TWM630138U - Gravity mixed flow device for waste gas scrubber - Google Patents

Gravity mixed flow device for waste gas scrubber Download PDF

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TWM630138U
TWM630138U TW111201138U TW111201138U TWM630138U TW M630138 U TWM630138 U TW M630138U TW 111201138 U TW111201138 U TW 111201138U TW 111201138 U TW111201138 U TW 111201138U TW M630138 U TWM630138 U TW M630138U
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Taiwan
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exhaust gas
water
pipe
aeration
gravity
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TW111201138U
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Chinese (zh)
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林豪傑
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千附實業股份有限公司
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Abstract

The utility model relates to a gravity-type mixed flow device for an exhaust gas washing tower. A water pan is arranged in the water tank of the exhaust gas washing tower to receive the waste water after circulating cleaning of the exhaust gas washing tower. The bottom of the water pan is connected to a drain pipe in the water tank. The drain pipe There are many radial aeration pipes in layers from top to bottom around the perimeter; thus, when the amount of cleaned wastewater received by the water pan exceeds a certain pressure, the cleaned wastewater can enter the drain pipe, and the drain pipe The surrounding aeration pipes are sprayed out at different heights, different speeds and in various directions, so as to achieve sufficient disturbance of the wastewater after cleaning in the sink.

Description

廢氣洗滌塔之重力式混流裝置 Gravity mixed flow device for waste gas scrubber

本新型係有關一種無需動力的重力式混流裝置,特別是指設於廢氣洗滌塔的底部,可使廢氣洗滌塔循環清洗後的廢水,經由不同速度及多種方向噴射流擾動,以避免汙泥沉積、提昇清洗後廢水之再利用率之廢氣洗滌塔之重力式混流裝置。 The new type relates to a gravity-type mixed flow device without power, especially, it is set at the bottom of the waste gas washing tower, which can make the waste water after the waste gas washing tower circulate and wash to be disturbed by jet flow at different speeds and in various directions, so as to avoid sludge deposition . Gravity type mixed flow device of waste gas washing tower to improve the reuse rate of waste water after cleaning.

一般工業製程產生的廢氣,通常包含有毒物質且具有臭味,如果廢氣未經過妥善處理而排放至空氣中,就會造成空氣污染,危害人們的生命安全。為了降低廢氣造成空氣的污染,使廢氣中的有毒物質濃度低於法規規定的限值,業界所常用的設備即為濕式洗滌塔。 The waste gas produced by general industrial processes usually contains toxic substances and has a odor. If the waste gas is discharged into the air without proper treatment, it will cause air pollution and endanger people's lives. In order to reduce the air pollution caused by the exhaust gas and make the concentration of toxic substances in the exhaust gas lower than the limit specified by the regulations, the equipment commonly used in the industry is the wet scrubber.

習見使用之濕式洗滌塔,其作用原理為藉由洗滌層與廢氣的接觸以去除廢氣中的酸鹼氣體等物質,洗滌層與廢氣的接觸時間及面積為整體去除效率之重要指標。然而在一定的成本及建置面積中無法無限制的擴張洗滌層,且初始廢氣進入塔身後將以一定流向直接穿越洗滌 層,無法全面地與洗滌層內的拉西環(Raschig rings)接觸,影響廢氣處理去除有害物質的效率。此外,若廢氣通過洗滌層的流速過快,會使廢氣與洗滌層內的拉西環的接觸時間過短,而降低洗滌效率。 Commonly used wet scrubbers, the principle of which is to remove substances such as acid and alkali gases in the exhaust gas through the contact between the scrubbing layer and the exhaust gas. The contact time and area of the scrubbing layer and the exhaust gas are important indicators of the overall removal efficiency. However, in a certain cost and construction area, the washing layer cannot be expanded without limit, and the initial exhaust gas will directly pass through the washing in a certain flow direction after entering the tower. The layer cannot be fully contacted with the Raschig rings in the scrubbing layer, which affects the efficiency of exhaust gas treatment to remove harmful substances. In addition, if the flow rate of the exhaust gas through the washing layer is too fast, the contact time between the exhaust gas and the Raschig ring in the washing layer will be too short, thereby reducing the washing efficiency.

為了改善習見濕式洗滌塔的缺失,創作人早年提出了第M514880U號「廢氣洗滌塔」新型專利案,如第1圖所示,該廢氣洗滌塔包括主體110、洗滌層120、灑水裝置130及遮擋結構140。主體110具有進氣口110a、排氣口110b及氣體通道110c,氣體通道110c連通進氣口110a及排氣口110b。洗滌層120配置於氣體通道110c內且位於排氣口110b下方,洗滌層120包括多個吸水構件122。灑水裝置130配置於洗滌層120上方。遮擋結構140固定於洗滌層120下方且位於進氣口110a上方,遮擋結構140遮擋部分的氣體通道110c。設置在洗滌層120上方的灑水系統130灑水至洗滌層120,使得洗滌層120的吸水構件122得以吸附水分。在廢氣經由進氣口110a進入主體110之氣體通道110c,並通過洗滌層120時,廢氣與含水的吸水構件122接觸,廢氣中的雜質乃可被吸水構件122吸收,淨化後的氣體再繼續往排氣口110b移動,透過排氣口110b排出。此外,主體110內部的底部設有一水槽150,並且設有幫浦(圖未示)以將水槽150內的水抽引至灑水裝置130,以對廢氣進行循環清洗。 In order to improve the lack of conventional wet scrubbers, the creator proposed a new patent case of "exhaust gas scrubber" No. M514880U in the early years. As shown in Figure 1, the exhaust gas scrubber includes a main body 110, a scrubbing layer 120, and a sprinkler 130. and the shielding structure 140 . The main body 110 has an intake port 110a, an exhaust port 110b, and a gas passage 110c, and the gas passage 110c communicates with the intake port 110a and the exhaust port 110b. The cleaning layer 120 is disposed in the gas channel 110c and below the exhaust port 110b , and the cleaning layer 120 includes a plurality of water absorbing members 122 . The sprinkler 130 is disposed above the washing layer 120 . The shielding structure 140 is fixed under the washing layer 120 and above the air inlet 110a, and the shielding structure 140 shields a part of the gas channel 110c. The sprinkler system 130 disposed above the washing layer 120 sprinkles water to the washing layer 120, so that the water absorbing member 122 of the washing layer 120 can absorb moisture. When the exhaust gas enters the gas channel 110c of the main body 110 through the air inlet 110a and passes through the washing layer 120, the exhaust gas contacts the water-absorbing member 122 containing water, and the impurities in the exhaust gas can be absorbed by the water-absorbing member 122, and the purified gas continues to flow to the water-absorbing member 122. The exhaust port 110b moves and is discharged through the exhaust port 110b. In addition, a water tank 150 is provided at the bottom of the main body 110, and a pump (not shown) is provided to draw the water in the water tank 150 to the sprinkler 130 to circulate and clean the exhaust gas.

惟,根據創作人的研究發現,習見廢氣洗滌塔 內經過循環清洗後的廢水會含有大量粉塵,當廢水中的粉塵因為濃度太高而沉積時,將容易導致噴嘴堵塞、影響廢氣水洗效果,因此清洗後廢水多直接定時全部廢棄排出。然而,隨著科技的快速發展與環保意識的高漲,清洗後廢水若直接廢棄排出,不僅清洗的成本高,而且容易產生工業危害,造成環境污染,有鑒於此,創作人乃孜孜不倦地進行研究與改進,經多次測試與改良後,終於有本新型之廢氣洗滌塔之重力式混流裝置產生。 However, according to the creator's research findings, the conventional exhaust gas scrubber The waste water after circulating cleaning will contain a lot of dust. When the dust in the waste water is deposited due to the high concentration, it will easily cause the nozzle to block and affect the washing effect of the waste gas. Therefore, the waste water after cleaning is mostly discarded and discharged at regular intervals. However, with the rapid development of science and technology and the rising awareness of environmental protection, if the waste water after cleaning is directly discarded and discharged, it will not only cost a lot of cleaning, but also easily cause industrial hazards and cause environmental pollution. Improvement, after many tests and improvements, finally the new gravity type mixed flow device of the waste gas washing tower is produced.

因此,本新型旨在提供一種廢氣洗滌塔之重力式混流裝置,係使廢氣洗滌塔之循環清洗後廢水中的粉塵濃度搭配定時、定量排出而降低,以保持循環清洗水一定的潔淨度而持續再利用者。 Therefore, the purpose of the present invention is to provide a gravity-type mixed-flow device for the waste gas washing tower, which reduces the dust concentration in the waste water after the cyclic cleaning of the waste gas washing tower with the regular and quantitative discharge, so as to maintain a certain cleanliness of the circulating cleaning water and continue. reuser.

依本新型之廢氣洗滌塔之重力式混流裝置,係於廢氣洗滌塔底部水槽的液面上設有一可用於承接循環清洗後廢水的水盤,水盤的底部與一洩流管連接,洩流管頂部有一洩壓閥,洩流管的周邊設有多數曝氣管,使清洗後廢水進入洩流管後,再經由多數曝氣管向外噴流出去,此為本新型之次一目的。 According to the new gravity type mixed flow device of the waste gas washing tower, there is a water pan on the liquid surface of the water tank at the bottom of the waste gas washing tower, which can be used to receive the waste water after circulating cleaning. The bottom of the water pan is connected with a drain pipe, and the top of the drain pipe is connected There is a pressure relief valve, and there are many aeration pipes around the discharge pipe, so that after cleaning the waste water enters the discharge pipe, and then sprays out through most of the aeration pipes. This is the second purpose of the new model.

依本新型之廢氣洗滌塔之重力式混流裝置,所述多數曝氣管係分佈於洩流管的周邊,由上而下分層設置,並且為放射狀設置,藉此提供清洗後廢水可從不同層 的曝氣管噴出,以提昇水中之擾動、避免汙泥沉降,為本新型之再一目的。 According to the gravity-type mixed flow device of the waste gas washing tower of the present invention, the aeration pipes are distributed around the discharge pipe, and are arranged in layers from top to bottom, and are arranged radially, so as to provide the waste water after cleaning from different layers The aeration pipe is sprayed out to improve the disturbance in the water and avoid sludge sedimentation, which is another purpose of this new model.

依本新型之廢氣洗滌塔之重力式混流裝置,藉由清洗後廢水可被充份擾動,廢水內的粉塵可被充份打散,避免集結而導致粉塵濃度過高且搭配定時、定量換水機制,使水槽內之循環水保持一定的潔淨度,而得藉幫浦抽到洗滌塔上端重新再利用,為本新型之又一目的。 According to the new gravity type mixed flow device of the waste gas washing tower, the waste water can be fully disturbed after cleaning, and the dust in the waste water can be fully dispersed, so as to avoid the accumulation of dust and cause the dust concentration to be too high, and with the timing and quantitative water exchange mechanism , so that the circulating water in the water tank can maintain a certain degree of cleanliness, and it must be pumped to the upper end of the washing tower for reuse by the pump, which is another purpose of this new model.

至於本新型之廢氣洗滌塔之重力式混流裝置,其詳細結構、具體實施例,則參照下列依附圖所作之說明,即可得到完全的了解。 As for the gravity-type mixed-flow device of the new type of waste gas washing tower, its detailed structure and specific embodiments can be fully understood by referring to the following description according to the accompanying drawings.

110:主體 110: Subject

110a:進氣口 110a: Air intake

110b:排氣口 110b: exhaust port

110c:氣體通道 110c: Gas channel

120:洗滌層 120: washing layer

122:吸水構件 122: Absorbent components

130:灑水裝置 130: Sprinklers

140:遮擋結構 140: Blocking Structure

150:水槽 150: Sink

200:廢氣洗滌塔 200: Exhaust gas scrubber

210:主體 210: Subject

220:遮擋結構 220: Occlusion Structure

230:洗滌層 230: Washing Layer

240:灑水裝置 240: Sprinklers

250:進氣口 250: Air intake

260:排氣口 260: exhaust port

300:重力式混流裝置 300: Gravity mixed flow device

400:拉西環層隔框 400: Raschig ring layer bulkhead

41:水槽 41: Sink

42:洩流管 42: Drain pipe

43:固定盤 43: Fixed plate

44:水盤 44: Water Tray

441:漏斗狀底面 441: Funnel-shaped bottom

45:洩壓閥 45: Pressure relief valve

500:曝氣管組 500: Aeration tube group

510:上層曝氣管 510: Upper aeration pipe

520:中層曝氣管 520: Middle layer aeration pipe

530:下層曝氣管 530: Lower aeration pipe

51a、51b、51c、51d;52a、52b、52c、52d;53a、53b、53c、53d:曝氣管單元 51a, 51b, 51c, 51d; 52a, 52b, 52c, 52d; 53a, 53b, 53c, 53d: Aeration tube unit

600:集水箱 600: Collecting tank

601:管路 601: Pipeline

D:水槽的直徑 D: Diameter of the sink

H:水槽的高度 H: height of the sink

L:水槽底部到拉西環層隔框的距離 L: The distance from the bottom of the sink to the Raschig ring shelf

P:水位線 P: water level line

W:水盤的直徑 W: the diameter of the water pan

第1圖為習見廢氣洗滌塔之截面示意圖。 Figure 1 is a schematic cross-sectional view of a conventional exhaust gas scrubber.

第2圖為本新型之廢氣洗滌塔的配置示意圖。 Figure 2 is a schematic diagram of the configuration of the new waste gas scrubber.

第3圖為本新型之重力式混流裝置的平面示意圖。 Figure 3 is a schematic plan view of the new gravity mixed flow device.

第4圖為本新型之曝氣管組的平面示意圖。 Figure 4 is a schematic plan view of the new type of aeration tube group.

第5圖為本新型之曝氣管組的上層曝氣管、中層曝氣管及下層曝氣管的平面示意圖。 Figure 5 is a schematic plan view of the upper aeration pipe, the middle aeration pipe and the lower aeration pipe of the new type of aeration pipe group.

第6圖為本新型之曝氣管組的俯視示意圖。 Figure 6 is a schematic top view of the new aeration tube group.

第7圖為本新型之第二實施例圖。 Figure 7 is a diagram of the second embodiment of the new model.

本新型之廢氣洗滌塔之重力式混流裝置,如第 2圖所示,該廢氣洗滌塔200係於主體210的內部,由下而上依序設有遮擋結構220、洗滌層230與灑水裝置240,主體210提供廢氣進入的進氣口250設於下端,主體210的排氣口260設於上端。主體210的底部則設置該重力式混流裝置300。 The gravity-type mixed flow device of the new waste gas scrubbing tower, such as the first As shown in Figure 2, the exhaust gas washing tower 200 is located inside the main body 210, and is provided with a shielding structure 220, a washing layer 230 and a sprinkler 240 in sequence from bottom to top. At the lower end, the exhaust port 260 of the main body 210 is provided at the upper end. The gravity-type mixing device 300 is disposed at the bottom of the main body 210 .

請參照第3圖所示,該重力式混流裝置300,係於水槽41的內部設有一洩流管42,該洩流管42的底部藉一固定盤43固定於水槽41的底面,使其呈直立狀,該洩流管42的周邊設有位於不同高度的曝氣管組500,洩流管42的上部為一水盤44,該水盤44藉由一位於進氣口250下方之拉西環層隔框400吊掛,該水盤44的內部為漏斗狀底面441,水盤44的底部與洩流管42之間設有一洩壓閥45。該洩壓閥45可在水盤44承接的水量超過一定壓力時打開,使水盤44內所承接的循環清洗後廢水進入洩流管42,再從曝氣管組500噴射而出。 Referring to FIG. 3, the gravity-type mixing device 300 is provided with a drain pipe 42 inside the water tank 41, and the bottom of the drain pipe 42 is fixed to the bottom surface of the water tank 41 by a fixing plate 43, so that it is Upright, aeration pipe groups 500 at different heights are arranged around the discharge pipe 42 , and the upper part of the discharge pipe 42 is a water pan 44 . The partition frame 400 is suspended. The inside of the water pan 44 is a funnel-shaped bottom surface 441 , and a pressure relief valve 45 is provided between the bottom of the water pan 44 and the drain pipe 42 . The pressure relief valve 45 can be opened when the amount of water received by the water pan 44 exceeds a certain pressure, so that the circulating and cleaned waste water received in the water pan 44 enters the drain pipe 42 and is then sprayed out from the aeration pipe group 500 .

如圖所示,所述水盤44的盤面係小於水槽41的內徑,因此當清洗後廢水從洗滌塔上方流下時,部份清洗後廢水會直接流入水槽41,部份清洗後廢水則會被水盤44承接,該水盤44係可漂浮於液面上,其底部約1/3沉浸於水槽41的水位線P之下,藉由浮力效應支撐其重量。當水盤44承接的清洗後廢水的水量未超過一定壓力時,藉由水面浮力保持於水位線P之上,洩壓閥45保持關閉。當其承接的清 洗後廢水的水量超過一定壓力時,則迫使洩壓閥45打開,以便水盤44所承接的循環清洗後廢水得以流入洩流管42。 As shown in the figure, the surface of the water pan 44 is smaller than the inner diameter of the water tank 41. Therefore, when the washed wastewater flows down from the top of the washing tower, some of the washed wastewater will flow directly into the water tank 41, and some of the washed wastewater will be The water pan 44 is received, the water pan 44 can float on the liquid surface, and about 1/3 of the bottom of the water pan 44 is immersed below the water level P of the water tank 41, and supports its weight by the buoyancy effect. When the water volume of the washed waste water received by the water pan 44 does not exceed a certain pressure, the pressure relief valve 45 is kept closed due to the buoyancy of the water surface being kept above the water level line P. when it undertakes When the water volume of the washed wastewater exceeds a certain pressure, the pressure relief valve 45 is forced to open, so that the circulating washed wastewater received by the water pan 44 can flow into the drain pipe 42 .

請同時參照第4、5圖所示,所述設於洩流管42外周邊的曝氣管組500,分別設有上層曝氣管510、中層曝氣管520及下層曝氣管530,每一層曝氣管510、520、530分別設有四支曝氣管單元51a、51b、51c、51d;52a、52b、52c、52d;53a、53b、53c、53d,各層曝氣管510、520、530的每支曝氣管單元51a、51b、51c、51d;52a、52b、52c、52d;53a、53b、53c、53d係相互間隔90度,上層曝氣管510與中層曝氣管520的曝氣管單元以30度錯開;中層曝氣管520與下層曝氣管530的曝氣管單元亦以30度錯開。而且,每層曝氣管510、520、530之曝氣管單元的管徑及長度均不同。例如,上層曝氣管510的曝氣管單元51a、51b、51c、51d,其管徑最大,但長度最短;中層曝氣管520的曝氣管單元52a、52b、52c、52d,其管徑適中,長度也適中;下層曝氣管530的曝氣管單元53a、53b、53c、53d,則管徑最小,但長度最長。藉此,提供洩流管42的各個角度均有曝氣管單元51a、51b、51c、51d;52a、52b、52c、52d;53a、53b、53c、53d(如第6圖所示),清洗後廢水進入洩流管42後即可從不同高度、不同角度及不同流速噴射而出,達到對水槽41內的清洗後廢水的充分擾動。 Please refer to Figures 4 and 5 at the same time, the aeration tube group 500 arranged on the outer periphery of the discharge pipe 42 is respectively provided with an upper layer aeration tube 510, a middle layer aeration tube 520 and a lower layer aeration tube 530. The aeration pipes 510, 520 and 530 on the first floor are respectively provided with four aeration pipe units 51a, 51b, 51c and 51d; 52a, 52b, 52c and 52d; 53a, 53b, 53c and 53d. Each aeration tube unit 51a, 51b, 51c, 51d of 530; 52a, 52b, 52c, 52d; 53a, 53b, 53c, and 53d are separated by 90 degrees from each other. The air pipe units are staggered by 30 degrees; the aeration pipe units of the middle layer aeration pipe 520 and the lower layer aeration pipe 530 are also staggered by 30 degrees. Moreover, the pipe diameter and length of the aeration pipe units of each layer of the aeration pipes 510, 520, and 530 are different. For example, the aeration pipe units 51a, 51b, 51c, and 51d of the upper aeration pipe 510 have the largest pipe diameter but the shortest length; Moderate, the length is also moderate; the aeration pipe units 53a, 53b, 53c, 53d of the lower aeration pipe 530 have the smallest pipe diameter but the longest length. Thereby, aeration pipe units 51a, 51b, 51c, 51d; 52a, 52b, 52c, 52d; 53a, 53b, 53c, 53d (as shown in FIG. 6) are provided at each angle of the drain pipe 42, and the cleaning After the waste water enters the drain pipe 42 , it can be sprayed out from different heights, different angles and different flow rates, so as to achieve sufficient disturbance to the washed waste water in the water tank 41 .

本新型之廢氣洗滌塔之重力式混流裝置,實施 時可如第3圖所示,使水槽41的高度H為水槽41底部到拉西環層隔框400距離高度L的二分之一;水盤44的直徑可為水槽41直徑D的二分之一。曝氣管組500之上層曝氣管510的曝氣管單元51a、51b、51c、51d,管徑為一又二分之1英吋,管長度為為水槽41直徑D的1/5;中層曝氣管520的曝氣管單元52a、52b、52c、52d,管徑為1英吋,管長度為為水槽41直徑D的1/4;下層曝氣管530的曝氣管單元53a、53b、53c、53d,管徑為0.5英吋,管長度為為水槽41直徑D的1/3;洩壓閥45的洩壓壓力可設定為大於5kg/cm2The gravity type mixed flow device of the new type of waste gas washing tower can be implemented as shown in Figure 3, so that the height H of the water tank 41 is half of the height L of the distance between the bottom of the water tank 41 and the Raschig ring layer partition frame 400; The diameter of 44 can be one-half of the diameter D of the water tank 41 . The aeration pipe units 51a, 51b, 51c, and 51d of the aeration pipe 510 on the upper layer of the aeration pipe group 500 have a pipe diameter of one and a half inches, and a pipe length of 1/5 of the diameter D of the water tank 41; The aeration pipe units 52a, 52b, 52c, and 52d of the air pipe 520 have a pipe diameter of 1 inch and a pipe length of 1/4 of the diameter D of the water tank 41; the aeration pipe units 53a, 53b, 53c, 53d, the pipe diameter is 0.5 inch, and the pipe length is 1/3 of the diameter D of the water tank 41; the relief pressure of the relief valve 45 can be set to be greater than 5kg/cm 2 .

本新型之廢氣洗滌塔之重力式混流裝置,實施時又可如第7圖所示,在廢氣洗滌塔200的外部設置一集水箱600,該集水箱600連通一管路601至水槽41的最上端,以汲取水槽41上方水位之溢流水,由於當水槽41內部受到曝氣管組500充分擾動後,水位下方的水中粉塵濃度可保持在標準值以下,可供抽取至洗滌塔上端再循環利用;水中經過擾動的粉塵則會上浮至水面,並隨著溢流水經管路601流至集水箱600收集排出。 As shown in FIG. 7 , the new gravity type mixed flow device of the waste gas washing tower can be implemented by setting a water collecting tank 600 outside the waste gas washing tower 200 . The upper end is used to draw the overflow water from the water level above the water tank 41. After the inside of the water tank 41 is fully disturbed by the aeration tube group 500, the dust concentration in the water below the water level can be kept below the standard value, which can be extracted to the upper end of the washing tower for recycling. ; The disturbed dust in the water will float to the water surface, and flow to the collecting tank 600 with the overflow water through the pipeline 601 for collection and discharge.

本新型之廢氣洗滌塔之重力式混流裝置,可以在不需額外動力下,直接利用落入水盤44的循環清洗後廢水的水量,對水槽41內的循環清洗後廢水充份擾流,使循環清洗後廢水中的粉塵含量被充份打散,進而使水中粉塵 濃度保持在標準值以下,以便循環回收再利用,進而降低成本以及提昇循環清洗的效率。 The new gravity type mixed flow device of the waste gas washing tower can directly use the water volume of the circulating cleaning wastewater falling into the water pan 44 without additional power to fully disturb the circulating cleaning wastewater in the water tank 41, so as to make the circulation After cleaning, the dust content in the wastewater is fully dispersed, and the dust in the water is further dispersed. The concentration is kept below the standard value for recycling and reuse, thereby reducing costs and improving the efficiency of circular cleaning.

綜上所述,本新型之廢氣洗滌塔之重力式混流裝置,其既未見於任何刊物,且市面上亦未見有任何類似的產品,是以,其具有新穎性應無疑慮。另外,本新型所具有之獨特特徵以及功能遠非習用所可比擬,所以其確實比習用更具有其進步性,而符合我國專利法有關新型專利之申請要件之規定,乃依法提起專利申請。 To sum up, the new gravity type mixed flow device for waste gas scrubbing tower has not been seen in any publications, and there is no similar product in the market, so there should be no doubts about its novelty. In addition, the unique features and functions of the new model are far from comparable to those of the conventional ones, so it is indeed more progressive than the conventional ones.

惟以上所述者,僅為本新型之較佳實施例而已,當不能以此限定本新型實施之範圍,即大凡依本新型申請專利範圍及說明書內容所作之簡單等效變化與修飾,皆應仍屬本新型專利涵蓋之範圍。 However, the above-mentioned are only the preferred embodiments of the present invention, which should not limit the scope of the present invention. It still falls within the scope of this new patent.

250:進氣口 250: Air intake

300:重力式混流裝置 300: Gravity mixed flow device

400:拉西環層隔框 400: Raschig ring layer bulkhead

41:水槽 41: Sink

42:洩流管 42: Drain pipe

43:固定盤 43: Fixed plate

44:水盤 44: Water Tray

441:漏斗狀底面 441: Funnel-shaped bottom

45:洩壓閥 45: Pressure relief valve

500:曝氣管組 500: Aeration tube group

P:水位線 P: water level line

H:水槽的高度 H: height of the sink

L:水槽底部到拉西環層隔框的距離 L: The distance from the bottom of the sink to the Raschig ring shelf

D:水槽的直徑 D: Diameter of the sink

W:水盤的直徑 W: the diameter of the water pan

Claims (9)

一種廢氣洗滌塔之重力式混流裝置,係於廢氣洗滌塔的內部設有洗滌層與灑水裝置,使廢氣從洗滌塔下方的進氣口進入,經過洗滌層與灑水裝置的洗滌,再從上方之排氣口排出;其特徵在於:所述廢氣洗滌塔的底部設有一重力式混流裝置,該重力式混流裝置係於水槽的內部設一洩流管,該洩流管的周邊設有曝氣管組,該洩流管的上端連接一水盤,該水盤藉由一拉西環層隔框吊掛,其底部與洩流管連通,其間設有一洩壓閥,該洩壓閥可在水盤承接的水量超過一定壓力時打開,使水盤內所承接的清洗後廢水進入洩流管,再從曝氣管組噴射流出。 A gravity mixed-flow device for an exhaust gas washing tower is provided with a washing layer and a sprinkler device inside the exhaust gas washing tower, so that the exhaust gas enters from the air inlet below the washing tower, is washed by the washing layer and the sprinkler device, and then flows out of the exhaust gas washing tower. It is characterized in that: the bottom of the exhaust gas washing tower is provided with a gravity-type mixed flow device, and the gravity-type mixed flow device is provided with a drain pipe inside the water tank, and the periphery of the drain pipe is provided with an aerator The air pipe group, the upper end of the drain pipe is connected to a water pan, the water pan is suspended by a Raschig ring layer frame, the bottom of which is communicated with the drain pipe, and a pressure relief valve is arranged therebetween, and the pressure relief valve can be installed in the water pan When the amount of water received exceeds a certain pressure, it is opened, so that the cleaned wastewater received in the water pan enters the discharge pipe, and then sprays out from the aeration pipe group. 如申請專利範圍第1項所述之廢氣洗滌塔之重力式混流裝置,其中所述拉西環層隔框設於所述廢氣洗滌塔之進氣口的上方,所述水槽設於所述廢氣洗滌塔之進氣口的下方。 The gravity-type mixed flow device of the exhaust gas scrubbing tower according to the claim 1, wherein the Raschig ring layer frame is arranged above the air inlet of the exhaust gas scrubbing tower, and the water tank is arranged in the exhaust gas Below the inlet of the scrubber. 如申請專利範圍第2項所述之廢氣洗滌塔之重力式混流裝置,其中所述水盤的盤面直徑小於所述水槽的內徑,使清洗後廢水從洗滌塔上方流下時,部份清洗後廢水直接流入所述水槽內部,部份清洗後廢水則流入所述水盤內。 According to the gravity type mixed flow device of the exhaust gas washing tower described in the second item of the patent application scope, the diameter of the surface of the water pan is smaller than the inner diameter of the water tank, so that when the washed wastewater flows down from the top of the washing tower, part of the washed wastewater It directly flows into the water tank, and part of the waste water after cleaning flows into the water pan. 如申請專利範圍第3項所述之廢氣洗滌塔之重力式混流裝置,其中所述水盤係可漂浮於所述水槽之水面上,藉 由水槽內之浮力效應支撐其重量。 The gravity-type mixed-flow device for the exhaust gas scrubbing tower as described in item 3 of the patent application scope, wherein the water pan can float on the water surface of the water tank, thereby Its weight is supported by the buoyancy effect in the tank. 如申請專利範圍第1項所述之廢氣洗滌塔之重力式混流裝置,其中所述廢氣洗滌塔的外部設有一集水箱,該集水箱連通管路至所述水槽的最上端,以汲取所述水槽上方含有漂浮粉塵之溢流水。 The gravity-type mixed-flow device for the exhaust gas scrubbing tower as described in claim 1, wherein a water collecting tank is arranged outside the exhaust gas scrubbing tower, and the water collecting tank communicates with the pipeline to the uppermost end of the water tank to draw the Overflow water containing floating dust above the sink. 如申請專利範圍第1至5項中任一項所述之廢氣洗滌塔之重力式混流裝置,其中所述曝氣管組分別設有上層曝氣管、中層曝氣管及下層曝氣管,每一層曝氣管分別設有多數曝氣管單元。 The gravity-type mixed-flow device for an exhaust gas scrubbing tower according to any one of the claims 1 to 5 of the application scope, wherein the aeration tube group is respectively provided with an upper layer aeration tube, a middle layer aeration tube and a lower layer aeration tube, Each layer of aeration pipes is respectively provided with a plurality of aeration pipe units. 如申請專利範圍第6項所述之廢氣洗滌塔之重力式混流裝置,其中所述曝氣管組之上層曝氣管的曝氣管單元與中層曝氣管的曝氣管單元以30度錯開;所述中層曝氣管與下層曝氣管的曝氣管單元以30度錯開。 The gravity-type mixed-flow device for the exhaust gas scrubbing tower as described in item 6 of the patent application scope, wherein the aeration pipe unit of the upper layer of the aeration pipe and the aeration pipe unit of the middle layer of the aeration pipe are staggered by 30 degrees ; The aeration tube units of the middle layer aeration tube and the lower layer aeration tube are staggered by 30 degrees. 如申請專利範圍第7項所述之廢氣洗滌塔之重力式混流裝置,其中所述上層曝氣管、中層曝氣管及下層曝氣管的曝氣管單元係相互間隔90度。 The gravity-type mixed flow device for the exhaust gas washing tower as described in claim 7, wherein the aeration pipe units of the upper aeration pipe, the middle aeration pipe and the lower aeration pipe are spaced 90 degrees apart from each other. 如申請專利範圍第8項所述之廢氣洗滌塔之重力式混流裝置,其中所述上層曝氣管的曝氣管單元,其管徑最大,長度最短;所述中層曝氣管的曝氣管單元,其管徑適中,長度適中;所述下層曝氣管的曝氣管單元,其管徑最小,長度最長;藉此提供洩流管的各個角度均有曝氣管單元,使循環清洗後廢水進入洩流管後可從不同高度、不 同角度及不同流速射出,達到對所述水槽內的廢水充分擾動。 The gravity-type mixed-flow device for the exhaust gas washing tower as described in item 8 of the patent application scope, wherein the aeration pipe unit of the upper aeration pipe has the largest pipe diameter and the shortest length; the aeration pipe of the middle layer aeration pipe The aeration pipe unit of the lower aeration pipe has the smallest pipe diameter and the longest length; thereby providing aeration pipe units at all angles of the discharge pipe, so that after the circulation cleaning After the waste water enters the drain pipe, it can be discharged from different heights, different Injection at the same angle and different flow rates can fully disturb the wastewater in the water tank.
TW111201138U 2022-01-27 2022-01-27 Gravity mixed flow device for waste gas scrubber TWM630138U (en)

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