TWM630138U - Gravity mixed flow device for waste gas scrubber - Google Patents
Gravity mixed flow device for waste gas scrubber Download PDFInfo
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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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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
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
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-
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
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
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/cm2。
The 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
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
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
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
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