利文獻1所示的氣體狀物質之濕式處理裝置，如果是將其中的吸氣風扇設置在較之儲水槽更靠近氣體狀物質吸入口側的裝置情況下(即，前方吸氣型的氣體狀物質之濕式處理裝置的情況下)，為了想要提高來自氣體狀物質吸入口的風量而使用大風量的吸氣風扇來增強吸力的話，會有下列的問題點。 [0005] 如果是前方吸引型的氣體狀物質之濕式處理裝置的情況下，被吸入的氣體狀物質將會以較大的風壓來與氣體狀物質吸入口側的儲水槽的水面進行撞擊，因而產生了：含有髒空氣的氣體狀物質將從微小的間隙或孔穴洩漏到裝置外部之問題。 [0006] 此外，如果是前方吸引型的氣體狀物質之濕式處理裝置的情況下，若採用大風量的吸氣風扇的話，因為受到大風壓的影響，使得氣體狀物質吸入口側的儲水槽的水面被大幅往下壓低，因而產生了：從前述氣體狀物質吸入口所吸入的含有髒空氣的氣體狀物質還不太與前述儲水槽的水進行接觸，就被從氣體狀物質排出口排出到外部之問題。 [先前技術文獻] [專利文獻] [0007] [專利文獻1]日本特開2017-104843號公報[0002] A known wet exhaust gas treatment device that performs exhaust gas treatment using water is an exhaust gas purification tower device. The conventional exhaust gas cleaning tower apparatus is in various forms, for example, a device in which water or a deodorant liquid is sprayed on the exhaust gas; after the exhaust gas and the water are sucked up, it is like forming a water waterfall. The exhaust gas collides with a device in the form of a water curtain; a spray water layer is formed using a spray nozzle, and the exhaust gas is alternately passed through a device in the form of a spray water layer and a filter layer. In addition, there are also ways to: disperse water in asbestos, non-woven fabric, wire mesh, etc., so that the exhaust gas passes through the asbestos, non-woven fabric, and wire mesh, and the dust and water-soluble gas are dissolved in the water, however, in the row The mist will be discharged from the gas, so it is not very good from the viewpoint of environmental protection. [0003] The above-described conventional device has a problem that it is prone to malfunction because the device tends to be complicated. In addition, if it is a device in the form of a filter cartridge, the filter cartridge must be replaced, and the conventional water-using device described above must use a separate device such as a sprayer and a water supply pump for maintenance. There will also be problems with labor and time. Further, the conventional water-using device of the above type must use a large amount of water. Therefore, the applicant of the present application has proposed a wet processing apparatus for a gaseous substance as disclosed in Patent Document 1, and has been well received. [0004] However, the wet processing apparatus for a gaseous substance shown in Patent Document 1 is a case where the intake fan is disposed closer to the gas substance suction port side than the water storage tank (ie, the front side) In the case of a wet processing apparatus for a gas-inhalation type gas-like substance, in order to increase the amount of air from the gas-like substance suction port and use a large-volume intake fan to increase the suction force, the following problems may occur. [0005] In the case of a wet processing apparatus of a forward-suction type gaseous substance, the inhaled gaseous substance will collide with the water surface of the water storage tank side of the gas-like substance suction port with a large wind pressure. Thus, there is a problem that a gaseous substance containing dirty air leaks from a minute gap or a cavity to the outside of the apparatus. [0006] In addition, in the case of a wet processing apparatus of a gas-inducing type of a front suction type, if a large-volume intake fan is used, the gas-like substance suction port side is stored due to the influence of the large wind pressure. The water surface of the water tank is lowered downwards substantially, so that the gaseous substance containing the dirty air sucked from the gas-like substance suction port is not in contact with the water of the water storage tank, and is discharged from the gas-like substance. The problem of being discharged to the outside. [Prior Art Document] [Patent Document] [0007] [Patent Document 1] JP-A-2017-104843
[發明所欲解決的技術課題] [0008] 本發明是有鑑於上述習知技術的問題點而進行開發完成的，其目的是要提供一種氣體狀物質之濕式處理裝置，其係製作成：即使提高了設置在氣體狀物質吸入口側的吸氣風扇的風量，被吸入到處理室內的氣體狀物質還是可與儲水槽的水確實地進行接觸。 [用以解決課題的技術方案] [0009] 為了解決上述的技術課題，本發明的氣體狀物質之濕式處理裝置，其係具有：處理室；設在前述處理室上部，且用來將裝置外部的氣體狀物質吸入前述處理室內之吸氣風扇；形成在前述處理室，且用來將氣體狀物質吸入前述處理室內之氣體狀物質吸入口；形成在前述處理室，且用來將吸入到前述處理室內的氣體狀物質排出到前述處理室外之氣體狀物質排出口；設在前述處理室內之儲水槽；以可將從前述氣體狀物質吸入口吸入的氣體狀物質與即將從前述氣體狀物質排出口排出的氣體狀物質在前述處理室內區隔分開的方式，呈直立地設置在前述儲水槽的靜止水面的上方的直立隔板；與前述氣體狀物質排出口側的前述儲水槽的靜止水面保持平行地設置在前述儲水槽的靜止水面的上方，且用來使前述儲水槽的水面產生激流之波浪狀多孔質激流產生板；設置在前述波浪狀多孔質激流產生板的上方，且用來承接因前述激流而產生的飛沫之至少一個多孔質障板；以下端最為遠離前述直立隔板的方式呈傾斜地設於前述直立隔板的傾斜規制板；並且是製作成：使前述傾斜規制板較之前述直立隔板更朝下方延伸，使得被吸入到前述處理室內的氣體狀物質與前述儲水槽的水進行接觸而被淨化。 [0010] 前述多孔質障板是被設置成：對於前述儲水槽的靜止水面構成傾斜且設有複數片為宜。 [0011] 前述傾斜規制板是被設置成：對於前述直立隔板傾斜15°~40°為宜，傾斜20°~30°更好。 [0012] 在本說明書中所稱的氣體狀物質，係包含：排廢氣、塗料粉塵、黑煙、有毒氣體之類的會對於環境造成影響的氣體狀物質，也包含：因為燃燒煤油、重油等而產生的碳系超細微粒子及因進行塗裝作業而產生的細微粉塵。 [0013] 前述波浪狀多孔質激流產生板以及前述多孔質障板，是以利用打孔金屬板來構成的為宜。 [0014] 藉由採用本發明的氣體狀物質之濕式處理裝置，係可執行：藉由將被吸入前述處理室內的氣體狀物質與前述儲水槽的水進行接觸而受到淨化之濕式氣體狀物質處理方法。 [發明之效果] [0015] 根據本發明，係可達成提供：即使提高設置在氣體狀物質吸入口側的吸氣風扇的風量，還是可以讓被吸入到處理室內的氣體狀物質與儲水槽的水確實地進行接觸的氣體狀物質之濕式處理裝置之效果。[Technical Problem to be Solved by the Invention] The present invention has been developed in view of the above problems of the prior art, and an object thereof is to provide a wet processing apparatus for a gaseous substance, which is manufactured as follows: Even if the air volume of the intake fan provided on the gas-like substance suction port side is increased, the gaseous substance sucked into the processing chamber can surely come into contact with the water in the water storage tank. [Means for Solving the Problems] [0009] In order to solve the above-described technical problems, a wet processing apparatus for a gaseous substance according to the present invention includes a processing chamber, an upper portion of the processing chamber, and a device for An external gas-like substance is sucked into the suction fan in the processing chamber; a gas-like substance suction port formed in the processing chamber and used to suck the gaseous substance into the processing chamber; formed in the processing chamber, and used to be sucked into a gaseous substance in the processing chamber is discharged to a gas-like substance discharge port outside the processing chamber; a water storage tank provided in the processing chamber; and a gaseous substance that can be sucked from the gas-like substance suction port and a gas-like substance to be discharged from the gas-like substance The gas-like substance discharged from the discharge port is vertically separated from the stationary water surface of the water storage tank so as to be separated from the processing chamber; and the static water surface of the water storage tank on the discharge side of the gas-like substance Provided in parallel above the static water surface of the aforementioned water storage tank, and used to excite the water surface of the aforementioned water storage tank a wavy porous galvanic flow generating plate; at least one porous baffle disposed above the wavy porous torrent generating plate and for receiving droplets generated by the torrent; the lower end is farthest from the erect partition The method is disposed obliquely on the inclined regulation plate of the vertical partition plate; and is formed such that the inclined regulation plate extends downward from the vertical vertical partition plate so that the gaseous substance sucked into the processing chamber and the foregoing storage The water in the sink is cleaned by contact. [0010] The porous baffle plate is preferably provided such that the stationary water surface of the water storage tank is inclined and a plurality of sheets are provided. [0011] The inclined gauge plate is preferably disposed such that the vertical partition is inclined by 15° to 40°, and preferably inclined by 20° to 30°. [0012] The gaseous substance referred to in the present specification includes: a gaseous substance that affects the environment such as exhaust gas, paint dust, black smoke, and toxic gas, and also includes: burning kerosene, heavy oil, etc. The resulting carbon-based ultrafine particles and fine dust generated by the coating operation. [0013] The wavy porous torrent generating plate and the porous baffle plate are preferably formed of a perforated metal plate. [0014] By using the wet processing apparatus for a gaseous substance of the present invention, it is possible to perform a wet gas state which is purified by bringing a gaseous substance sucked into the processing chamber into contact with water of the water storage tank. Material handling method. [Effect of the Invention] According to the present invention, it is possible to provide a gas-like substance and a water storage tank that can be sucked into the processing chamber even if the air volume of the air suction fan provided on the gas-like substance suction port side is increased. The effect of a wet processing apparatus for a gaseous substance in which water is reliably contacted.
[0017] 以下，將佐以附圖來說明本發明的實施方式。第1圖是顯示本發明的氣體狀物質之濕式處理裝置的一種實施方式。 [0018] 在第1圖~第4圖中，元件符號10是本發明的氣體狀物質之濕式處理裝置。 [0019] 氣體狀物質之濕式處理裝置10是具有：處理室12；設置在前述處理室上部之用來將裝置外部的氣體狀物質吸入到前述處理室12內的吸氣風扇14；形成在前述處理室12之用來將氣體狀物質吸入到前述處理室12內的氣體狀物質吸入口16；形成在前述處理室12之用來將被吸入到前述處理室12內的氣體狀物質予以排出前述處理室12外的氣體狀物質排出口18；設在前述處理室12內的儲水槽20；以可將從前述氣體狀物質吸入口16吸入的氣體狀物質與即將從前述氣體狀物質排出口18排出的氣體狀物質在前述處理室12內區隔分開的方式，呈直立地設置在前述儲水槽20的靜止水面的上方的直立隔板22；與前述氣體狀物質排出口18側的前述儲水槽20的靜止水面保持平行地設置在前述儲水槽20的靜止水面的上方，且用來使前述儲水槽20的水面產生激流之波浪狀多孔質激流產生板24；設置在前述波浪狀多孔質激流產生板24的上方，且用來承接因前述激流而產生的飛沫之至少一個多孔質障板26a、26b、26c；以下端最為遠離前述直立隔板22的方式呈傾斜地設於前述直立隔板22的傾斜規制板28。並且，是製作成：使前述傾斜規制板28較之前述直立隔板22更朝下方延伸，使得被吸入到前述處理室12內的氣體狀物質與前述儲水槽20的水進行接觸而被淨化。 [0020] 圖示的例子，處理室12的下部是設成儲水槽20。因為在儲水槽20是設置有：具備水閥的供水暨排水口30，所以可進行供水和排水。此外，關於多孔質障板，圖示的例子是顯示出設有三片多孔質障板26a、26b、26c的例子。雖然多孔質障板是至少設有一片即可，但是，設有複數片更好。 [0021] 又，如第3圖所示，前述多孔質障板26a、26b、26c是配置成：對於前述儲水槽20的靜止水面呈傾斜。如第3圖所示，靜止水面的水位是位於T1的位置。又，圖示的例子的波浪狀多孔質激流產生板24以及多孔質障板26a、26b、26c是以打孔金屬板來製作的例子。 [0022] 波浪狀多孔質激流產生板24是形成波浪狀並且穿設有許多孔。圖示的例子的波浪狀多孔質激流產生板24是採用SUS不鏽鋼板製的打孔金屬板的例子。可適合採用例如：打孔的直徑為3mm~5mm左右，開口率為50%~ 60%左右，波浪高度為10mm~20mm左右的打孔金屬板。但是波浪狀多孔質激流產生板24係可因應進行處理的風量、被集塵的灰塵種類和大小的不同，來改變打孔的直徑、波浪高度或折彎的數量(即，波浪的頻率)。 [0023] 吸氣風扇14是受到驅動用馬達32所驅動。又，傾斜規制板28是設成對於前述直立隔板22構成傾斜，並且是設成傾斜15°~40°為宜。圖示的例子，係如第4圖所示，傾斜規制板28的傾斜角度θ是30°。又，傾斜規制板28也利用支承片34來被支承在直立隔板22。 [0024] 第1圖~第3圖中，儲水槽20的水是顯示出靜止水面的狀態，氣體狀物質之濕式處理裝置10的開關是處在OFF的狀態。在第3圖中有顯示出氣體狀物質的流動。因為是從氣體狀物質吸入口16將氣體狀物質之濕式處理裝置10的外部的氣體吸入到處理室12內，因此若是將氣體狀物質之濕式處理裝置10設置在包含飲食店在內的店舖、製造工場、化學工場或工廠的話，所稱的氣體狀物質就是含有氣體狀物質的空氣。 [0025] 在處理室12係形成有：與氣體狀物質吸入口16相連通的連通吸入開口部36；以及與氣體狀物質排出口18相連通的連通排出開口部38。 [0026] 第3圖是顯示出氣體狀物質之濕式處理裝置10內的儲水槽20的水還保持在靜止水面的狀態下，氣體狀物質的流動。從氣體狀物質吸入口16吸入氣體狀物質(吸氣)之後，係送往處理室12，與儲水槽20的水進行接觸，並且通過波浪狀多孔質激流產生板24以及多孔質障板26a、26b、26c之後，從氣體狀物質排出口18排出(排氣)。 [0027] 含有氣體狀物質之濕式處理裝置10的外部髒空氣之氣體狀物質是從氣體狀物質吸入口16被吸入處理室12內，利用直立隔板22將其送往儲水槽20，穿過水並且通過儲水槽20之後被從氣體狀物質排出口18排出之前，儲水槽20的構造是不會讓空氣洩漏出去。 [0028] 第4圖是顯示將氣體狀物質之濕式處理裝置10的開關變成ON的狀態的示意圖。如第4圖所示，若將氣體狀物質之濕式處理裝置10的開關變成ON的話，係利用吸氣風扇14強制性地從氣體狀物質吸入口16將氣體狀物質吸入到處理室12內，因此，儲水槽20內的氣體狀物質吸入口16側的水之水位將下降到第4圖中的水位T2的程度。 [0029] 另一方面，因為氣體狀物質是從氣體狀物質排出口18排出，因而儲水槽20內的氣體狀物質排出口18的水W之水位則會上昇，而成為可與波浪狀多孔質激流產生板24進行接觸的水位T3。 [0030] 又，因為傾斜規制板28是較之直立隔板22更往下方延伸，所以在傾斜規制板28的背面側將會形成氣體狀物質的渦流40。並且儲水槽20內的水W會與氣體狀物質一起撞擊到波浪狀多孔質激流產生板24的孔，而在將要穿過孔的時候，形成很激烈的激流，從整個波浪狀多孔質激流產生板24往上噴。這個時候，也會產生氣泡和飛沫。全部之含有吸進來的髒空氣之氣體狀物質都會以這種方式與水流進行接觸。 [0031] 因此，本發明的氣體狀物質之濕式處理裝置10，雖然是將吸氣風扇設置在較之儲水槽更靠近氣體狀物質吸入口側的裝置(前方吸氣型的氣體狀物質之濕式處理裝置)，但即使是使用大風量之可發揮強大的吸引外氣的吸力的型式的風扇來作為吸氣風扇14，全部之含有吸入的髒空氣之氣體狀物質都會與水流進行接觸而受到淨化。因此，不會產生傳統裝置的那種含髒空氣的氣體狀物質從微小的間隙或孔穴噴出到裝置外部的問題、或者從前述氣體狀物質吸入口吸入之含髒空氣的氣體狀物質還不太充分與前述儲水槽的水進行接觸就被從氣體狀物質排出口排出的問題。此外，因為設置了傾斜規制板28，因而與傳統裝置相較，儲水槽20內的水W更為減少，這也是其優點。 [0032] 因為形成了激流而產生的具有飛沫的水滴42，將會與設置在水面上方的多孔質障板26a、26b、26c碰撞而被回彈而流回去儲水槽20。 [0033] 是以，氣體狀物質將會因為與儲水槽20的水W進行接觸而受到淨化。黑煙、油煙、塗料之類的較大型粒子則是被水W所去除掉。然後，氣體狀物質則是從氣體狀物質排出口16排出去。 [0034] 又，亦可在氣體狀物質排出口16安裝脫臭裝置，例如：專利文獻1所揭示的這樣，亦可安裝使用加熱器來進行脫臭的脱臭裝置。 [0035] 根據本發明的氣體狀物質之濕式處理裝置，針對於因燃燒煤油、重油等而產生的碳系超細微粒子亦可很有效率地分離回收，亦可進行除塵。 [0036] 又，亦可如專利文獻1所示般地，可在本發明的氣體狀物質之濕式處理裝置，安裝上利用循環泵浦來將儲水槽的水予以循環回到循環水槽的循環過濾裝置。 [0037] 如果是設置在飲食店之類的店舖的廚房內的話，可採用將本發明的氣體狀物質之濕式處理裝置的尺寸製作得小一點的裝置，如果是設置在製造工場或化學工場、工廠內的話，則可採用將氣體狀物質之濕式處理裝置的尺寸製作得大一些的裝置。如果是設置在飲食店之類的店舖的情況下，係可將烹飪調理時所產生的排煙之類的物質有效地予以分離去除。此外，如果將氣體狀物質之濕式處理裝置的尺寸製作成小型化的話，無論是使用在飲食店或工場、商業設施內，也都可以放置在桌面上，當作桌上型的裝置來使用。是以，本發明的氣體狀物質之濕式處理裝置，係可設置在會產生排煙、排氣的各種場所來進行淨化處理。 [0038] 此外，本發明並不侷限於上述實施方式。上述的實施方式只是舉例而已，只要是具有與本發明的申請專利範圍所述的技術思想實質上相同的結構且可達成同樣的作用效果者，無論是哪一種都被包含在本發明的技術範圍內。[0017] Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. Fig. 1 is a view showing an embodiment of a wet processing apparatus for a gaseous substance of the present invention. [0018] In the first to fourth figures, the reference numeral 10 is a wet processing apparatus for a gaseous substance of the present invention. [0019] The wet processing apparatus 10 for a gaseous substance has a processing chamber 12, and an intake fan 14 provided in an upper portion of the processing chamber for sucking a gaseous substance outside the apparatus into the processing chamber 12; a gas-like substance suction port 16 for sucking a gaseous substance into the processing chamber 12 in the processing chamber 12; and a gaseous substance formed in the processing chamber 12 for sucking into the processing chamber 12 to be discharged a gas-like substance discharge port 18 outside the processing chamber 12; a water storage tank 20 provided in the processing chamber 12; and a gas-like substance that can be sucked from the gas-like substance suction port 16 and a discharge port from the gas-like substance The gas-like substance discharged from the 18 is partitioned in the processing chamber 12 so as to be vertically disposed above the stationary water surface of the water storage tank 20; and the storage of the gas-like substance discharge port 18 side The static water surface of the water tank 20 is disposed in parallel above the stationary water surface of the water storage tank 20, and the wavy porous torrent generating plate 2 for causing the water surface of the water storage tank 20 to generate a torrent flow 4; at least one of the porous baffles 26a, 26b, 26c disposed above the wavy porous torrent generating plate 24 and for receiving the droplets generated by the torrent; the lower end is farthest from the erecting partition 22 The manner is obliquely provided on the inclined regulation plate 28 of the upright partition 22 described above. Further, the inclined regulation plate 28 is formed to extend downward from the vertical partition plate 22 such that the gaseous substance sucked into the processing chamber 12 comes into contact with the water of the water storage tank 20 to be purified. [0020] In the illustrated example, the lower portion of the processing chamber 12 is configured as a water storage tank 20. Since the water storage tank 20 is provided with a water supply and drain port 30 having a water valve, water supply and drainage can be performed. Further, regarding the porous baffle, an example shown is an example in which three porous baffles 26a, 26b, and 26c are provided. Although the porous baffle is provided with at least one sheet, it is more preferable to provide a plurality of sheets. Further, as shown in FIG. 3, the porous baffles 26a, 26b, and 26c are disposed to be inclined with respect to the stationary water surface of the water storage tank 20. As shown in Figure 3, the water level of the stationary water surface is at the position of T1. Moreover, the wavy porous torrent generating plate 24 and the porous baffles 26a, 26b, and 26c of the illustrated example are produced by punching a metal plate. [0022] The undulating porous torrent generating plate 24 is formed in a wave shape and is provided with a plurality of holes. The wavy porous spur generating plate 24 of the illustrated example is an example of a perforated metal plate made of SUS stainless steel. For example, a perforated metal plate having a diameter of about 3 mm to 5 mm, an opening ratio of 50% to 60%, and a wave height of about 10 mm to 20 mm can be suitably used. However, the wavy porous torrent generating plate 24 can change the diameter of the perforation, the wave height, or the number of bends (i.e., the frequency of the waves) in accordance with the amount of air to be treated, the type and size of the dust to be collected. [0023] The intake fan 14 is driven by the drive motor 32. Further, the inclined regulation plate 28 is preferably formed to be inclined with respect to the upright partition plate 22, and is preferably inclined at 15 to 40 degrees. In the illustrated example, as shown in Fig. 4, the inclination angle θ of the inclined regulation plate 28 is 30°. Further, the inclined regulation plate 28 is also supported by the upright partition 22 by the support piece 34. [0024] In the first to third figures, the water in the water storage tank 20 is in a state in which the stationary water surface is displayed, and the switch of the wet processing apparatus 10 for the gaseous substance is in an OFF state. The flow of the gaseous substance is shown in Fig. 3. Since the gas outside the wet processing apparatus 10 of the gaseous substance is sucked into the processing chamber 12 from the gas-like substance suction port 16, the wet processing apparatus 10 for the gaseous substance is installed in a restaurant including a restaurant. In the case of a shop, a manufacturing plant, a chemical factory, or a factory, the gaseous substance is a gas containing a gaseous substance. [0025] The processing chamber 12 is formed with a communication suction opening portion 36 that communicates with the gas-like substance suction port 16 and a communication discharge opening portion 38 that communicates with the gas-like material discharge port 18. 3 is a flow of a gaseous substance in a state where the water in the water storage tank 20 in the wet processing apparatus 10 of the gaseous substance is maintained on the stationary water surface. After the gaseous substance (intake) is taken in from the gas-like substance suction port 16, it is sent to the processing chamber 12, and is brought into contact with the water of the water storage tank 20, and passes through the wavy porous torrent generating plate 24 and the porous baffle 26a. After 26b and 26c, it is discharged (exhaust) from the gaseous substance discharge port 18. [0027] The gaseous substance of the external dirty air of the wet processing apparatus 10 containing a gaseous substance is sucked into the processing chamber 12 from the gaseous substance suction port 16, and is sent to the water storage tank 20 by the vertical partition 22, and is worn. Before passing through the water and passing through the gas storage tank 20 and being discharged from the gaseous substance discharge port 18, the configuration of the water storage tank 20 does not allow air to leak out. [0028] FIG. 4 is a schematic view showing a state in which the switch of the wet processing apparatus 10 for a gaseous substance is turned ON. As shown in FIG. 4, when the switch of the wet processing apparatus 10 for a gaseous substance is turned on, the gas-like substance is forcibly sucked into the processing chamber 12 from the gaseous substance suction port 16 by the suction fan 14. Therefore, the water level of the water-like substance suction port 16 side in the water storage tank 20 is lowered to the level of the water level T2 in Fig. 4 . On the other hand, since the gaseous substance is discharged from the gas-like substance discharge port 18, the water level of the water W in the gas-like substance discharge port 18 in the water storage tank 20 rises, and becomes wavy porous. The torrent generates a water level T3 at which the plate 24 makes contact. Further, since the inclined regulating plate 28 extends downward from the upright partition 22, a vortex 40 of a gaseous substance is formed on the back side of the inclined regulating plate 28. And the water W in the water storage tank 20 collides with the gaseous substance to hit the hole of the undulating porous torrent generating plate 24, and when passing through the hole, a very intense torrent is formed, resulting from the entire wavy porous torrent The plate 24 is sprayed upward. At this time, bubbles and droplets are also generated. All of the gaseous substances containing the inhaled dirty air come into contact with the water flow in this way. Therefore, the wet processing apparatus 10 for a gaseous substance of the present invention is a device in which the intake fan is disposed closer to the gas substance inlet side than the water storage tank (the gas type substance in front of the intake type) In addition, a type of fan that can exert a strong suction force for attracting outside air, which is a large amount of air, is used as the intake fan 14, and all of the gaseous substances containing the sucked dirty air come into contact with the water flow. Purified. Therefore, there is no problem that the gaseous substance containing the dirty air of the conventional device is ejected from the minute gap or the cavity to the outside of the device, or the gaseous substance containing the dirty air sucked from the gas-like substance suction port is not too small. The problem of being discharged from the gas-like material discharge port sufficiently in contact with the water of the aforementioned water storage tank. Further, since the inclined regulating plate 28 is provided, the water W in the water storage tank 20 is further reduced as compared with the conventional device, which is also an advantage. The water droplets 42 having droplets generated by the formation of the turbulent flow collide with the porous baffles 26a, 26b, and 26c provided above the water surface to be rebounded and flow back to the water storage tank 20. [0033] Therefore, the gaseous substance will be purified by contact with the water W of the water storage tank 20. Larger particles such as black smoke, soot, and paint are removed by water W. Then, the gaseous substance is discharged from the gaseous substance discharge port 16. Further, a deodorizing device may be attached to the gas-like substance discharge port 16. For example, as disclosed in Patent Document 1, a deodorizing device that uses a heater to perform deodorization may be attached. [0035] According to the wet processing apparatus for a gaseous substance of the present invention, the carbon-based ultrafine particles generated by burning kerosene, heavy oil, or the like can be efficiently separated and recovered, and dust can be removed. Further, as shown in Patent Document 1, in the wet processing apparatus for a gaseous substance of the present invention, the circulation of the water in the water storage tank can be recycled to the circulating water tank by circulation pumping. filter. [0037] If it is installed in a kitchen of a restaurant such as a restaurant, a device that makes the size of the wet processing device of the gaseous substance of the present invention smaller can be used, if it is installed in a manufacturing factory or a chemical factory. In the factory, a device having a larger size of a wet processing device for a gaseous substance can be used. In the case of a store such as a restaurant, it is possible to effectively separate and remove substances such as smoke generated during cooking conditioning. In addition, if the size of the wet processing device for gaseous substances is reduced to a small size, it can be placed on a tabletop as a desktop device, whether it is used in a restaurant, a factory, or a commercial facility. . Therefore, the wet processing apparatus for a gaseous substance of the present invention can be installed in various places where smoke and exhaust are generated to perform purification treatment. Further, the present invention is not limited to the above embodiment. The above-described embodiments are merely examples, and any one of them can be achieved in the technical scope of the present invention as long as it has substantially the same structure as the technical idea described in the patent application scope of the present invention. Inside.
[0039][0039]
10‧‧‧氣體狀物質之濕式處理裝置10‧‧‧ Wet treatment device for gaseous substances
12‧‧‧處理室12‧‧‧Processing room
14‧‧‧吸氣風扇14‧‧‧Inhalation fan
16‧‧‧氣體狀物質吸入口16‧‧‧Inhalation of gaseous substances
18‧‧‧氣體狀物質排出口18‧‧‧ gas-like substance discharge
20‧‧‧儲水槽20‧‧‧Water storage tank
22‧‧‧直立隔板22‧‧‧Upright partition
24‧‧‧波浪狀多孔質激流產生板24‧‧‧Wave-shaped porous torrent generation board
26a、26b、26c‧‧‧多孔質障板26a, 26b, 26c‧‧‧ porous baffles
28‧‧‧傾斜規制板28‧‧‧ Tilting regulation board
30‧‧‧供水暨排水口30‧‧‧Water supply and drain
32‧‧‧驅動用馬達32‧‧‧Drive motor
34‧‧‧支承片34‧‧‧Support piece
36‧‧‧連通吸入開口部36‧‧‧Connected to the suction opening
38‧‧‧連通排出開口部38‧‧‧Connecting discharge opening
40‧‧‧渦流40‧‧‧ eddy current
42‧‧‧水滴42‧‧‧ water droplets
T1、T2、T3‧‧‧水位T1, T2, T3‧‧‧ water level
W‧‧‧水W‧‧‧Water
[0016] 第1圖是顯示本發明的氣體狀物質之濕式處理裝置的一種實施方式的局部透視立體圖。 第2圖是將第1圖的氣體狀物質之濕式處理裝置由別的方向觀察時的局部透視立體圖。 第3圖是第1圖的氣體狀物質之濕式處理裝置的示意說明圖，係顯示靜止水面的狀態。 第4圖是第3圖的局部放大說明圖，係顯示產生了激流的狀態。1 is a partial perspective perspective view showing an embodiment of a wet processing apparatus for a gaseous substance of the present invention. Fig. 2 is a partial perspective perspective view of the wet processing apparatus for a gaseous substance of Fig. 1 when viewed from another direction. Fig. 3 is a schematic explanatory view of a wet processing apparatus for a gaseous substance according to Fig. 1, showing a state of a stationary water surface. Fig. 4 is a partially enlarged explanatory view of Fig. 3 showing a state in which a torrent is generated.
Claims (3)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2018-007588 | 2018-01-19 | ||
| JP2018007588A JP6906232B2 (en) | 2018-01-19 | 2018-01-19 | Wet particulate matter processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| TW201932184A true TW201932184A (en) | 2019-08-16 |
Family
ID=67472813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW107106347A TW201932184A (en) | 2018-01-19 | 2018-02-26 | Wet-type processing device for a gaseous substance for the gaseous substance sucked into the processing chamber to reliably contact with the water in the water storage tank even if the air volume of the air-intaking fan provided on the gaseous substance suction inlet side is increased |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JP6906232B2 (en) |
| TW (1) | TW201932184A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113983581B (en) * | 2021-11-02 | 2022-10-25 | 珠海格力电器股份有限公司 | Kitchen air conditioner |
| JP7458100B1 (en) | 2023-01-30 | 2024-03-29 | 株式会社ジョンクェルコンサルティング | Carbon dioxide treatment device and carbon dioxide treatment method |
| KR102638860B1 (en) * | 2023-09-08 | 2024-02-22 | 영진아이엔디(주) | Plasma scrubber system having powder trap inside water treatment tank and method for treating waste gas using the same |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08103620A (en) * | 1994-10-07 | 1996-04-23 | Dainaka Seiki Kk | Dust collection treating device |
| JP2001145916A (en) * | 1999-11-19 | 2001-05-29 | Kyc Machine Industry Co Ltd | Dust collector for mixer in batcher plant |
| JP6749146B2 (en) * | 2015-11-27 | 2020-09-02 | 株式会社ネイブヒート | Wet gaseous substance treatment equipment |
-
2018
- 2018-01-19 JP JP2018007588A patent/JP6906232B2/en active Active
- 2018-02-26 TW TW107106347A patent/TW201932184A/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| JP2019126743A (en) | 2019-08-01 |
| JP6906232B2 (en) | 2021-07-21 |
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