TW201328954A - Method and device for pumping high concentration sediment with compressed air - Google Patents
Method and device for pumping high concentration sediment with compressed air Download PDFInfo
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- TW201328954A TW201328954A TW101100039A TW101100039A TW201328954A TW 201328954 A TW201328954 A TW 201328954A TW 101100039 A TW101100039 A TW 101100039A TW 101100039 A TW101100039 A TW 101100039A TW 201328954 A TW201328954 A TW 201328954A
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- 239000013049 sediment Substances 0.000 title claims abstract description 99
- 238000000034 method Methods 0.000 title claims abstract description 32
- 238000005086 pumping Methods 0.000 title claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims description 31
- 239000010802 sludge Substances 0.000 claims description 28
- 238000007599 discharging Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 3
- 230000035485 pulse pressure Effects 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 238000010586 diagram Methods 0.000 description 4
- 239000000523 sample Substances 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 206010036790 Productive cough Diseases 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 210000003802 sputum Anatomy 0.000 description 1
- 208000024794 sputum Diseases 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
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- Treatment Of Sludge (AREA)
Abstract
Description
空氣泵浦於工業界中廣泛運用於流體狀漿料之輸送,該機種低磨耗製造簡單係一相當低廉且成熟之技術。Air pumping is widely used in the industry for the transport of fluid-like slurries, which are a relatively inexpensive and mature technology.
本案發明人於民國98年5月11日所提出之098116360號發明專利申請案之低磨耗以壓縮空氣汲送原料之方法及裝置(以下簡稱空氣泵浦),該發明並未詳細述明當空氣泵浦置於湖泊港灣等水體中時抽除底泥之方法,本發明人乃針對深水中底泥之抽除設計出一種高濃度底泥以壓縮空氣汲送之方法及裝置,先將空氣泵浦排空後再藉助深水之水壓強制將高濃度膠體狀底泥擠入空氣泵浦,再藉導入壓縮空氣將高濃度底泥擠出空氣泵浦至目的點,使抽出之底泥濃度達到最高,免除傳統沉水泵浦面對太濃之底泥無法抽除,需加水稀釋攪動方能抽除,導致抽泥濃度太低使抽泥效率不彰,本案發明構件中並無轉動元件即使底泥中有雜物並不會卡住轉動元件無清除雜物之困擾,其妥善率高,底泥可原狀抽除擁有最高之濃度,為一構造簡單成本低廉妥善率高之泵浦者。The method and apparatus for low-abrasive consumption of compressed air to feed raw materials (hereinafter referred to as air pumping) in the invention patent application No. 098,116,360, which was filed on May 11, 1998, the inventor of the present invention. The method for pumping out the sediment when the pump is placed in a water body such as a lake harbor, the present inventors have designed a method and a device for the high-concentration sediment to extract the compressed air for the extraction of the sediment in the deep water, firstly the air pump After the pumping is drained, the high-concentration colloidal bottom mud is forced into the air pump by means of the deep water pressure, and then the compressed air is introduced to pump the high-concentrated sediment to the target point, so that the extracted sludge concentration reaches The highest, exempting the traditional submersible pump from the too thick bottom mud can not be removed, need to add water to dilute the agitation to be able to pump out, resulting in too low mud concentration to make the pumping efficiency is not good, there is no rotating element in the invention component There is debris in the bottom mud and it will not get stuck in the rotating components without removing debris. The proper rate is high, and the sediment can be pumped out to have the highest concentration. It is a pump with simple structure, low cost and high proper rate.
為使 貴審查委員能更了解本發明構造、操作流程、功效、原理及其特徵茲配合圖示說明於後。In order to enable the review board to better understand the structure, operation flow, function, principle and characteristics of the present invention, it is described in conjunction with the illustration.
如圖1所示本發明之高濃度底泥以壓縮空氣汲送之方法及裝置,由密閉槽體(1)、探泥管組(2)(3)、進排氣管組(5)(7)(8)及導泥管組(4)(6)(20)所組成。其中密閉槽體係直立圓形密閉槽體可承受壓縮空氣(25)之壓力及環繞於槽體四週之水體壓縮力,該槽體以垂直方式配置,其槽身中心線下方端板正中央裝設探泥管(2),探泥管(2)係一中空管,與槽體軸心線重合配置,探泥管(2)上裝設入料逆止閥(3)該逆止閥(3)使流體底泥(19)僅能流入槽體(1)而無法排出槽體(1)之方向配置;槽體(1)正中央裝設導泥內管(6),其往上延伸穿透槽頂端板並連接裝設排料逆止閥(4)後連接排泥管(20),用以將底泥汲送至目的點,該逆止閥(4)使底泥於汲送過程中無法逆流回密閉槽體(1),導泥內管(6)係一中空管,軸向底端則沿密閉槽體(1)軸心線往下延伸至適當高度終止,導泥內管(6)軸向底端與密閉槽體(1)下端板間所形成之容積相對應水重+密閉槽體(1)之結構體重需大於密閉槽體(1)將槽內原料以壓縮空氣(10)完全擠出之容積相對應浮力,使密閉槽體(1)於沉水抽泥作業時不致發生密閉槽體(1)上浮之狀況者;以導泥內管(6)導引液態底泥(19)於密閉槽體(1)內向上位移,並阻隔壓縮空氣(25)衝破液面短流排出密閉槽體(1),導泥內管(6)再連接排泥管(20)將底泥導引至目的點;進排氣管組與槽體(1)上方端板之引氣管(5)連接,進排氣管組上裝設進氣閥(7)與排氣閥(8)兩者間以引氣三通(9)與引氣管(5)相連,用以導引壓縮空氣進出密閉槽體(1),其中排氣閥(8)用以排出密閉槽體(1)內之壓縮空氣(10),而進氣閥(7)用以導引壓縮空氣(10)將槽體(1)內之高濃度底泥擠出,於空氣泵浦沉水汲泥作業時,進排氣管組並未隨密閉槽體(1)沉入水體中,而係離水裝設於抽泥船(15)上者;密閉槽體(1)上方端板焊設吊點,抽泥船(15)上之吊車(16)將空氣泵浦以垂直方式吊入湖泊或海洋內用以抽除沉積於湖泊海洋底部之高濃度底泥。The method and apparatus for conveying high-concentration sediment of the present invention by compressed air as shown in FIG. 1 are composed of a closed tank body (1), a mud collecting pipe group (2) (3), and an intake and exhaust pipe group (5) ( 7) (8) and the mud pipe group (4) (6) (20). The closed trough system upright circular closed trough body can withstand the pressure of the compressed air (25) and the water body compressing force around the trough body, the trough body is arranged in a vertical manner, and the end plate of the trough body center line is installed at the center of the end plate The mud pipe (2), the mud pipe (2) is a hollow pipe, which is arranged to coincide with the axis line of the tank body, and the mud check pipe (2) is provided with a feed check valve (3). 3) The fluid bottom mud (19) can only flow into the tank body (1) and cannot be discharged in the direction of the tank body (1); the tank body (1) is provided with a mud guide inner tube (6) in the center thereof, which extends upward Passing through the top plate of the trough and connecting the discharge check valve (4), and then connecting the drain pipe (20) for delivering the bottom mud to the destination point, the check valve (4) allowing the bottom mud to be sent During the process, it is impossible to return to the closed tank body (1), and the inner mud tube (6) is a hollow tube. The axial bottom end extends along the axial line of the closed tank body (1) to the appropriate height to terminate. The volume formed between the axial bottom end of the inner tube (6) and the lower end plate of the closed tank body (1) corresponds to the water weight + the closed tank body (1) has a structural weight greater than that of the closed tank body (1) The volume of the compressed air (10) is completely extruded corresponding to the buoyancy, so that the airtight The body (1) does not cause the condition of the closed tank body (1) to float when the submerged mud pumping operation; the liquid bottom mud (19) is guided to guide the liquid bottom mud (19) to be displaced upward in the closed tank body (1). And blocking the compressed air (25) to break through the short surface of the liquid surface to discharge the closed tank body (1), and the mud inner pipe (6) is connected to the mud discharging pipe (20) to guide the sediment to the destination point; the intake and exhaust pipe group Connected to the air inlet pipe (5) of the upper end plate of the tank body (1), and the air intake valve (7) and the exhaust valve (8) are arranged between the intake and exhaust pipe group to be ventilated tee (9) and The air inlet pipe (5) is connected to guide the compressed air into and out of the sealed tank body (1), wherein the exhaust valve (8) is used for discharging the compressed air (10) in the closed tank body (1), and the intake valve ( 7) It is used to guide the compressed air (10) to extrude the high concentration sediment in the tank body (1). When the air pumping submerged mud is used, the intake and exhaust pipe group does not follow the sealed tank body (1) Sink into the water body, and the water is installed on the mud pump (15); the upper end plate of the closed tank body (1) is welded with the lifting point, and the crane (16) on the mud pump (15) pumps the air. It is hoisted vertically into a lake or ocean to remove high concentrations of sediment deposited on the bottom of the lake.
如圖2、3、4、5、6、7、8、9所示之高濃度底泥以壓縮空氣汲送底泥之方法及裝置,該方法包括密閉槽體(1)沉水步驟、排氣入泥步驟及進氣排泥步驟。本發明當其用於抽除湖泊及海洋等深水區域底泥(19)時,首先進行密閉槽體(1)沉水步驟,抽泥船(15)上之吊車(16)將密閉槽體(1)垂直吊起,使探泥管(2)垂直液面向下緩速入水,首先進氣閥(7)關閉,排氣閥(8)開啟,湖中清水(18)擁入槽體(1)中,俟密閉槽體(1)完全入水之同時關閉排氣閥(8)停止水體入槽,俟探泥管(2)深入湖底部之底泥層(19)後停止槽體下降,將進氣閥(7)打開,導引壓縮空氣(10)注入槽體(1)上方,槽內液體承受壓縮空氣(10)之正壓力自排料逆止閥(4)被壓出循排泥管(20)排出密閉槽體(1),受入料逆止閥(4)之阻擋使槽內液體無法循探泥管(2)流回湖泊,汲送至目的點之液體受排料逆止閥(4)之阻擋無法逆流回槽內(1),以壓縮空氣(10)之持續加壓使槽內液體持續排出,俟槽內液位下降至導泥內管(6)之軸向下緣時,壓縮空氣(10)無液面之阻擋將直接穿入導泥內管(6),使槽內液體停止排出密閉槽體(1);接著進入排氣入泥步驟,此時進氣閥(7)關閉排氣閥(8)開啟槽內壓縮空氣(10)循引氣管(5)及排氣閥(8)逸入大氣中,當槽內壓力低於密閉槽體(1)四週之水壓時,底泥(19)循探泥管(4)被強制擠入密閉槽體(1)內,俟底泥入流達到額定時間時關閉排氣閥(8)停止底泥流入密閉槽體(1);接著進入進氣排泥步驟,進氣閥(7)開啟壓縮空氣(10)注入槽體(1)上方,槽內液體承受壓縮空氣(10)之正壓力自排料逆止閥(4)被壓出循排泥管(20)排出密閉槽體(1),受入料逆止閥(4)之阻擋使槽內底泥無法循探泥管(2)流回湖泊,汲送至目的點之液體受排料逆止閥(4)之阻擋無法逆流回槽內(1),以壓縮空氣(10)之持續加壓使槽內液體持續排出令槽內液位下降,排泥至額定時間關閉進氣閥(7)再進入排氣入泥步驟,再填充底泥入密閉槽體(1),以排氣入泥步驟及進氣排泥步驟這兩步驟交替運轉,用以持續抽除底泥;於底泥抽除過程中可用吊車(16)水平移動密閉槽體(1)使探泥管(2)隨時沒入底泥(19)中位移,將探泥管(2)所經過區域之底泥抽除,而達到即時及大面積底泥逐次抽除之方法者。The method and device for delivering high-concentration bottom sediment with compressed air as shown in Figures 2, 3, 4, 5, 6, 7, 8, and 9 include a closed tank (1) submerged step, row The gas entering step and the air intake step. When the present invention is used for removing sediments (19) in deep water areas such as lakes and oceans, the first step is to perform a submerged tank (1) submerged step, and the crane (16) on the dredger (15) will close the trough ( 1) Vertically hoist, so that the vertical liquid of the mud pipe (2) is slowly moved into the water. First, the intake valve (7) is closed, the exhaust valve (8) is opened, and the clear water (18) in the lake is filled into the tank (1) In the middle, the closed tank body (1) closes the exhaust valve (8) and stops the water body into the tank. The mud pipe (2) penetrates the bottom mud layer (19) at the bottom of the lake and stops the tank body. The intake valve (7) is opened, and the compressed air (10) is introduced into the tank body (1). The liquid in the tank is subjected to the positive pressure of the compressed air (10). The self-discharging check valve (4) is pressed out of the mud. The tube (20) is discharged from the sealed tank body (1), and is blocked by the feed check valve (4), so that the liquid in the tank cannot flow back to the lake according to the mud pipe (2), and the liquid sent to the destination point is rejected by the discharge material. The blockage of the valve (4) cannot be reversed back into the tank (1), and the continuous pressurization of the compressed air (10) continuously discharges the liquid in the tank, and the liquid level in the tank drops to the axial direction of the inner tube (6) of the mud. At the edge, the blockage of the compressed air (10) without liquid level will directly penetrate the inner tube (6). Stop the liquid in the tank and discharge it into the closed tank body (1); then enter the exhaust gas into the mud step, at this time the intake valve (7) closes the exhaust valve (8) to open the compressed air in the tank (10) to circulate the air pipe (5) And the exhaust valve (8) escapes into the atmosphere, and when the pressure in the tank is lower than the water pressure around the closed tank body (1), the sediment (19) is forced into the closed tank body according to the mud pipe (4) ( 1) Inside, when the bottom mud inflow reaches the rated time, close the exhaust valve (8) to stop the sludge from flowing into the closed tank (1); then enter the intake sludge step, and the intake valve (7) opens the compressed air (10) Injection into the tank body (1), the liquid in the tank is subjected to the positive pressure of the compressed air (10). The self-discharging check valve (4) is pressed out of the draining pipe (20) to discharge the sealed tank body (1). The blocking of the check valve (4) prevents the bottom mud in the tank from flowing back to the lake through the mud pipe (2), and the liquid sent to the destination point is blocked by the discharge check valve (4) and cannot be returned to the tank (1) Continuously pressurizing the compressed air (10) to continuously discharge the liquid in the tank to lower the liquid level in the tank, and to close the intake valve (7) after the sludge is discharged to the rated time, and then enter the exhaust gas into the mud step, and then fill the bottom mud into the airtight seal. Tank (1), stepping into the mud and stepping in the air These two steps are alternately operated to continuously remove the sediment; in the process of sediment extraction, the crane (16) can be used to horizontally move the closed tank (1) to make the probe (2) fall into the sediment (19) at any time. Displacement, the bottom mud of the area through which the mud pipe (2) passes is removed, and the method of instantaneous and large-area sediment removal is achieved.
如圖2、3、4、5、6、7、8、9所示之高濃度底泥以壓縮空氣汲送底泥之方法及裝置,當進行底泥汲送作業時,其密閉槽體(1)置於深水區域中,槽體四週承受之壓力等於水壓,當密閉槽體(1)內壓縮空氣(10)逐漸排空,密閉槽體(1)之內外壓差將逐漸加大,俟壓差大於底泥層(19)之底泥最大流動阻力,底泥將以原始污泥濃度狀態被擠入密閉槽體(1)內,密閉槽體(1)之探泥管(2)內並無會卡住底泥層(19)中雜物之轉動元件,只要能流入密閉槽體(1)之底泥均可藉壓縮空氣(10)擠出密閉槽體(1),因此其底泥內雜物容許範圍廣;當進行底泥汲送作業時,槽內之壓縮空氣(10)其比重遠低於槽內底泥(19),因此自然懸浮於槽內底泥(19)之上方,隨著壓縮空氣(10)持續注入密閉槽體(1)槽內底泥(19)於槽內位置自然被壓縮空氣取代而被擠出密閉槽體(1),槽內底泥(19)被擠出時其所能達到之最高揚程為壓縮空氣(25)之注入壓力,此壓縮空氣(10)之最低壓力需大於密閉槽體(1)所承受之水壓與底泥(19)於排泥管(20)流動壓損之總合;槽內液位下降至導泥內管(6)之軸向下緣底端時,無槽內底泥之阻隔壓縮空氣(10)將直接穿入導泥內管(6),槽內殘餘底泥再也無法被壓出密閉槽體(1),此時停止壓縮空氣注入密閉槽體(1)開啟排氣閥(8)使密閉槽體(1)內之壓縮空氣卸壓,俟槽內外壓差達到額定值,槽體四週之底泥(19)又被擠入槽內,當底泥注入達到額定時間液位達到預定上限值,再度灌入壓縮空氣(10)將槽內底泥壓往目的點,如此交替運轉以批次方式汲送湖底高濃度底泥(19),於底泥汲送過程中槽體上方之排料逆止閥(4)負責避免排泥管(20)內底泥於槽體執行排氣卸壓入泥步驟時逆流回密閉槽體(1)內,入料逆止閥(3)則防止執行進氣排泥作業時,槽內底泥受壓縮空氣加壓自入料逆止閥(3)及探泥管(2)流出密閉槽體(1)而排入槽外之湖泊內者。As shown in Figures 2, 3, 4, 5, 6, 7, 8, and 9, the high-concentration sediment is a method and apparatus for delivering sediment to compressed air, and when the bottom mud is sent, the closed tank body (the closed tank body ( 1) In the deep water area, the pressure around the tank body is equal to the water pressure. When the compressed air (10) in the closed tank body (1) is gradually emptied, the pressure difference between the inside and the outside of the closed tank body (1) will gradually increase. The pressure difference is greater than the maximum flow resistance of the sediment in the sediment layer (19). The sediment will be squeezed into the closed tank (1) in the original sludge concentration state, and the mud (1) of the closed tank (1) There is no rotating element that can catch the debris in the sediment layer (19). As long as it can flow into the bottom of the closed tank (1), the sealed tank (1) can be extruded by compressed air (10). The allowable range of debris in the sediment is wide; when the sediment is sent, the compressed air (10) in the tank is much lower than the sediment in the tank (19), so it is naturally suspended in the tank (19). Above, as the compressed air (10) continues to be injected into the closed tank (1), the bottom mud (19) is naturally replaced by compressed air in the tank and is extruded into the closed tank (1). 19) The highest it can be reached when it is squeezed out The process is the injection pressure of the compressed air (25). The minimum pressure of the compressed air (10) needs to be greater than the water pressure of the closed tank (1) and the flow pressure of the sediment (19) in the drain pipe (20). When the liquid level in the tank drops to the bottom end of the axial lower edge of the inner pipe (6), the compressed air (10) that does not have the inner bottom mud will directly penetrate the inner pipe (6), the groove The residual bottom mud can no longer be pressed out of the closed tank body (1). At this time, the compressed air is injected into the sealed tank body (1), and the exhaust valve (8) is opened to depressurize the compressed air in the closed tank body (1). The pressure difference between the inside and outside of the gutter reaches the rated value, and the bottom mud (19) around the tank is squeezed into the tank. When the sediment is injected to the rated time, the liquid level reaches the predetermined upper limit, and the compressed air (10) is refilled. The bottom mud in the tank is pressed to the target point, so that the high-concentration sediment (19) at the bottom of the lake is sent in batch mode, and the discharge check valve (4) above the tank is responsible for avoiding mud discharge during the sediment feeding process. The inner bottom mud of the tube (20) is countercurrently flowed back into the closed tank body (1) when the tank is subjected to the exhaust gas pressure relief mud-in step, and the feed check valve (3) prevents the inner bottom of the tank from being subjected to the air intake mud discharge operation. Mud pressurized by compressed air Feeding check valve (3) and the soil pipe probe (2) flowing out of the sealed tank (1) into the lake outside the groove by.
如圖2、3、4、5、6、7、8、9所示之高濃度底泥以壓縮空氣汲送之方法及裝置,當進行底泥汲送作業時,其密閉槽體(1)置於深水中探泥管(2)完全沒入底泥層(19),底泥被水壓強制擠入密閉槽體(1),即使底泥濃度高至呈膠體狀仍能被此正壓力強制擠往密閉槽體(1),因探泥管(2)隨時插入底泥層(19)因此槽體四週之清水(18)受底泥層(19)之阻隔不會流入密閉槽體(1)因此所汲送之底泥(19)擁有接近湖底污泥狀態之最高污泥濃度;且探泥管(2)及密閉槽體(1)內均無轉動元件,因此並不會卡住底泥層(19)內之雜物,只要循探泥管(2)流入之底泥(19)均能被壓縮空氣(10)強制擠往目的點,其汲送底泥效率高,所汲送底泥內含雜物容許範圍廣妥善率高。注入密閉槽體(1)之壓縮空氣(10)可任意調整使底泥輸出之揚程同步調整,不像一般抽水泵浦其抽水揚程為固定值,若抽除對象之污泥濃度太高,由於其濃泥之流動阻力大固定之揚程無法加大揚程使濃泥加速流動將使污泥抽除效率大符降低,需加水降低濃度提高流動性以使抽泥作業得以持續運作,此舉導致抽出之污泥含水率相對較高,使底泥之抽除效率低,且泵浦內之高速轉動元件極易卡住底泥層內之雜物而降低或失去抽泥效率,使其妥善率降低。本發明裝置當水深愈深時,底泥層(19)擠入密閉槽體(1)之壓差愈大,因此底泥所能擠入之濃度愈高,因此其汲送效果愈佳,只要能流入密閉槽體(1)之底泥均能被壓縮空氣(10)壓送至目的點,其所能輸送之底泥範圍廣泛,係一相當穩定價廉又可靠之新型沉水抽泥泵浦。As shown in Figures 2, 3, 4, 5, 6, 7, 8, and 9, the high-concentration sediment is sent by compressed air, and the closed tank body (1) is used when the bottom mud is sent. The mud pipe (2) placed in the deep water is completely immersed in the sediment layer (19), and the sediment is forced into the closed tank body by the water pressure (1), even if the sediment concentration is high to be colloidal, the positive pressure can be applied. Forced to squeeze into the closed tank (1), because the mud pipe (2) is inserted into the sediment layer (19) at any time, so the clear water around the tank (18) will not flow into the closed tank by the sediment layer (19). 1) Therefore, the sediment (19) sent by the sludge has the highest sludge concentration near the bottom of the lake; and there are no rotating elements in the mud pipe (2) and the closed tank (1), so it will not get stuck. The debris in the sediment layer (19) can be forced to be squeezed by the compressed air (10) to the destination point as long as the mud (19) flowing into the mud pipe (2) is high. The amount of impurities contained in the bottom mud is wide and the proper rate is high. The compressed air (10) injected into the closed tank body (1) can be adjusted arbitrarily to adjust the head of the sediment output synchronously. Unlike the conventional pumping pump, the pumping head is fixed, and if the sludge concentration of the pumping object is too high, The flow resistance of the thick mud is fixed. The lift can not increase the lift. Accelerating the flow of the thick mud will reduce the efficiency of sludge removal. It is necessary to add water to reduce the concentration and improve the fluidity so that the pumping operation can continue to operate. The sludge has a relatively high water content, which makes the sediment removal efficiency low, and the high-speed rotating components in the pump easily catch the debris in the sediment layer to reduce or lose the pumping efficiency, so that the proper rate is lowered. . When the water depth is deeper, the pressure difference of the bottom mud layer (19) squeezed into the closed tank body (1) is larger, so the higher the concentration that the bottom mud can be squeezed, the better the sputum delivery effect is as long as The bottom mud which can flow into the closed tank body (1) can be sent to the target point by the compressed air (10), and the bottom mud which can be transported is widely distributed, and is a new type of submerged mud pump which is relatively stable, inexpensive and reliable. Pu.
如圖2、3、4、5、6、7、8、9所示之高濃度底泥以壓縮空氣汲送之方法及裝置,其進行底泥汲送作業之模式係批次式,若要連續抽取底泥則需設置雙槽空氣泵浦組。如圖10、11所示之雙槽高濃度底泥以壓縮空氣汲送之方法及裝置,其設置兩個互相獨立之第一循環槽(22)及第二循環槽(23),每一循環槽(22)(23)均係一可獨立運作之空氣泵浦,其上各自排泥管(20)互相連接成單一管線,排泥管(20)與循環槽(22)(23)間再以排料逆止閥(4)相接,其上進排氣管組之進氣閥(24)(26)相互串聯至空氣源,並將此互相獨立之第一循環槽(22)及第二循環槽(23)彼此固接成一體,各自獨立之空氣泵浦循環槽(22)(23)其串接數量若愈多,則於槽體切換汲泥過程中,其槽體交換壓送底泥之瞬間所造成排泥管(20)之壓力脈衝現象將愈低,相對串接循環槽之數量愈高排泥管(20)脈衝壓現象將大為降低,流體輸送之穩定度愈高。As shown in Figures 2, 3, 4, 5, 6, 7, 8, and 9, the high-concentration sediment is sent by compressed air, and the mode of the sediment-carrying operation is batch type. A continuous pumping of the sediment requires a double-slot air pumping unit. The method and device for sending a double-slot high-concentration sediment as shown in Figs. 10 and 11 by compressed air, which are provided with two mutually independent first circulation grooves (22) and second circulation grooves (23), each cycle The tanks (22) and (23) are each an independently operable air pump, wherein the respective drain pipes (20) are connected to each other into a single line, and between the drain pipe (20) and the circulation tank (22) (23). The discharge check valve (4) is connected, and the intake valves (24) (26) of the upper exhaust pipe group are connected in series to the air source, and the first circulation groove (22) and the first one are independent of each other. The two circulating grooves (23) are integrally fixed to each other, and the more the number of the series of the independent air pumping circulating grooves (22) (23), the groove exchange pressure is sent during the switching of the tank body. The pressure pulse phenomenon of the drain pipe (20) caused by the moment of the bottom mud will be lower. The higher the number of the serially connected circulation grooves, the higher the pulse pressure phenomenon of the drain pipe (20), and the higher the stability of fluid transport. .
如圖10、11所示之雙槽高濃度底泥以壓縮空氣汲送之方法及裝置,包括,初始入泥步驟,交替循環排泥步驟。本方法進行底泥汲取作業時,首先進入初始入料步驟,兩循環槽(22)(23)上之排氣閥(25)(27)開啟,使密閉槽體(1)之內壓與大氣等壓,探泥管(2)四週之底泥(19)被水壓循探泥管(2)及入料逆止閥(3)擠入循環槽(22)(23)內,俟槽內液上昇至額定時間後關閉排氣閥(25)(27)使槽內壓力與探泥管(2)四週之水壓相同令底泥(19)停止流入循環槽(22)(23)內,接著進入交替循環排料步驟;進行交替循環排料步驟時,先進行第一循環槽(22)之排料作業,第一循環槽(22)之進氣閥(24)開啟導引壓縮空氣(10)入槽,將槽內高濃度底泥向下壓送經導泥內管(6)、排料逆止閥(4)及排泥管(20)導引至目的點,當槽內液位下降至額定值或額定時間時,關閉進氣閥(24)停止第一循環槽之排料,進行第二循環槽(23)之進氣排料作業,打開第二循環槽進氣閥(26)導引壓縮空氣(10)注入第二循環槽(23)將槽內污泥向下壓送經導泥內管(6)、排料逆止閥(4)及排泥管(20)導引至目的點;於第二循環槽(23)排料之同時,第一循環槽(22)進行排氣入泥步驟,第一循環槽(22)之排氣閥(25)開啟導引底泥(19)注入第一循環槽(22)俟槽內液位達到額定值或額定時間時關閉排氣閥(25)待機,當第二循環槽(23)之液位下降至額定值或額定時間關閉進氣閥(26),再進入第一循環槽(22)之進氣排泥步驟,第一循環槽進氣閥(24)開啟注入壓縮空氣(10)將槽內污泥壓送至目的點,如此兩個循環槽(22)(23)週而復始交替運轉連續將底泥汲送至目的點者。The method and apparatus for delivering a double-slot high-concentration sediment as shown in Figs. 10 and 11 by compressed air, including the initial sludge introduction step, alternately circulating the sludge discharge step. When the method performs the bottom mud picking operation, first enters the initial feeding step, and the exhaust valve (25) (27) on the two circulating tanks (22) (23) is opened to make the internal pressure of the closed tank body (1) and the atmosphere Isobaric, the bottom mud (19) around the mud pipe (2) is squeezed into the circulation tank (22) (23) by the water pressure pipe (2) and the feed check valve (3). After the liquid rises to the rated time, close the exhaust valve (25) (27) so that the pressure in the tank is the same as the water pressure around the probe (2), so that the sediment (19) stops flowing into the circulation tank (22) (23). Then enter the alternating cycle discharging step; when performing the alternating cycle discharging step, the discharging operation of the first circulating tank (22) is first performed, and the intake valve (24) of the first circulating tank (22) is opened to guide the compressed air ( 10) Into the tank, press the high-concentration sediment in the tank downward through the mud inner tube (6), the discharge check valve (4) and the drain pipe (20) to the destination point. When the position drops to the rated value or rated time, close the intake valve (24) to stop the discharge of the first circulation tank, perform the intake discharge operation of the second circulation tank (23), and open the second circulation tank intake valve. (26) guiding the compressed air (10) into the second circulation tank (23) to press the sludge in the tank downward The pilot mud inner tube (6), the discharge check valve (4) and the mud discharge pipe (20) are guided to the destination point; while the second circulation groove (23) is discharged, the first circulation groove (22) Performing the venting step, the exhaust valve (25) of the first circulation tank (22) opens the pilot sludge (19) and is injected into the first circulation tank (22). When the liquid level in the tank reaches the rated value or rated time Close the exhaust valve (25) to stand by. When the liquid level of the second circulating tank (23) drops to the rated value or rated time, close the intake valve (26), and then enter the first circulating tank (22). Step, the first circulating tank intake valve (24) opens and injects compressed air (10) to pump the sludge in the tank to the destination point, so that the two circulating tanks (22) (23) are alternately operated alternately to continuously deliver the sludge. To the purpose of the point.
綜上所述本發明之高濃度底泥以壓縮空氣汲送之方法及裝置,有如下特徵:In summary, the method and apparatus for delivering high-concentration sediment of the present invention by compressed air have the following characteristics:
(一).抽除底泥濃度最高:本發明空氣泵浦之探泥管(2)深入深水區域之底泥層(19)內,底泥藉助水壓強制擠入密閉槽體(1)內,使所汲送底泥有接近底泥層之最高污泥濃度,無傳統沉水泵浦面對流動性不佳底泥需以加水攪動稀釋方能抽除導致所抽底泥濃度低,抽泥效率差之狀況發生,因此有最高之抽泥效率及最低之耗能。(One). The concentration of the bottom sediment is the highest: the air pumped mud pipe (2) of the present invention penetrates into the bottom mud layer (19) of the deep water area, and the bottom mud is forced into the closed tank body (1) by the water pressure, so that the bottom is muddy. The bottom sludge has a maximum sludge concentration close to the bottom mud layer. No traditional sinking pump faces the poor fluidity. The bottom mud needs to be diluted by adding water to remove the sludge. The concentration of the sludge is low and the sludge pumping efficiency is poor. The situation occurs, so there is the highest pumping efficiency and the lowest energy consumption.
(二).抽取底泥內容許雜物之範圍廣:空氣泵浦內無轉動元件,使卡住底泥中雜物之機率降至最低,只要能流經探泥管(2)之底泥,均可用壓縮空氣(10)壓送至目的點,為適用範圍廣泛又相對穩定及可靠之產品。(two). The range of allowable debris in the sediment is wide: there is no rotating element in the air pump, which minimizes the probability of getting stuck in the sediment. As long as it can flow through the bottom of the mud pipe (2), it can be compressed. The air (10) is pumped to the destination, which is a wide range of products that are relatively stable and reliable.
上述之高濃度底泥以壓縮空氣汲送之方法及裝置,其置於深水中,以空氣泵浦四週之水壓強制將底泥擠入空氣泵浦內並以壓縮空氣壓送底泥至使用點,其抽泥濃度高,容許底泥內含雜物範圍廣,為一甚具實用性及經濟性之泵浦裝置者。The above-mentioned high-concentration sediment is a method and a device for sending compressed air, which is placed in deep water, and the water pressure is pumped around the air to force the bottom mud into the air pump and the compressed air is used to deliver the sediment to the use. At the point, the mud concentration is high, and the sediment is allowed to have a wide range of impurities, which is a practical and economical pumping device.
本發明觀念創新可克服習用裝置缺失,抽泥濃度高容許泥中通過粒徑大,為一甚具實用性與創新性之發明,爰依法提出申請,尚祈 貴審查委員能惠予審查,並早日賜準本案專利為禱。The innovative concept of the invention can overcome the lack of conventional devices, and the high concentration of mud can allow the passage of large particle size in the mud, which is an invention with practicality and innovation, and the application is made according to law, and the review committee of the member can be reviewed, and As soon as possible, the patent of this case is prayed.
(1)...槽體(1). . . Slot
(2)...探泥管(2). . . Mud tube
(3)...入料逆止閥(3). . . Feed check valve
(4)...排料逆止閥(4). . . Discharge check valve
(5)...引氣管(5). . . Air vent tube
(6)...導泥內管(6). . . Guide mud inner tube
(7)...進氣閥(7). . . Intake valve
(8)...排氣閥(8). . . Vent
(9)...引氣三通(9). . . Ventilation tee
(10)...壓縮空氣(10). . . Compressed air
(11)...排氣(11). . . exhaust
(12)...入料(12). . . Feeding
(13)...排料(13). . . Marking
(14)...空氣泵浦下沉(14). . . Air pump sinking
(15)...抽泥船(15). . . Dredger
(16)...吊車(16). . . crane
(17)...貯泥倉(17). . . Mud storage silo
(18)...清水(18). . . Clear water
(19)...底泥(19). . . Sediment
(20)...排泥管(20). . . Drain pipe
(21)...水壓(twenty one). . . Water pressure
(22)...第一循環槽(twenty two). . . First cycle slot
(23)...第二循環槽(twenty three). . . Second cycle slot
(24)...第一循環槽進氣閥(twenty four). . . First circulation tank intake valve
(25)...第一循環槽排氣閥(25). . . First circulation tank exhaust valve
(26)...第二循環槽進氣閥(26). . . Second circulation tank intake valve
(27)...第二循環槽排氣閥(27). . . Second circulation tank exhaust valve
圖1.係本發明之高濃度底泥以壓縮空氣汲送之裝置正視圖。Figure 1. Front view of the apparatus for delivering high concentration sludge of the present invention in compressed air.
圖2.係本發明之高濃度底泥以壓縮空氣汲送之方法及裝置之下水示意圖。Figure 2. Schematic diagram of the method and apparatus for the high-concentration sediment of the present invention to be sent by compressed air.
圖3.係圖2中之視圖view:A之放大示意圖。Figure 3. is an enlarged schematic view of the view view: A in Figure 2.
圖4.係本發明之高濃度底泥以壓縮空氣汲送之方法及裝置之下水沉入底泥層排空槽內液體示意圖。Fig. 4 is a schematic view showing the liquid of the high-concentration sediment of the present invention which is sent to the sump of the sediment layer by the method and apparatus for the compressed air.
圖5.係圖4中之視圖view:B之放大示意圖。Figure 5. is an enlarged schematic view of the view view: B in Figure 4.
圖6.係本發明之高濃度底泥以壓縮空氣汲送之方法及裝置之槽體注泥示意圖。Figure 6. Schematic diagram of the tank filling method of the method and apparatus for conveying high-concentration sediment of the present invention by compressed air.
圖7.係圖6中之視圖view:C之放大示意圖。Figure 7. is an enlarged schematic view of the view view: C in Figure 6.
圖8.係本發明之高濃度底泥以壓縮空氣汲送之方法及裝置之滿料壓縮空氣壓送污泥示意圖。Figure 8. Schematic diagram of the full-size compressed air pressure-feeding sludge of the method and apparatus for high-concentration sediment of the present invention.
圖9.係圖8中之視圖view:D之放大示意圖。Figure 9. is an enlarged schematic view of the view view: D in Figure 8.
圖10.係本發明之雙槽高濃度底泥以壓縮空氣汲送之方法及裝置其第一循環槽壓送底泥及第二循環槽進泥程序圖。Figure 10 is a flow chart of the first circulating tank pressure feed bottom mud and the second circulation tank mud entering method of the double tank high concentration bottom sediment of the present invention.
圖11.係本發明之雙槽高濃度底泥以壓縮空氣汲送之方法及裝置其第一循環槽進泥程序及第二循環槽壓送底泥程序圖。Figure 11 is a schematic diagram of the first circulating tank mud entering procedure and the second circulating tank pressing sludge feeding method of the double tank high concentration sediment of the present invention.
(1)...密閉槽體(1). . . Confined tank
(2)...探泥管(2). . . Mud tube
(3)...入料逆止閥(3). . . Feed check valve
(4)...排料逆止閥(4). . . Discharge check valve
(5)...引氣管(5). . . Air vent tube
(6)...導泥內管(6). . . Guide mud inner tube
(7)...進氣閥(7). . . Intake valve
(8)...排氣閥(8). . . Vent
(9)...引氣三通(9). . . Ventilation tee
(10)...壓縮空氣(10). . . Compressed air
(11)...排氣(11). . . exhaust
(12)...入料(12). . . Feeding
(13)...排料(13). . . Marking
(22)...第一循環槽(twenty two). . . First cycle slot
(23)...第二循環槽(twenty three). . . Second cycle slot
(24)...第一循環槽之進氣閥(twenty four). . . Intake valve of the first circulation tank
(25)...第一循環槽之排氣閥(25). . . Exhaust valve of the first circulation tank
(26)...第二循環槽之進氣閥(26). . . Intake valve of the second circulation tank
(27)...第二循環槽之排氣閥(27). . . Exhaust valve of the second circulation tank
Claims (7)
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| TW101100039A TW201328954A (en) | 2012-01-02 | 2012-01-02 | Method and device for pumping high concentration sediment with compressed air |
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| TW201024544A (en) * | 2008-12-22 | 2010-07-01 | ri-yang Zhang | Low-wearing method and device to suck and deliver raw material by using compressed air |
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