TW202210160A

TW202210160A - Particles capturing system

Info

Publication number: TW202210160A
Application number: TW109139767A
Authority: TW
Inventors: 董福慶; 王亘黼; 胡竹生; 鄭詠仁; 顏鴻程; 陳孟群
Original assignee: 財團法人工業技術研究院
Priority date: 2020-09-09
Filing date: 2020-11-13
Publication date: 2022-03-16
Also published as: TWI788729B; TWM609892U

Abstract

A particles capturing system includes: a venturi filter device which has an air intake portion, neck portion and air outtake portion; a cyclone filter device has entrance and exit, which is disposed in air outtake portion; a plurality of first nozzles for providing first water spray mist are disposed in venturi filter device; the horizontal height of each first nozzle position is higher than the horizontal height of neck portion; an air flow through venturi filter device, neck portion, first nozzles, cyclone filter device and exit, then flow out of cyclone filter device, and thereby capture and remove particles from the air.

Description

微粒捕集系統Particulate capture system

本發明涉及處理粉塵之技術領域，尤指一種微粒、粉塵、微細粉塵的捕集。The present invention relates to the technical field of dust processing, especially to the capture of particles, dust and fine dust.

在主要空汙來源中，粉塵、微粒(Particles)、微細粉塵(fine dust)扮演了關鍵的角色，因為粉塵、微粒、微細粉塵的體積極不可思議的細微，一旦暴露在充斥該類粉塵、微粒、微細粉塵的空氣中，便會對人體健康造成嚴重危害，尤其是呼吸道方面的疾病。Among the main sources of air pollution, dust, particles (Particles), fine dust (fine dust) play a key role, because the body of dust, particles, fine dust is incredibly fine, once exposed to the flood of such dust, particles, fine dust In the air of fine dust, it will cause serious harm to human health, especially respiratory diseases.

就高科技製造業的顆粒粉塵廢棄處理系統而言，許多廢氣減量過程中都需要收集微細粉塵。廢氣中的微細粉塵是極細的固體微粒，會長時間懸浮在空氣中。直徑超過10微米的粒子歸為粗微粒，這類顆粒微粒會被鼻毛或鼻咽腔內的黏膜吸附。直徑小於10微米(PM10)的微細粉塵屬於懸浮粒子，一旦吸入人體，將會沿著氣管與支氣管一直深入直達肺部。In the case of particulate dust disposal systems in high-tech manufacturing, many exhaust gas abatement processes require the collection of fine dust. Fine dust in exhaust gas is extremely fine solid particles that remain suspended in the air for a long time. Particles larger than 10 microns in diameter are classified as coarse particles, which are adsorbed by the nasal hairs or mucous membranes in the nasopharyngeal cavity. Fine dust with a diameter of less than 10 microns (PM10) belongs to suspended particles. Once inhaled into the human body, it will penetrate deep into the lungs along the trachea and bronchi.

直徑小於2.5微米的微細粉塵便屬於微細懸浮微粒(PM2.5)，而小於0.1微米者則屬於超微細懸浮微粒。包括PM10、PM2.5，在現有的氣體洗滌器(gas scrubber)和分離器(separator)都很難處理，因此可能造成排氣道阻塞。Fine dust with a diameter of less than 2.5 microns is classified as fine suspended particles (PM2.5), while those less than 0.1 microns are classified as ultra-fine suspended particles. Including PM10, PM2.5, in the existing gas scrubber (gas scrubber) and separator (separator) are difficult to handle, so it may cause exhaust duct blockage.

於各種加工製程中，常會產生許多粉塵、微粒、微細粉塵，必須將此類粉塵去除，以避免排放至大氣環境中。In various processing processes, many dusts, particles and fine dusts are often generated, and such dusts must be removed to avoid being discharged into the atmosphere.

就半導體製程所產生的廢氣而言，雖然大部分化學物質及粉塵/微粒能透過洗滌塔去除，但仍有極小尺寸(＜PM10)的粉塵無法有效除去。若將含有該類微粒、微細粉塵的廢氣排放到大氣環境，則會造成直接之空氣汙染及環境汙染。As for the waste gas generated by the semiconductor process, although most of the chemical substances and dust/particulates can be removed through the scrubber, there are still very small size (<PM10) dusts that cannot be effectively removed. If the exhaust gas containing such particles and fine dust is discharged into the atmospheric environment, it will cause direct air pollution and environmental pollution.

據此，如何發展出一種可有效收集、捕集粉塵、微粒、微細粉塵的「微粒捕集系統」，是相關技術領域人士亟待解決之課題。Accordingly, how to develop a "particle capture system" that can effectively collect and capture dust, particles, and fine dust is an urgent problem for those in the relevant technical fields.

於一實施例中，本發明提出一種微粒捕集系統，其包含：一文氏管過濾裝置，其具有一進氣部、一喉部與一出氣部，出氣部的水平高度高於進氣部的水平高度，喉部位於進氣部與出氣部之間，喉部的內徑小於進氣部與出氣部的內徑；一旋風式過濾裝置，設置於文氏管過濾裝置之出氣部，旋風式過濾裝置由複數過濾單元構成，各過濾單元包含一直型管部，直型管部之底部具有一錐型管部，直型管部的軸心垂直於水平面，錐型管部管徑較小的一端朝向喉部，複數過濾單元之直型管部的具有至少兩種尺寸，複數過濾單元層層套設，位於最外層之過濾單元具有一入口，入口的水平高度高於相鄰內層過濾單元之底部的水平高度，位於最內層之過濾單元的直型管部的頂部為一出口，出口的水平高度高於入口的水平高度；複數第一噴嘴，設置於文氏管過濾裝置內，複數第一噴嘴的水平高度高於喉部的水平高度，各複數第一噴嘴提供第一水霧，各第一水霧的噴灑方向大致平行於文氏管過濾裝置的軸心方向由第一噴嘴朝向喉部噴灑；以及氣體由進氣部之進氣口進入文氏管過濾裝置，依序通過喉部、複數第一噴嘴，由入口進入旋風式過濾裝置，由出口流出旋風式過濾裝置，藉此捕集氣體中之粉塵與微粒。In one embodiment, the present invention provides a particle capture system, comprising: A venturi filter device has an air inlet, a throat and an air outlet, the horizontal height of the air outlet is higher than the horizontal height of the air inlet, the throat is located between the air inlet and the air outlet, and the throat is located between the air inlet and the air outlet. The inner diameter is smaller than the inner diameter of the air inlet and the air outlet; A cyclone filter device is arranged at the air outlet of the venturi filter device. The cyclone filter device is composed of a plurality of filter units. Each filter unit includes a straight pipe portion. The bottom of the straight pipe portion has a conical pipe portion, which is straight The axis of the shaped tube part is perpendicular to the horizontal plane, the smaller end of the tapered tube part faces the throat, the straight tube parts of the plurality of filter units have at least two sizes, and the plurality of filter units are nested layer by layer and located in the outermost layer The filter unit has an inlet, the level of the inlet is higher than the level of the bottom of the adjacent inner filter unit, the top of the straight pipe part of the innermost filter unit is an outlet, and the level of the outlet is higher than the inlet. the horizontal height; A plurality of first nozzles are arranged in the venturi filter device, the horizontal height of the plurality of first nozzles is higher than the horizontal height of the throat, each of the plurality of first nozzles provides a first water mist, and the spraying directions of the first water mists are substantially parallel Sprayed from the first nozzle toward the throat in the axial direction of the venturi filter device; and The gas enters the venturi filter device from the air inlet of the air inlet, passes through the throat and the plurality of first nozzles in sequence, enters the cyclone filter device from the inlet, and flows out of the cyclone filter device from the outlet, thereby capturing the gas in the gas. Dust and particulates.

請參閱圖1所示，本發明所提供之一種粉塵微粒捕集系統100，其包含一文氏管過濾裝置10、一旋風式過濾裝置20、複數第一噴嘴30及複數第二噴嘴40。文氏管過濾裝置10與旋風式過濾裝置20大致同軸心C設置。Referring to FIG. 1 , a dust particle collection system 100 provided by the present invention includes a venturi filter device 10 , a cyclone filter device 20 , a plurality of first nozzles 30 and a plurality of second nozzles 40 . The venturi filter device 10 and the cyclone filter device 20 are arranged substantially coaxially C.

請參閱圖1及圖2A、2B所示，文氏管過濾裝置10具有一進氣部11、一喉部12與一出氣部13。進氣部11具有一進氣口111，提供氣體A進入進氣部11。通常，氣體A帶有含有汙染的粉塵、微粒、微細粉塵。Please refer to FIG. 1 and as shown in FIGS. 2A and 2B , the venturi filter device 10 has an air inlet portion 11 , a throat portion 12 and an air outlet portion 13 . The intake portion 11 has an intake port 111 for providing gas A into the intake portion 11 . Usually, the gas A contains dust, particulates, and fine dust containing contamination.

圖2A與圖2B是為了更清楚地本發明結構及氣體與水霧的流動，因此將圖1的粉塵微粒捕集系統100分為兩張圖面，然圖2A與圖2B為相連結的整體結構，可由圖2A頂部的與圖2B底部的標示得知二者的連結關係。FIGS. 2A and 2B are for the purpose of clarifying the structure of the present invention and the flow of gas and water mist. Therefore, the dust particle collection system 100 of FIG. 1 is divided into two drawings. However, FIGS. 2A and 2B are connected as a whole. For the structure, the connection relationship between the two can be known from the labels at the top of FIG. 2A and the bottom of FIG. 2B .

出氣部13的水平高度H₁₃ (如圖2B)高於進氣部11的水平高度H₁₁ (如圖2A)。喉部12位於進氣部11與出氣部13之間，喉部12的內徑小於進氣部11與出氣部13的內徑。在此實施例中，縮小的喉部內部的截面積，用以加大進氣之亂流流速，增加捕集粉塵、微粒、微細粉塵的效率。The horizontal height H ₁₃ of the air outlet portion 13 (as shown in FIG. 2B ) is higher than the horizontal height H ₁₁ of the air intake portion 11 (as shown in FIG. 2A ). The throat portion 12 is located between the air inlet portion 11 and the air outlet portion 13 , and the inner diameter of the throat portion 12 is smaller than the inner diameters of the air inlet portion 11 and the air outlet portion 13 . In this embodiment, the reduced cross-sectional area inside the throat is used to increase the turbulent flow velocity of the intake air and increase the efficiency of collecting dust, particles and fine dust.

如圖2A，文氏管過濾裝置10更包括一調整元件14，調整元件14具有一錐部141，錐部141具有直徑較小的一端(例如為一尖端)朝向喉部12。調整元件14可升降地設置於進氣部11，藉此改變氣體A由進氣部11通過喉部12時之允許通過的截面積，進而調整氣體A由進氣部11通過喉部12時之流速。As shown in FIG. 2A , the venturi filter device 10 further includes an adjusting element 14 , and the adjusting element 14 has a tapered portion 141 , and the tapered portion 141 has an end (eg, a tip) with a smaller diameter toward the throat portion 12 . The adjusting element 14 is arranged in the intake part 11 so as to be able to rise and fall, thereby changing the cross-sectional area of the gas A when it passes through the throat part 12 from the intake part 11 , and then adjusts the time when the gas A passes through the throat part 12 from the intake part 11 . flow rate.

於本實施例中，調整元件14連接於一調整齒輪組15，調整齒輪組15包括一第一齒輪組件151與一第二齒輪組件152。In this embodiment, the adjusting element 14 is connected to an adjusting gear set 15 , and the adjusting gear set 15 includes a first gear assembly 151 and a second gear assembly 152 .

第一齒輪組件151包括一第一齒輪1511與一第一桿體1512。第一桿體1512之兩端分別連接於調整元件14與第一齒輪1511，第一桿體1512之軸心方向垂直於水平面H。The first gear assembly 151 includes a first gear 1511 and a first rod body 1512 . Two ends of the first rod body 1512 are respectively connected to the adjusting element 14 and the first gear 1511 , and the axial direction of the first rod body 1512 is perpendicular to the horizontal plane H. As shown in FIG.

第二齒輪組件152，包括一第二齒輪1521與一第二桿體1522。第二桿體1522之一端連接於第二齒輪1521，第二桿體1522之另一端凸伸於文氏管過濾裝置10外。第二齒輪1521與第一齒輪1511相嚙合，藉由驅動第二桿體1522，同步帶動第二齒輪1521驅動第一齒輪1511旋轉，進而驅動第一桿體1512帶動調整元件14升降。在一實施例中，調整元件14可為一柱塞。The second gear assembly 152 includes a second gear 1521 and a second rod body 1522 . One end of the second rod body 1522 is connected to the second gear 1521 , and the other end of the second rod body 1522 protrudes out of the venturi filter device 10 . The second gear 1521 is meshed with the first gear 1511, and by driving the second rod 1522, the second gear 1521 is synchronously driven to drive the first gear 1511 to rotate, thereby driving the first rod 1512 to drive the adjusting element 14 to move up and down. In one embodiment, the adjustment element 14 may be a plunger.

在另一實施例中，可省略設置調整齒輪組15，亦即，氣體A進入喉部12允許通過的環狀截面積為固定。In another embodiment, the adjustment gear set 15 may be omitted, that is, the annular cross-sectional area of the gas A entering the throat 12 and allowing to pass through is fixed.

請參閱圖1及圖2A、2B所示，第一噴嘴30設置於文氏管過濾裝置10內，第一噴嘴30的水平高度H₃₀ (如圖2B)高於喉部12的水平高度H₁₂ (如圖2A)。各第一噴嘴30提供第一水霧M1，各第一水霧M1的噴灑方向大致平行於文氏管過濾裝置10的軸心C之方向，且由第一噴嘴30朝向喉部12噴灑，藉以洗滌粉塵、微粒、微細粉塵至下方收集桶。Referring to FIG. 1 and FIGS. 2A and 2B , the first nozzle 30 is disposed in the venturi filter device 10 , and the horizontal height H ₃₀ ( FIG. 2B ) of the first nozzle 30 is higher than the horizontal height H _{12 of the throat 12} (Figure 2A). Each first nozzle 30 provides a first water mist M1, and the spraying direction of each first water mist M1 is substantially parallel to the direction of the axis C of the venturi filter device 10, and is sprayed from the first nozzle 30 toward the throat 12, thereby Wash dust, particles, and fine dust to the collection bucket below.

如圖2B，於本實施例中，第一噴嘴30可為複數個，各第一噴嘴30之水平高度H₃₀ 為相同，且等距環繞文氏管過濾裝置10的軸心C設置。第一噴嘴30的數量不限，例如可至少為三個，且在以軸心C為中心的圓周上是等分地配置，例如，若設有三個第一噴嘴30，則第一噴嘴30間的夾角為120度，若設有四個第一噴嘴30，則第一噴嘴30間的夾角為90度。As shown in FIG. 2B , in this embodiment, the first nozzles 30 may be plural, and the horizontal heights H ₃₀ of the first nozzles 30 are the same, and are arranged equidistantly around the axis C of the venturi filter device 10 . The number of the first nozzles 30 is not limited, for example, there can be at least three, and they are equally arranged on the circumference with the axis C as the center. For example, if there are three first nozzles 30, the first nozzles 30 The included angle is 120 degrees. If four first nozzles 30 are provided, the included angle between the first nozzles 30 is 90 degrees.

請見圖1及圖2B，第二噴嘴40設置於靠近出氣部13且環繞旋風式過濾裝置20外圍。第二噴嘴40的水平高度H₄₀ 高於第一噴嘴30的水平高度H₃₀ 。各第二噴嘴40提供第二水霧M2，各第二水霧M2的噴灑方向大致平行於水平面H、或垂直於水平面且朝下方(未圖示)，且由第二噴嘴40朝向旋風式過濾裝置20內噴灑。Please refer to FIG. 1 and FIG. 2B , the second nozzle 40 is disposed near the air outlet 13 and surrounds the periphery of the cyclone filter device 20 . The horizontal height H ₄₀ of the second nozzle 40 is higher than the horizontal height H _{30 of the first nozzle 30} . Each second nozzle 40 provides a second water mist M2, the spraying direction of each second water mist M2 is substantially parallel to the horizontal plane H, or perpendicular to the horizontal plane and facing downward (not shown), and the second nozzle 40 is directed toward the cyclone filter The device 20 is sprayed.

如圖2B，於本實施例中，第二噴嘴40可為複數個，各第二噴嘴40之水平高度H₄₀ 為相同且等距環繞旋風式過濾裝置20的軸心C設置。第二噴嘴40的數量不限，例如可至少為三個，且在以軸心C為中心的圓周上是等分地配置，例如，若設有三個第二噴嘴40，則第二噴嘴40間的夾角為120度，若設有四個第二噴嘴40，則第二噴嘴40間的夾角為90度。As shown in FIG. 2B , in this embodiment, the second nozzles 40 may be plural, and the horizontal heights H ₄₀ of the second nozzles 40 are the same and are arranged equidistantly around the axis C of the cyclone filter device 20 . The number of the second nozzles 40 is not limited, for example, it can be at least three, and they are equally arranged on the circumference with the axis C as the center. For example, if there are three second nozzles 40, the second nozzles 40 The included angle is 120 degrees. If four second nozzles 40 are provided, the included angle between the second nozzles 40 is 90 degrees.

於進氣口111的下方設有一收集桶16，用以收集落下之第一水霧M1及第二水霧M2及捕集到的粉塵、微粒、微細粉塵。A collecting bucket 16 is provided below the air inlet 111 for collecting the falling first water mist M1 and the second water mist M2 and the collected dust, particles and fine dust.

於圖1、2A所示實施例中，進氣口111位於進氣部11之側邊，且位於收集桶16之上方，氣體A以平行於水平面H之方向進入進氣部11。除此之外，可依所需將進氣口111設置為其他態樣。In the embodiment shown in FIGS. 1 and 2A , the air inlet 111 is located on the side of the air inlet portion 11 and above the collecting bucket 16 , and the gas A enters the air inlet portion 11 in a direction parallel to the horizontal plane H. Besides, the air inlet 111 can be set to other shapes as required.

請參閱圖3所示，進氣口111位於進氣部11之底部，進氣口111連接一管體112且管體112的頂端凸伸於收集桶16之上方。氣體A以垂直於水平面H之方向進入進氣部11。管體112的上方設有一蓋體113，蓋體113與管體112之頂端具有一距離，氣體A由管體112之頂端流出後，再由蓋體113之四周流入進氣部11。Referring to FIG. 3 , the air inlet 111 is located at the bottom of the air inlet portion 11 , the air inlet 111 is connected to a pipe body 112 and the top of the pipe body 112 protrudes above the collecting bucket 16 . The gas A enters the air inlet 11 in a direction perpendicular to the horizontal plane H. As shown in FIG. A cover body 113 is arranged above the tube body 112 , and the cover body 113 has a distance from the top of the tube body 112 .

收集桶16之一側設有一排水管161，用以排除收集桶16中所收集的汙水。A drain pipe 161 is provided on one side of the collecting bucket 16 for draining the sewage collected in the collecting bucket 16 .

請參閱圖1及圖2A所示，文氏管過濾裝置10之喉部12設有一多孔性材料121，其具有特殊設計之多孔性結構，材質為金屬或聚合物，微生物會在其表面潤溼累積，以增大與第一水霧M1與第二水霧M2的表面接觸，並對第一水霧M1與第二水霧M2進行汙水降解分離處理。在另一實施例中，可省略多孔性材料121。Please refer to FIG. 1 and FIG. 2A , the throat 12 of the venturi filter device 10 is provided with a porous material 121 , which has a specially designed porous structure and is made of metal or polymer, and microorganisms will wet the surface of the porous material 121 . Accumulation, so as to increase the surface contact with the first water mist M1 and the second water mist M2, and perform sewage degradation and separation treatment on the first water mist M1 and the second water mist M2. In another embodiment, the porous material 121 may be omitted.

請參閱圖1及圖2B所示，旋風式過濾裝置20設置於文氏管過濾裝置10之出氣部13。旋風式過濾裝置20包括一第一過濾單元21、一第二過濾單元22、一第三過濾單元23及一第四過濾單元24。Please refer to FIG. 1 and FIG. 2B , the cyclone filter device 20 is disposed at the air outlet 13 of the venturi filter device 10 . The cyclone filter device 20 includes a first filter unit 21 , a second filter unit 22 , a third filter unit 23 and a fourth filter unit 24 .

第一過濾單元21具有一第一直型管部211及一第一錐型管部212，於第一直型管部211設有一第一開口213作為氣體的入口。第一直型管部211的軸心C垂直於水平面H。第一過濾單元21的第一錐型管部212的底部設有一第一下降管214，第一下降管214之軸向C長度之底部之水平高度H₂₁₄ 低於各第一噴嘴30之水平高度H₃₀ 。第一下降管214之底部具有一第一錐部215，第一錐部215具有管部管徑較小的一第一錐部開口217朝向喉部12(可參見圖1與圖2A)。The first filter unit 21 has a first straight pipe portion 211 and a first tapered pipe portion 212 , and a first opening 213 is provided in the first straight pipe portion 211 as a gas inlet. The axis C of the first straight pipe portion 211 is perpendicular to the horizontal plane H. As shown in FIG. A first descending pipe 214 is provided at the bottom of the first conical pipe portion 212 of the first filter unit 21 , and the horizontal height H ₂₁₄ of the bottom of the axial length C of the first descending pipe 214 is lower than the horizontal height of each first nozzle 30 H ₃₀ . The bottom of the first descending pipe 214 has a first tapered portion 215 , and the first tapered portion 215 has a first tapered portion opening 217 with a smaller pipe diameter facing the throat portion 12 (see FIGS. 1 and 2A ).

第二過濾單元22具有一第二直型管部221及一第二錐型管部222。第二直型管部221的外徑小於第一直型管部211的內徑，第二過濾單元22同軸心C設置於第一過濾單元21內。第二錐型管部222的底部的水平高度H₂₂₂ 低於第一開口213的水平高度H₂₁₃ 。The second filter unit 22 has a second straight pipe portion 221 and a second tapered pipe portion 222 . The outer diameter of the second straight pipe portion 221 is smaller than the inner diameter of the first straight pipe portion 211 , and the second filter unit 22 is coaxially disposed in the first filter unit 21 . The horizontal height H ₂₂₂ of the bottom of the second tapered tube portion 222 is lower than the horizontal height H _{213 of the first opening 213} .

第三過濾單元23具有一第三直型管部231及一第三錐型管部232。第三直型管部231的外徑小於第二直型管部221的內徑，第三過濾單元同軸心C設置於第二過濾單元22內。第三錐型管部232的底部的水平高度H₂₃₂ 低於第二錐型管部222的底部的水平高度H₂₂₂ 。The third filter unit 23 has a third straight pipe portion 231 and a third conical pipe portion 232 . The outer diameter of the third straight pipe portion 231 is smaller than the inner diameter of the second straight pipe portion 221 , and the third filter unit is coaxially disposed in the second filter unit 22 . The horizontal height H ₂₃₂ of the bottom of the third tapered tube portion 232 is lower than the horizontal height H 222 of the bottom of the second tapered tube portion ₂₂₂ .

於第三直型管部231設有一第三開口233，第三開口233的水平高度H₂₃₃ 高於第二錐型管部222的底部的水平高度H₂₂₂ 。第三過濾單元23的第三錐型管部232的底部設有一第三下降管234，第三下降管234之軸向C長度之底部之水平高度H₂₃₄ 高於第一錐型管部212的底部的水平高度H₂₁₂ 。第三下降管234之底部具有一第三錐部235，第三錐部235具有管徑較小的一第三錐部開口237朝向喉部12。在另一實施例中，第三下降管234之軸向C長度之底部之水平高度H₂₃₄ 可以視需求設置成為低於第一錐型管部212的底部的水平高度H₂₁₂ 。A third opening 233 is formed in the third straight tube portion 231 , and the horizontal height H ₂₃₃ of the third opening 233 is higher than the horizontal height H 222 of the bottom of the second tapered tube portion ₂₂₂ . A third descending pipe 234 is provided at the bottom of the third conical pipe portion 232 of the third filter unit 23 . The horizontal height H ₂₃₄ of the bottom of the axial length C of the third descending pipe 234 is higher than that of the first conical pipe portion 212 . The horizontal height H ₂₁₂ of the bottom. The bottom of the third descending pipe 234 has a third tapered portion 235 , and the third tapered portion 235 has a third tapered portion opening 237 with a smaller diameter toward the throat portion 12 . In another embodiment, the horizontal height H ₂₃₄ of the bottom of the axial C length of the third descending pipe 234 can be set to be lower than the horizontal height H ₂₁₂ of the bottom of the first tapered pipe portion 212 as required.

第四過濾單元24具有一第四直型管部241及一第四錐型管部242。第四直型管部241的外徑小於第三直型管部231的內徑，第四過濾單元24同軸心C設置於第三過濾單元23內。第四錐型管部242的底部的水平高度H₂₄₂ 低於第三開口233的水平高度H₂₃₃ 且高於第三錐型管部232的底部的水平高度H₂₃₂ ，第四直型管部241的頂部為氣體的出口。The fourth filter unit 24 has a fourth straight pipe portion 241 and a fourth conical pipe portion 242 . The outer diameter of the fourth straight pipe portion 241 is smaller than the inner diameter of the third straight pipe portion 231 , and the fourth filter unit 24 is coaxially disposed in the third filter unit 23 . The horizontal height H ₂₄₂ of the bottom of the fourth tapered tube portion 242 is lower than the horizontal height H 233 of the third opening ₂₃₃ and higher than the horizontal height H ₂₃₂ of the bottom of the third tapered tube portion 232 . The fourth straight tube portion 241 The top is the gas outlet.

請參閱圖2A、2B所示，完整說明微粒捕集系統100的氣體A及第一水霧M1與第二水霧M2的流動路徑。其中，實線箭頭代表氣體的路徑，虛線箭頭代表水霧的路徑。Please refer to FIGS. 2A and 2B for a complete description of the gas A and the flow paths of the first water mist M1 and the second water mist M2 of the particle capture system 100 . Among them, the solid arrows represent the path of the gas, and the dashed arrows represent the path of the water mist.

氣體A由進氣口111進入進氣部11，而後由調整元件14的週圍進入喉部12，可藉由調整齒輪組15控制調整元件14升降，改變允許通過喉部12的環狀截面積及氣體A進入喉部12的流速；例如，在一實施例中，使允許通過喉部12的環狀截面積縮小進而增大氣體A的流速，在另一實施例中，使允許通過喉部12的環狀截面積加大進而減小氣體A的流速。又在另一實施例中，可省略設置調整齒輪組15，使氣體允許通過喉部12的環狀截面積為固定。The gas A enters the air inlet 11 from the air inlet 111, and then enters the throat 12 from the surrounding of the adjusting element 14. The adjusting element 14 can be controlled to rise and fall by the adjusting gear set 15, and the annular cross-sectional area allowed to pass through the throat 12 and The flow rate of the gas A entering the throat 12; for example, in one embodiment, the annular cross-sectional area allowed to pass through the throat 12 is reduced to increase the flow rate of the gas A, and in another embodiment, the flow rate of the gas A allowed to pass through the throat 12 is reduced The annular cross-sectional area of is increased to reduce the flow rate of gas A. In yet another embodiment, the adjustment gear set 15 can be omitted, so that the annular cross-sectional area of the throat 12 that allows gas to pass through is fixed.

於第四直型管部241的頂部外可設置一抽氣風扇(圖中未示出)，以將氣體A由進氣口111抽入進氣部11。An air suction fan (not shown in the figure) may be disposed outside the top of the fourth straight pipe portion 241 to draw the gas A into the air inlet portion 11 from the air inlet 111 .

而後，氣體A通過多孔性材料121繼續向上流入出氣部13。當氣體A通過第一噴嘴30時，可藉由第一水霧M1的沖刷以捕集氣體A中所含的粉塵。Then, the gas A continues to flow upward into the gas outlet 13 through the porous material 121 . When the gas A passes through the first nozzle 30, the dust contained in the gas A can be captured by the flushing of the first water mist M1.

而後，帶著粉塵的第一水霧M1落入多孔性材料121，可由多孔性材料121對第一水霧M1進行汙水降解分離處理。通過多孔性材料121的第一水霧M1繼續下落至收集桶16中。在另一實施例中，可省略多孔性材料121。Then, the first water mist M1 with dust falls into the porous material 121 , and the first water mist M1 can be degraded and separated from sewage by the porous material 121 . The first water mist M1 passing through the porous material 121 continues to fall into the collecting tub 16 . In another embodiment, the porous material 121 may be omitted.

於此同時，氣體A仍繼續上行，由第一開口213進入第一過濾單元21。當氣體A通過第二噴嘴40時，可藉由第二水霧M2對氣體A進行第二次沖刷以捕集氣體A中所含的微粒，並阻隔微粒再進入第二過濾單元22。At the same time, the gas A continues to ascend, and enters the first filter unit 21 through the first opening 213 . When the gas A passes through the second nozzle 40 , the gas A can be washed for the second time by the second water mist M2 to capture the particles contained in the gas A, and prevent the particles from entering the second filter unit 22 .

帶著微粒的第二水霧M2通過第一錐型管部212、第一下降管214、第一錐部215與第一錐部開口217之後，落入多孔性材料121，由多孔性材料121對第二水霧M2進行汙水降解分離處理。通過多孔性材料121的第二水霧M2繼續下落至收集桶16中。After the second water mist M2 with particles passes through the first conical pipe part 212 , the first descending pipe 214 , the first conical part 215 and the opening 217 of the first conical part, it falls into the porous material 121 , and is removed by the porous material 121 . Sewage degradation and separation treatment is performed on the second water mist M2. The second water mist M2 passing through the porous material 121 continues to fall into the collecting tub 16 .

於此同時，氣體A由第二錐型管部222的底部流入第二過濾單元22，再由第三開口233進入第三過濾單元23，而氣體A中的粉塵、微粒受離心力與重力雙重作用落下，經第三錐部開口237排出，氣體A而後由第四錐型管部242的底部流入第四過濾單元24，最後，氣體A1由第四直型管部241的頂部流出旋風式過濾裝置20，亦即，由第四直型管部241的頂部流出的氣體A1已經是除去粉塵、微粒的氣體。At the same time, the gas A flows into the second filter unit 22 from the bottom of the second conical tube portion 222, and then enters the third filter unit 23 through the third opening 233, and the dust and particles in the gas A are subjected to the dual action of centrifugal force and gravity After falling, it is discharged through the opening 237 of the third conical portion, and the gas A flows into the fourth filter unit 24 from the bottom of the fourth conical pipe portion 242. Finally, the gas A1 flows out of the cyclone filter device from the top of the fourth straight pipe portion 241. 20, that is, the gas A1 flowing out from the top of the fourth straight pipe portion 241 is already the gas for removing dust and particles.

值得說明的是，如本發明技術領域人士所理解，旋風式過濾裝置20的工作原理為，當氣體A進入旋風式過濾裝置20、23時，可於旋風式過濾裝置20、23內部產生螺旋狀迴轉，氣體A中的粉塵、微粒受離心力與重力雙重作用而由氣體A中分離而由旋風式過濾裝置20的底部落出。據此，本發明特殊設計的第一過濾單元21、第二過濾單元22、第三過濾單元23及第四過濾單元24之多層套設結構，可對氣體A發揮雙重旋風式過濾效果。It should be noted that, as understood by those skilled in the art of the present invention, the working principle of the cyclone filter device 20 is that when the gas A enters the cyclone filter devices 20 and 23, a spiral shape can be generated inside the cyclone filter devices 20 and 23. Rotation, the dust and particles in the gas A are separated from the gas A by the double action of centrifugal force and gravity, and fall out from the bottom of the cyclone filter device 20 . Accordingly, the specially designed multi-layered structure of the first filter unit 21, the second filter unit 22, the third filter unit 23 and the fourth filter unit 24 of the present invention can exert a double cyclone filter effect on the gas A.

由第三過濾單元23及第四過濾單元24旋風分離出的微粒、微細粉塵，可藉由第三下降管234及第三錐部235之第三錐部開口237導引至第一下降管214、第一錐部215中，經由第一錐部開口217排出。同樣地，由第一過濾單元21、第二過濾單元22旋風分離出的粉塵，可落入第一下降管214、第一錐部215中，經由第一錐部開口217排出。，再導引至旋風式過濾裝置20外部。The particles and fine dust separated by the cyclone of the third filter unit 23 and the fourth filter unit 24 can be guided to the first downcomer 214 through the third downcomer 234 and the third cone opening 237 of the third cone 235 , In the first cone 215, the discharge is discharged through the first cone opening 217. Similarly, the dust separated by the cyclone of the first filter unit 21 and the second filter unit 22 can fall into the first down pipe 214 and the first cone 215 and be discharged through the first cone opening 217 . , and then guide it to the outside of the cyclone filter device 20 .

圖4至圖7為圖1實施例之旋風式過濾裝置之過濾單元之不同實施例之結構示意圖。請參閱圖4所示，第一過濾單元21A具有一第一直型管部211及一第一錐型管部212，第三過濾單元23A具有一第三直型管部231及一第三錐型管部232。相較於圖2B，圖4實施例的第一過濾單元21A及第三過濾單元23不具有圖2B所示第一下降管214及第一錐部215，以及不具有第三下降管234及第三錐部235。4 to 7 are schematic structural diagrams of different embodiments of the filter unit of the cyclone filter device of the embodiment of FIG. 1 . Please refer to FIG. 4 , the first filter unit 21A has a first straight pipe portion 211 and a first tapered pipe portion 212 , and the third filter unit 23A has a third straight pipe portion 231 and a third cone Type tube portion 232 . Compared with FIG. 2B , the first filter unit 21A and the third filter unit 23 of the embodiment of FIG. 4 do not have the first downcomer 214 and the first cone 215 shown in FIG. 2B , and do not have the third downcomer 234 and the Triple taper portion 235 .

請參閱圖5所示，本實施例是以圖4實施例結構為基礎，於第一過濾單元21B的第一錐型管部212的底部設有一第一料斗216，例如，為一空心圓柱，於第三過濾單元23B的第三錐型管部232的底部設有一第三料斗236，例如，為一空心圓柱，用以收集來自氣體中的粉塵、微粒。Please refer to FIG. 5. This embodiment is based on the structure of the embodiment shown in FIG. 4. A first hopper 216 is provided at the bottom of the first conical tube portion 212 of the first filter unit 21B, for example, a hollow cylinder. A third hopper 236 is disposed at the bottom of the third conical tube portion 232 of the third filter unit 23B, for example, a hollow cylinder for collecting dust and particles from the gas.

請參閱圖6所示，第一過濾單元21C具有一第一直型管部211、一第一錐型管部212部及第一下降管214。第三過濾單元23C具有一第三直型管部231、一第三錐型管部232及第三下降管234。相較於圖2B，本實施例的第一過濾單元21C及第三過濾單元23C不具有圖2B所示第一錐部215及第三錐部235。Referring to FIG. 6 , the first filter unit 21C has a first straight pipe portion 211 , a first tapered pipe portion 212 and a first descending pipe 214 . The third filter unit 23C has a third straight pipe portion 231 , a third tapered pipe portion 232 and a third descending pipe 234 . Compared with FIG. 2B , the first filter unit 21C and the third filter unit 23C of the present embodiment do not have the first tapered portion 215 and the third tapered portion 235 shown in FIG. 2B .

請參閱圖7所示，本實施例是以圖6實施例結構為基礎，於第一過濾單元21D的第一下降管214之底部設有一第一料斗216，例如，為一空心圓柱，於第三過濾單元23D的第三下降管234之底部設有一第三料斗236，例如，為一空心圓柱，分別收集來自氣體中的粉塵、微粒。Please refer to FIG. 7 , this embodiment is based on the structure of the embodiment shown in FIG. 6 . A first hopper 216 is provided at the bottom of the first descending pipe 214 of the first filter unit 21D, for example, a hollow cylinder. A third hopper 236 is disposed at the bottom of the third descending pipe 234 of the three filter units 23D, for example, a hollow cylinder, which collects dust and particles from the gas respectively.

圖4至圖7實施例顯示，本發明的過濾單元除了具有直型管部、錐型管部之外，另可依所需搭配錐部、下降管、料斗。The embodiments shown in FIGS. 4 to 7 show that the filter unit of the present invention not only has a straight pipe portion and a conical pipe portion, but also can be equipped with a conical portion, a descending pipe, and a hopper as required.

請參閱圖8所示，本實施例旋風式過濾裝置20E是以圖2A實施例為基礎，於第三過濾單元23與第四過濾單元24之間更包括一第五過濾單元25及一第六過濾單元26。Please refer to FIG. 8 , the cyclone filter device 20E of this embodiment is based on the embodiment of FIG. 2A , and further includes a fifth filter unit 25 and a sixth filter unit between the third filter unit 23 and the fourth filter unit 24 Filter unit 26.

第五過濾單元25具有一第五直型管部251及一第五錐型管部252，第五直型管部251的外徑小於第三直型管部231的內徑，第五過濾單元同軸心C設置於第三過濾單元23內。第五錐型管部252的底部的水平高度H₂₅₂ 低於第三開口233的水平高度H₂₃₃ 且高於第三錐型管部232的底部的水平高度H₂₃₂ 。The fifth filter unit 25 has a fifth straight pipe portion 251 and a fifth conical pipe portion 252. The outer diameter of the fifth straight pipe portion 251 is smaller than the inner diameter of the third straight pipe portion 231. The fifth filter unit The coaxial center C is arranged in the third filter unit 23 . The horizontal height H ₂₅₂ of the bottom of the fifth tapered tube portion 252 is lower than the horizontal height H 233 of the third opening ₂₃₃ and higher than the horizontal height H 232 of the bottom of the third tapered tube portion ₂₃₂ .

第六過濾單元26具有一第六直型管部261及一第六錐型管部262，第六直型管部261的外徑小於第五直型管部251的內徑，第六過濾單元26同軸心C設置於第五過濾單元25內。第六錐型管部262的底部的水平高度H₂₆₂ 低於第五錐型管部252的底部的水平高度H₂₅₂ ，於第六直型管部261設有一第六開口263，第六開口263的水平高度H₂₆₃ 高於第四錐型管部242的底部的水平高度H₂₄₂ 。The sixth filter unit 26 has a sixth straight pipe portion 261 and a sixth conical pipe portion 262. The outer diameter of the sixth straight pipe portion 261 is smaller than the inner diameter of the fifth straight pipe portion 251. The sixth filter unit 26 is coaxially arranged in the fifth filter unit 25 . The horizontal height H ₂₆₂ of the bottom of the sixth tapered tube portion 262 is lower than the horizontal height H ₂₅₂ of the bottom of the fifth tapered tube portion 252 . The sixth straight tube portion 261 is provided with a sixth opening 263 . The sixth opening 263 The horizontal height H ₂₆₃ of is higher than the horizontal height H 242 of the bottom of the fourth tapered tube portion ₂₄₂ .

第四過濾單元24同軸心設置於第六過濾單元26內，第四直型管部241的頂部為氣體A1的出口。The fourth filter unit 24 is coaxially disposed in the sixth filter unit 26, and the top of the fourth straight pipe portion 241 is the outlet of the gas A1.

圖8實施例之氣體A的流動方向為，由第一開口213進入第一過濾單元21，而後由第二錐型管部222的底部流入第二過濾單元22，再由第三開口233進入第三過濾單元23，而後由第五錐型管部252的底部流入第五過濾單元25，再由第六開口263進入第六過濾單元26，而後由第四錐型管部242的底部流入第四過濾單元24，最後，氣體A1由第四直型管部241的頂部流出旋風式過濾裝置20E。The flow direction of the gas A in the embodiment of FIG. 8 is that it enters the first filter unit 21 through the first opening 213 , then flows into the second filter unit 22 through the bottom of the second conical tube portion 222 , and then enters the second filter unit 22 through the third opening 233 The third filter unit 23 flows into the fifth filter unit 25 from the bottom of the fifth conical tube portion 252 , then enters the sixth filter unit 26 through the sixth opening 263 , and then flows into the fourth filter unit 26 from the bottom of the fourth conical tube portion 242 In the filter unit 24, finally, the gas A1 flows out of the cyclone filter device 20E from the top of the fourth straight pipe portion 241.

請參閱圖9所示，本實施例旋風式過濾裝置20F是以圖2A實施例為基礎，僅具有第一過濾單元21及第四過濾單元24。Referring to FIG. 9 , the cyclone filter device 20F of this embodiment is based on the embodiment of FIG. 2A , and only has a first filter unit 21 and a fourth filter unit 24 .

第一過濾單元21具有一第一直型管部211及一第一錐型管部212，於第一直型管部211設有一第一開口213作為入口。第四過濾單元24具有一第四直型管部241及一第四錐型管部242，第四直型管部241的頂部為氣體A1出口。The first filter unit 21 has a first straight pipe portion 211 and a first tapered pipe portion 212 , and a first opening 213 is provided in the first straight pipe portion 211 as an inlet. The fourth filter unit 24 has a fourth straight pipe portion 241 and a fourth conical pipe portion 242 , and the top of the fourth straight pipe portion 241 is the gas A1 outlet.

圖9實施例之氣體A的流動方向為，由第一開口213進入第一過濾單元21，而後由第四錐型管部242的底部流入第四過濾單元24，最後，氣體A1由第四直型管部241的頂部流出旋風式過濾裝置20F。The flow direction of the gas A in the embodiment of FIG. 9 is that it enters the first filter unit 21 from the first opening 213 , and then flows into the fourth filter unit 24 from the bottom of the fourth conical tube portion 242 . The top of the shaped pipe portion 241 flows out of the cyclone filter device 20F.

請參閱圖10所示，本實施例旋風式過濾裝置20G是以圖9實施例為基礎，位於最內層之第四過濾單元24內設有複數個子過濾單元27，各子過濾單元27具有一子直型管部271、一子錐型管部272及一子下降管274。子直型管部271的外徑小於位於最內層之第四過濾單元24的內徑。於各子直型管部271設有一子開口273，子開口273的水平高度H₂₇₃ 高於位於最內層之第四過濾單元24的第四錐型管部242的底部的水平高度H₂₄₂ ，各子過濾單元27的頂部相連通並與第四過濾單元24的第四直型管部241相連通。子下降管274的底部的水平高度H₂₇₄ 與位於最內層之第四過濾單元24的第四錐型管部242的底部的水平高度H₂₄₂ 大致相同，或亦可低於水平高度H₂₄₂ 。Please refer to FIG. 10 , the cyclone filter device 20G of this embodiment is based on the embodiment of FIG. 9 , and the fourth filter unit 24 located in the innermost layer is provided with a plurality of sub-filter units 27 , and each sub-filter unit 27 has a A sub-straight pipe portion 271 , a sub-tapered pipe portion 272 and a sub-downward pipe 274 are provided. The outer diameter of the sub-straight pipe portion 271 is smaller than the inner diameter of the fourth filter unit 24 located at the innermost layer. Each sub-straight pipe portion 271 is provided with a sub-opening 273, and the horizontal height H ₂₇₃ of the sub-opening 273 is higher than the horizontal height H ₂₄₂ of the bottom of the fourth conical pipe portion 242 of the fourth filter unit 24 located in the innermost layer, The tops of each sub-filter unit 27 communicate with each other and communicate with the fourth straight pipe portion 241 of the fourth filter unit 24 . The horizontal height H ₂₇₄ of the bottom of the sub-downpipe 274 is substantially the same as the horizontal height H ₂₄₂ of the bottom of the fourth conical pipe portion 242 of the fourth filter unit 24 located at the innermost layer, or may be lower than the horizontal height H ₂₄₂ .

請參閱圖10、10A所示，於本實施例中，位於最內層之第四過濾單元24之軸心C設有複數個子過濾單元27，且複數個子過濾單元27環繞於位於最內層之第四過濾單元24之軸心C等距設置。Referring to FIGS. 10 and 10A, in this embodiment, the axis C of the fourth filter unit 24 located in the innermost layer is provided with a plurality of sub-filter units 27, and the plurality of sub-filter units 27 surround the innermost layer of the filter unit 27. The axis C of the fourth filter unit 24 is equidistantly arranged.

圖10實施例之氣體A的流動方向為，由第一開口213進入第一過濾單元21，而後由第四錐型管部242的底部流入第四過濾單元24，再由各子開口273流入各子過濾單元27，最後，氣體A1由第四直型管部241的頂部匯集流出旋風式過濾裝置20G。在本實施例中，透過氣體螺旋狀漩渦繞著管壁的流動，使氣體與微粒產生分離，藉以捕集氣體中之粉塵與微粒。在另一實施例中，可在進入第二層旋風式過濾裝置入口前，透過另外增加之第二水霧噴灑，阻隔微粒再進入第二層，同時藉由第二水霧再次洗滌以捕集氣體中之粉塵、微粒、微細粉塵至下方收集桶。粉塵、微粒均通過層層套設之旋風式複數過濾單元，達成多重次捕集氣體中之粉塵與微粒。The flow direction of the gas A in the embodiment shown in FIG. 10 is that it enters the first filter unit 21 from the first opening 213 , then flows into the fourth filter unit 24 from the bottom of the fourth conical pipe portion 242 , and then flows into each of the sub-openings 273 . In the sub-filter unit 27, finally, the gas A1 is collected from the top of the fourth straight pipe portion 241 and flows out of the cyclone filter device 20G. In this embodiment, the gas and particles are separated through the flow of the gas spiral vortex around the pipe wall, so as to capture the dust and particles in the gas. In another embodiment, before entering the inlet of the cyclone filter device of the second layer, the second water mist spraying can be added to prevent the particles from entering the second layer, and at the same time, the second water mist can be washed again to capture the particles. Dust, particles, and fine dust in the gas are collected in the lower bucket. Dust and particles pass through the cyclone-type multiple filter units set in layers to achieve multiple capture of dust and particles in the gas.

上述圖2B、圖8至11所揭露的旋風式過濾裝置具有共同的結構特徵：各過濾單元皆包含一直型管部及錐型管部，直型管部的軸心垂直於水平面，錐型管部管徑較小的一端(尖端)朝向喉部，位於最外層之過濾單元具有一入口，入口的水平高度高於相鄰內層過濾單元之底部的水平高度，位於最內層之過濾單元的直型管部的頂部為一出口，出口的水平高度高於入口的水平高度。在一實施例中，位於最外層之過濾單元的入口可設置於管部的正中央、或是設置於管部的側邊。The cyclone filter devices disclosed in the above-mentioned FIGS. 2B and 8 to 11 have common structural features: each filter unit includes a straight pipe portion and a conical pipe portion, the axis of the straight pipe portion is perpendicular to the horizontal plane, and the conical pipe portion is perpendicular to the horizontal plane. The smaller end (tip) of the pipe diameter faces the throat, the filter unit located in the outermost layer has an inlet, the level of the inlet is higher than the level of the bottom of the adjacent inner layer filter unit, and the filter unit located in the innermost layer has an inlet. The top of the straight pipe is an outlet, and the level of the outlet is higher than that of the inlet. In one embodiment, the inlet of the filter unit located at the outermost layer may be disposed in the center of the pipe portion, or may be disposed at the side of the pipe portion.

另須說明的是，於上述實施例中所示各水平高度H_x 是相對於水平面H的距離，換言之，若是將圖1所示微粒捕集系統100旋轉九十度設置，亦即使軸心C平行於水平面H時，上述各水平高度H_x 可改以其他位置為基準，例如，可改以進氣口111為基準。It should also be noted that the horizontal heights H _x shown in the above-mentioned embodiments are the distances relative to the horizontal plane H. In other words, if the particle trapping system 100 shown in FIG. 1 is rotated by 90 degrees, the axis C When being parallel to the horizontal plane H, the above-mentioned horizontal heights H _x can be changed to take other positions as the reference, for example, the air inlet 111 can be changed to be the reference.

綜上所述，本發明所提供之微粒捕集系統，以文氏管過濾裝置搭配旋風式過濾裝置及兩段式噴霧，經實做樣品驗證，可有效捕集氣體中粒徑小於2.5μm(微米)的粉塵，有利於解決製程產生之微粒廢氣排放入大氣環境之問題。To sum up, the particle capture system provided by the present invention uses a Venturi filter device, a cyclone filter device and a two-stage spray. It is verified by actual samples that it can effectively capture the particle size in the gas less than 2.5μm ( Micron) dust is beneficial to solve the problem of particulate exhaust gas generated by the process being discharged into the atmospheric environment.

雖然本發明已以實施例揭露如上，然其並非用以限定本發明，任何所屬技術領域中具有通常知識者，在不脫離本發明的精神和範圍內，當可作些許的更動與潤飾，故本發明的保護範圍當視後附的申請專利範圍所界定者為準。Although the present invention has been disclosed above by the embodiments, it is not intended to limit the present invention. Anyone with ordinary knowledge in the technical field can make some changes and modifications without departing from the spirit and scope of the present invention. Therefore, The protection scope of the present invention shall be determined by the scope of the appended patent application.

100:微粒捕集系統 10:文氏管過濾裝置 11:進氣部 111:進氣口 112:管體 113:蓋體 12:喉部 121:多孔性材料 13:出氣部 14:調整元件 141:錐部 15:調整齒輪組 151:第一齒輪組件 1511:第一齒輪 1512:第一桿體 152:第二齒輪組件 1521:第二齒輪 1522:第二桿體 16:收集桶 161:排水管 20,20E,20F,20G:旋風式過濾裝置 21,21B,21C,21D:第一過濾單元 211:第一直型管部 212:第一錐型管部 213:第一開口 214:第一下降管 215:第一錐部 216:第一料斗 217:第一錐部開口 22:第二過濾單元 221:第二直型管部 222:第二錐型管部 23,23B,23C,23D:第三過濾單元 231:第三直型管部 232:第三錐型管部 233:第三開口 234:第三下降管 235:第三錐部 236:第三料斗 237:第三錐部開口 24:第四過濾單元 241:第四直型管部 242:第四錐型管部 25:第五過濾單元 251:第五直型管部 252:第五錐型管部 26:第六過濾單元 261:第六直型管部 262:第六錐型管部 263:第六開口 27:子過濾單元 271:子直型管部 272:子錐型管部 273:子開口 274:子下降管 30:第一噴嘴 40:第二噴嘴 A, A1:氣體 C:軸心 H:水平面 H₁₁ , H₁₂ , H₁₃ , H₃₀ , H₄₀ , H₂₁₂ , H₂₁₃ , H₂₁₄ , H₂₂₂ , H₂₃₂ , H₂₃₃ , H₂₃₄ , H₂₄₂ , H₂₅₂ , H₂₆₂ , H₂₆₃ , H₂₇₃ , H₂₇₄ :水平高度 M1:第一水霧 M2:第二水霧100: Particulate capture system 10: Venturi filter device 11: Air inlet 111: Air inlet 112: Tube body 113: Cover body 12: Throat 121: Porous material 13: Air outlet 14: Adjustment element 141: Cone 15: Adjustment gear set 151: First gear assembly 1511: First gear 1512: First rod body 152: Second gear assembly 1521: Second gear 1522: Second rod body 16: Collection bucket 161: Drain pipe 20 , 20E, 20F, 20G: cyclone filter device 21, 21B, 21C, 21D: first filter unit 211: first straight pipe part 212: first tapered pipe part 213: first opening 214: first descending pipe 215: first cone part 216: first hopper 217: first cone part opening 22: second filter unit 221: second straight pipe part 222: second conical pipe part 23, 23B, 23C, 23D: third Filter unit 231: Third straight pipe portion 232: Third tapered pipe portion 233: Third opening 234: Third descending pipe 235: Third tapered portion 236: Third hopper 237: Third tapered portion opening 24: Third Four filter units 241: Fourth straight pipe part 242: Fourth tapered pipe part 25: Fifth filter unit 251: Fifth straight pipe part 252: Fifth conical pipe part 26: Sixth filter unit 261: No. Six straight pipe part 262: Sixth tapered pipe part 263: Sixth opening 27: Sub-filter unit 271: Sub-straight pipe part 272: Sub-conical pipe part 273: Sub-opening 274: Sub-down pipe 30: First Nozzle 40: Second Nozzle A, A1: Gas C: Axis H: Horizontal Surface H ₁₁ , H ₁₂ , H ₁₃ , H ₃₀ , H ₄₀ , H ₂₁₂ , H ₂₁₃ , H ₂₁₄ , H ₂₂₂ , H ₂₃₂ , H ₂₃₃ , H ₂₃₄ , H ₂₄₂ , H ₂₅₂ , H ₂₆₂ , H ₂₆₃ , H ₂₇₃ , H ₂₇₄ : Level M1: First water mist M2: Second water mist

圖1為本發明之一實施例之組合結構示意圖。圖2A至2B為圖1實施例之進氣氣體與水霧流動方向之示意圖。圖2B為圖1實施例之旋風式過濾裝置之進氣氣體與水霧流動方向之示意圖。圖2C為圖2B之B-B剖面結構示意圖。圖3為本發明之文氏管過濾裝置另一實施例之進氣氣體與水霧流動方向之示意圖。圖4至圖7為圖1實施例之旋風式過濾裝置之過濾單元之不同實施例之結構示意圖。圖8至圖10為本發明之旋風式過濾裝置之不同實施例之結構示意圖。圖10A為圖10之C-C剖面結構示意圖。FIG. 1 is a schematic diagram of a combined structure of an embodiment of the present invention. 2A to 2B are schematic diagrams illustrating the flow directions of the intake gas and the water mist in the embodiment of FIG. 1 . FIG. 2B is a schematic diagram of the flow direction of the intake gas and the water mist of the cyclone filter device of the embodiment of FIG. 1 . FIG. 2C is a schematic diagram of the cross-sectional structure of FIG. 2B along B-B. 3 is a schematic diagram of the flow direction of the intake gas and the water mist in another embodiment of the venturi filter device of the present invention. 4 to 7 are schematic structural diagrams of different embodiments of the filter unit of the cyclone filter device of the embodiment of FIG. 1 . 8 to 10 are schematic structural diagrams of different embodiments of the cyclone filter device of the present invention. FIG. 10A is a schematic diagram of the cross-sectional structure of FIG. 10 taken along C-C.

100:微粒捕集系統100: Particulate capture system

10:文氏管過濾裝置10: Venturi filter device

11:進氣部11: Intake part

111:進氣口111: Air intake

12:喉部12: Throat

121:多孔性材料121: Porous Materials

13:出氣部13: Air outlet

14:調整元件14: Adjustment components

15:調整齒輪組15: Adjust the gear set

16:收集桶16: Collection Buckets

20:旋風式過濾裝置20: Cyclone filter device

30:第一噴嘴30: First Nozzle

40:第二噴嘴40: Second nozzle

C:軸心C: axis

H:水平面H: horizontal plane

Claims

一種微粒捕集系統，其包含：一文氏管過濾裝置，其具有一進氣部、一喉部與一出氣部，該出氣部的水平高度高於該進氣部的水平高度，該喉部位於該進氣部與該出氣部之間，該喉部的內徑小於該進氣部與該出氣部的內徑；一旋風式過濾裝置，與該文氏管過濾裝置同軸心設置於該出氣部，該旋風式過濾裝置由複數過濾單元構成，各該過濾單元包含一直型管部，該直型管部之底部具有一錐型管部，該直型管部的軸心垂直於水平面，該錐型管部管徑較小的一端朝向該喉部，該複數過濾單元之該直型管部的具有至少兩種尺寸，該複數過濾單元層層套設，位於最外層之該過濾單元具有一入口，該入口的水平高度高於相鄰內層該過濾單元之底部的水平高度，位於最內層之該過濾單元的該直型管部的頂部為一出口，該出口的水平高度高於該入口的水平高度；複數第一噴嘴，設置於該文氏管過濾裝置內，該複數第一噴嘴的水平高度高於該喉部的水平高度，各該第一噴嘴提供第一水霧，各該第一水霧的噴灑方向大致平行於該文氏管過濾裝置的軸心方向由該第一噴嘴朝向該喉部噴灑；以及氣體由該進氣部之進氣口進入該文氏管過濾裝置，依序通過該喉部、該複數第一噴嘴，由該入口進入該旋風式過濾裝置，由該出口流出該旋風式過濾裝置，藉此捕集該氣體中之粉塵、微粒、微細粉塵。A particulate capture system comprising: A venturi filter device has an air inlet, a throat and an air outlet, the level of the air outlet is higher than that of the air inlet, and the throat is located between the air inlet and the air outlet During the time, the inner diameter of the throat portion is smaller than the inner diameter of the air inlet portion and the air outlet portion; A cyclone filter device is disposed on the air outlet coaxially with the venturi filter device, the cyclone filter device is composed of a plurality of filter units, each filter unit includes a straight pipe portion, and the bottom of the straight pipe portion has a a tapered tube portion, the axis of the straight tube portion is perpendicular to the horizontal plane, the end of the tapered tube portion with the smaller diameter faces the throat portion, and the straight tube portion of the plurality of filter units has at least two sizes , the plurality of filter units are set in layers, the filter unit located in the outermost layer has an entrance, the level of the entrance is higher than the level of the bottom of the filter unit in the adjacent inner layer, and the filter unit located in the innermost layer has an entrance. The top of the straight pipe portion is an outlet, and the level of the outlet is higher than the level of the inlet; A plurality of first nozzles are arranged in the venturi filter device, the horizontal height of the plurality of first nozzles is higher than the horizontal height of the throat, each of the first nozzles provides a first water mist, and the The spraying direction is substantially parallel to the axial direction of the venturi filter device and sprayed from the first nozzle toward the throat; and The gas enters the venturi filter device from the air inlet of the air inlet, passes through the throat and the plurality of first nozzles in sequence, enters the cyclone filter device from the inlet, and flows out of the cyclone filter device from the outlet , so as to capture the dust, particles and fine dust in the gas.

如請求項1之微粒捕集系統，其中該文氏管過濾裝置更包括一調整元件，該調整元件具有一錐部，該錐部具有直徑較小的一尖錐部朝向該喉部，該調整元件可升降地設置於該進氣部，以調整該氣體由該進氣部通過該喉部時之流速。The particle trapping system of claim 1, wherein the venturi filter device further comprises an adjusting element, the adjusting element has a tapered portion, and the tapered portion has a pointed tapered portion with a smaller diameter toward the throat portion, the adjusting element The element is arranged in the air inlet part so as to be able to rise and fall, so as to adjust the flow rate of the gas when the air passes through the throat part from the air inlet part.

如請求項2之微粒捕集系統，其中該調整元件連接於一調整齒輪組，該調整齒輪組包括：一第一齒輪組件，包括一第一齒輪與一第一桿體，該第一桿體之兩端分別連接於該調整元件與該第一齒輪，該第一桿體之軸心方向垂直於水平面；以及一第二齒輪組件，包括一第二齒輪與一第二桿體，該第二桿體之一端連接於該第二齒輪，該第二桿體之另一端凸伸於該文氏管過濾裝置外，該第二齒輪與該第一齒輪相嚙合，藉由驅動該第二桿體，同步帶動該第二齒輪驅動該第一齒輪旋轉，進而驅動該第一桿體帶動該調整元件升降。The particle trap system of claim 2, wherein the adjustment element is connected to an adjustment gear set, the adjustment gear set comprising: A first gear assembly includes a first gear and a first rod body, two ends of the first rod body are respectively connected to the adjusting element and the first gear, and the axis direction of the first rod body is perpendicular to the horizontal plane ;as well as a second gear assembly, comprising a second gear and a second rod, one end of the second rod is connected to the second gear, and the other end of the second rod protrudes out of the venturi filter device , the second gear is meshed with the first gear, and by driving the second rod, the second gear is synchronously driven to drive the first gear to rotate, and then the first rod is driven to drive the adjustment element to rise and fall.

如請求項1之微粒捕集系統，其中該進氣口的下方設有一收集桶，用以收集落下之該第一水霧及該第二水霧。The particle collection system of claim 1, wherein a collection bucket is arranged below the air inlet for collecting the falling first water mist and the second water mist.

如請求項4之微粒捕集系統，其中該進氣口位於該進氣部之側邊，且位於該收集桶之上方，該氣體以平行該水平面之方向進入該進氣部。The particulate capture system of claim 4, wherein the air inlet is located at the side of the air inlet portion and above the collection barrel, and the gas enters the air inlet portion in a direction parallel to the horizontal plane.

如請求項1之微粒捕集系統，其中該進氣口位於該進氣部之底部，該進氣口連接一管體且該管體的頂端凸伸於該收集桶之上方，該氣體以垂直該水平面之方向進入該進氣部。The particle collection system of claim 1, wherein the air inlet is located at the bottom of the air inlet portion, the air inlet is connected to a pipe body, and the top of the pipe body protrudes above the collection barrel, and the gas is vertically The direction of the horizontal plane enters the air inlet.

如請求項6之微粒捕集系統，其中該管體的上方設有一蓋體，該蓋體與該管體之該頂端具有一距離，該氣體由該管體之該頂端流出後，再由該蓋體之四周流入該進氣部。The particle trapping system of claim 6, wherein a cover body is arranged above the tube body, the cover body is at a distance from the top end of the tube body, and the gas flows out from the top end of the tube body, and then flows out of the tube body. The periphery of the cover body flows into the air inlet portion.

如請求項1之微粒捕集系統，其中該文氏管過濾裝置之該喉部設有一多孔性材料。The particulate capture system of claim 1, wherein the throat of the venturi filter device is provided with a porous material.

如請求項1之微粒捕集系統，其中該旋風式過濾裝置包括：一第一過濾單元，其具有一第一直型管部及一第一錐型管部，於該第一直型管部設有一第一開口作為該入口；一第二過濾單元，其具有一第二直型管部及一第二錐型管部，該第二直型管部的外徑小於該第一直型管部的內徑，該第二過濾單元同軸心設置於該第一過濾單元內，該第二錐型管部的底部的水平高度低於該第一開口的水平高度；一第三過濾單元，其具有一第三直型管部及一第三錐型管部，該第三直型管部的外徑小於該第二直型管部的內徑，該第三過濾單元同軸心設置於該第二過濾單元內，該第三錐型管部的底部的水平高度低於該第二錐型管部的底部的水平高度，於該第三直型管部設有一第三開口，該第三開口的水平高度高於該第二錐型管部的底部的水平高度；以及一第四過濾單元，其具有一第四直型管部及一第四錐型管部，該第四直型管部的外徑小於該第三直型管部的內徑，該第四過濾單元同軸心設置於該第三過濾單元內，該第四錐型管部的底部的水平高度低於該第三開口的水平高度且高於該第三錐型管部的底部的水平高度，該第四直型管部的頂部為該出口。The particulate capture system of claim 1, wherein the cyclone filter device comprises: a first filter unit, which has a first straight pipe portion and a first tapered pipe portion, and a first opening is provided in the first straight pipe portion as the inlet; a second filter unit, which has a second straight pipe part and a second conical pipe part, the outer diameter of the second straight pipe part is smaller than the inner diameter of the first straight pipe part, the second filter The unit is coaxially arranged in the first filter unit, and the level of the bottom of the second conical tube portion is lower than the level of the first opening; a third filter unit, which has a third straight pipe part and a third conical pipe part, the outer diameter of the third straight pipe part is smaller than the inner diameter of the second straight pipe part, the third filter The unit is coaxially arranged in the second filter unit, the horizontal height of the bottom of the third conical tube part is lower than the horizontal height of the bottom of the second conical tube part, and the third straight tube part is provided with a first three openings, the level of the third opening is higher than the level of the bottom of the second tapered tube portion; and a fourth filter unit, which has a fourth straight pipe part and a fourth conical pipe part, the outer diameter of the fourth straight pipe part is smaller than the inner diameter of the third straight pipe part, the fourth filter The unit is coaxially arranged in the third filter unit, the level of the bottom of the fourth conical pipe part is lower than the level of the third opening and higher than the level of the bottom of the third conical pipe part, the The top of the fourth straight pipe portion is the outlet.

如請求項9之微粒捕集系統，其中該第一過濾單元的該第一錐型管部的底部設有一第一料斗。The particle trapping system of claim 9, wherein a first hopper is provided at the bottom of the first conical tube portion of the first filter unit.

如請求項9之微粒捕集系統，其中該第一過濾單元的該第一錐型管部的底部設有一第一下降管，該第一下降管之軸向長度之底部之水平高度低於各該第一噴嘴之水平高度。The particle trapping system of claim 9, wherein the bottom of the first tapered pipe portion of the first filter unit is provided with a first down pipe, and the horizontal height of the bottom of the axial length of the first down pipe is lower than each The level of the first nozzle.

如請求項11之微粒捕集系統，其中該第一下降管之該底部具有一第一錐部，該第一錐部具有管徑較小的一開口朝向該喉部。The particle trapping system of claim 11, wherein the bottom of the first downcomer has a first tapered portion, and the first tapered portion has an opening with a smaller diameter toward the throat portion.

如請求項11之微粒捕集系統，其中該第一下降管之該底部設有一第一料斗。The particle trapping system of claim 11, wherein the bottom of the first downcomer is provided with a first hopper.

如請求項9之微粒捕集系統，其中該第三過濾單元的該第三錐型管部的底部設有一第三料斗。The particle trapping system of claim 9, wherein a third hopper is provided at the bottom of the third conical tube portion of the third filter unit.

如請求項9之微粒捕集系統，其中該第三過濾單元的該第三錐型管部的底部設有一第三下降管，該第三下降管之軸向長度之底部之水平高度高於該第一錐型管部的底部的水平高度。The particle trapping system of claim 9, wherein the bottom of the third conical pipe portion of the third filter unit is provided with a third descending pipe, and the horizontal height of the bottom of the axial length of the third descending pipe is higher than that of the third descending pipe. The level of the bottom of the first tapered tube portion.

如請求項15之微粒捕集系統，其中該第三下降管之該底部具有一第三錐部，該第三錐部具有管徑較小的一開口朝向該喉部。The particle trapping system of claim 15, wherein the bottom of the third downcomer has a third tapered portion, and the third tapered portion has an opening with a smaller diameter toward the throat portion.

如請求項15之微粒捕集系統，其中該第三下降管之該底部設有一第三料斗。The particle trapping system of claim 15, wherein the bottom of the third downcomer is provided with a third hopper.

如請求項9之微粒捕集系統，其中該第三過濾單元與該第四過濾單元之間更包括：一第五過濾單元，其具有一第五直型管部及一第五錐型管部，該第五直型管部的外徑小於該第三直型管部的內徑，該第五過濾單元同軸心設置於該第三過濾單元內，該第五錐型管部的底部的水平高度低於該第三開口的水平高度且高於該第三錐型管部的底部的水平高度；以及一第六過濾單元，其具有一第六直型管部及一第六錐型管部，該第六直型管部的外徑小於該第五直型管部的內徑，該第六過濾單元同軸心設置於該第五過濾單元內，該第六錐型管部的底部的水平高度低於該第五錐型管部的底部的水平高度，於該第六直型管部設有一第六開口，該第六開口的水平高度高於該第五錐型管部的底部的水平高度；該第四過濾單元同軸心設置於該第六過濾單元內，該第四直型管部的底部的水平高度低於該第六開口的水平高度且高於該第六錐型管部的底部的水平高度，該第四直型管部的頂部為該出口。The particulate capture system of claim 9, wherein the third filter unit and the fourth filter unit further include: a fifth filter unit, which has a fifth straight pipe part and a fifth conical pipe part, the outer diameter of the fifth straight pipe part is smaller than the inner diameter of the third straight pipe part, the fifth filter The unit is coaxially arranged in the third filter unit, and the level of the bottom of the fifth conical tubular portion is lower than the level of the third opening and higher than the level of the bottom of the third conical tubular portion; and a sixth filter unit, which has a sixth straight pipe part and a sixth conical pipe part, the outer diameter of the sixth straight pipe part is smaller than the inner diameter of the fifth straight pipe part, the sixth filter The unit is coaxially arranged in the fifth filter unit, the horizontal height of the bottom of the sixth conical tube part is lower than the horizontal height of the bottom of the fifth conical tube part, and the sixth straight tube part is provided with a first Six openings, and the level of the sixth opening is higher than the level of the bottom of the fifth conical tubular portion; The fourth filter unit is coaxially disposed in the sixth filter unit, and the level of the bottom of the fourth straight pipe portion is lower than the level of the sixth opening and higher than the bottom of the sixth conical pipe portion. Horizontal height, the top of the fourth straight pipe is the outlet.

如請求項1之微粒捕集系統，其中位於最內層之該過濾單元內設有複數個子過濾單元，各該子過濾單元具有一子直型管部與一子錐型管部及一子下降管，該子直型管部的外徑小於位於最內層之該過濾單元的內徑，該子錐型管部連接下方之子下降管的底部的水平高度與位於最內層之該過濾單元的該錐型管部的底部的水平高度大致相同，或低於其水平高度，於各該子直型管部設有一子開口，該子開口的水平高度高於位於最內層之該過濾單元的該錐型管部的底部，各該子過濾單元的頂部相連通並與位於最內層之該過濾單元的該直型管部相連通。The particulate capture system of claim 1, wherein the filter unit located at the innermost layer is provided with a plurality of sub-filter units, and each of the sub-filter units has a sub-straight pipe portion, a sub-conical pipe portion, and a sub-drop Pipe, the outer diameter of the sub-straight pipe portion is smaller than the inner diameter of the filter unit located in the innermost layer, and the sub-conical pipe portion connects the level of the bottom of the sub-downpipe below and the filter unit located in the innermost layer. The level of the bottom of the tapered pipe portion is approximately the same or lower than the level. Each of the straight pipe portions is provided with a sub-opening, and the level of the sub-opening is higher than that of the filter unit located in the innermost layer. The bottom of the tapered tube portion and the top of each sub-filter unit communicate with the straight tube portion of the filter unit located at the innermost layer.

如請求項1之微粒捕集系統，其中各該第一噴嘴之水平高度相同且等距環繞該文氏管過濾裝置的軸心設置。The particle trapping system of claim 1, wherein each of the first nozzles has the same horizontal height and is equidistantly arranged around the axis of the venturi filter device.

如請求項1之微粒捕集系統，其中該文氏管過濾裝置內靠近該出氣部且環繞該旋風式過濾裝置外圍設置有複數第二噴嘴，該複數第二噴嘴的水平高度高於該複數第一噴嘴的水平高度，各該第二噴嘴提供第二水霧，各該第二水霧的噴灑方向大致平行於該水平面或垂直於該水平面且朝下方，由該第二噴嘴朝向該旋風式過濾裝置內噴灑；該氣體由該進氣部之進氣口進入該文氏管過濾裝置，依序通過該喉部、該複數第一噴嘴，由該入口進入該旋風式過濾裝置、通過該複數第二噴嘴，由該出口流出該旋風式過濾裝置，藉此捕集該氣體中之粉塵、微粒、微細粉塵。The particulate capture system of claim 1, wherein a plurality of second nozzles are arranged in the venturi filter device near the air outlet and around the periphery of the cyclone filter device, and the level of the plurality of second nozzles is higher than the plurality of first nozzles The level of a nozzle, each of the second nozzles provides a second water mist, the spraying direction of each of the second water mists is substantially parallel to the horizontal plane or perpendicular to the horizontal plane and downward, and the second nozzle is directed toward the cyclone filter The gas is sprayed in the device; the gas enters the venturi filter device from the air inlet of the air inlet, passes through the throat, the plurality of first nozzles in sequence, enters the cyclone filter device from the inlet, and passes through the plurality of first nozzles. Two nozzles flow out of the cyclone filter device from the outlet, thereby capturing dust, particles and fine dust in the gas.

如請求項21之微粒捕集系統，其中各該第二噴嘴之水平高度相同且等距環繞該旋風式過濾裝置的軸心設置。The particle collection system of claim 21, wherein each of the second nozzles has the same horizontal height and is equidistantly arranged around the axis of the cyclone filter device.