TWI663002B - Feedback-type aqueous cyclonic separation system - Google Patents
Feedback-type aqueous cyclonic separation system Download PDFInfo
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- TWI663002B TWI663002B TW106134091A TW106134091A TWI663002B TW I663002 B TWI663002 B TW I663002B TW 106134091 A TW106134091 A TW 106134091A TW 106134091 A TW106134091 A TW 106134091A TW I663002 B TWI663002 B TW I663002B
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- 238000000926 separation method Methods 0.000 title claims abstract description 42
- 230000007246 mechanism Effects 0.000 claims abstract description 53
- 239000002245 particle Substances 0.000 claims abstract description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000012544 monitoring process Methods 0.000 claims abstract description 33
- 238000003756 stirring Methods 0.000 claims abstract description 28
- 239000002689 soil Substances 0.000 claims abstract description 22
- 238000001514 detection method Methods 0.000 claims abstract description 21
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 8
- 230000004308 accommodation Effects 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 8
- 238000012216 screening Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 230000005476 size effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 239000012190 activator Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本發明係提供一種反饋式水力漩流分離系統，該反饋式水力漩流分離系統係針對混合物中不同大小顆粒之物體進行分離與集收，而該反饋式水力漩流分離系統具有攪拌機構、分離機構與反饋監控機構；其中，該反饋監控機構具有分別設於該攪拌機構、分離機構間之流量偵測件、粒徑監測件及流量控制件，因此針對受到重金屬污染之土壤轉換為泥水進行分選處理，得以利用該等粒徑監測件、流量偵測件的設置，來適時針對該分選機構之泥水隨流速所排出之顆粒的流量、流速訊息進行分析回饋，以調整至適合之該泥水進給地流速與流量，有效達到所欲分離之顆粒粒度精準分離功效。The present invention provides a feedback-type hydrocyclone separation system. The feedback-type hydrocyclone separation system separates and collects objects of different size particles in a mixture. The feedback-type hydrocyclone separation system has a stirring mechanism and a separation mechanism. Mechanism and feedback monitoring mechanism; among them, the feedback monitoring mechanism has a flow detection element, a particle size monitoring element, and a flow control element respectively disposed between the stirring mechanism and the separation mechanism, so that the soil contaminated by heavy metals is converted into muddy water. The selection process can use the settings of the particle size monitoring components and flow detection components to timely analyze and feed back the flow and velocity information of the particles discharged by the muddy water of the sorting mechanism with the flow rate, so as to adjust to the appropriate muddy water. The flow velocity and flow of the feed can effectively achieve the precise separation of the particle size to be separated.
Description
本發明是有關於一種水力漩流分離系統設計，特別是一種反饋式水力漩流分離系統。 The invention relates to the design of a hydraulic swirling flow separation system, in particular to a feedback type hydraulic swirling flow separation system.
參閱圖1，習知攪拌分離裝置1包含有一攪拌機構11及一分離機構12；其中，該攪拌機構11具有一供重金屬污染之土壤(圖中未示出)容置之容器111，一伸置於該容器111內之作動件112，以及一設於該容器111底端用以與該分離機構12連接之輸接管113；另，該分離機構12具有一呈上寬下窄且內部開設有一容置空間122之錐形本體121，一設於該錐形本體121上且與該輸接管113連接之入口123，一設於該錐形本體121上方且一端伸入該錐形本體121內之集收管124，以及一設於該錐形本體121下方之承接斗125。 Referring to FIG. 1, the conventional stirring and separating device 1 includes a stirring mechanism 11 and a separating mechanism 12. Among them, the stirring mechanism 11 has a container 111 for containing heavy metal contaminated soil (not shown in the figure). An actuating member 112 in the container 111 and a transfer pipe 113 provided at the bottom end of the container 111 for connecting with the separating mechanism 12; in addition, the separating mechanism 12 has a width up and down and an accommodation opening inside. A conical body 121 in the space 122, an inlet 123 provided on the conical body 121 and connected to the transfer pipe 113, and a collection and collection provided above the conical body 121 and with one end protruding into the conical body 121 The tube 124 and a receiving bucket 125 disposed below the conical body 121.
是以，在針對受到重金屬污染之該土壤進行處理時，將該等土壤以及與該土壤相對應之比例水量放置於該攪拌機構11之該容器111內，藉由該作動件112於該容器111內產生攪拌驅動，以使該土壤、水在混合作用中呈泥水態樣，同時並於攪拌過程中再注入一可於該容器111中產生壓力之氣體，以使該泥水受到壓力作用而以高流速方式進入該錐形本體121內，並利用該錐形本體121具有上寬下窄之設計，使該泥水進入該容置空間122後便產生強烈之高流速，且具有離心之水流漩流作用，同時以使泥水在前述之作用下快速分離出具有粗、細顆粒等二種區隔尺寸之顆粒粒徑的區分。Therefore, when the soil contaminated with heavy metals is treated, the soil and the proportion of water corresponding to the soil are placed in the container 111 of the stirring mechanism 11, and the actuator 112 is placed in the container 111. An agitation drive is generated inside, so that the soil and water are in the state of mud and water in the mixing effect, and a gas that can generate pressure in the container 111 is injected during the stirring process, so that the mud and water are subjected to pressure to increase the pressure. The flow velocity is entered into the cone body 121, and the cone body 121 is designed to have a wide width and a narrow width, so that the muddy water enters the accommodating space 122 to generate a strong high flow velocity, and has a centrifugal water flow swirling effect. At the same time, to make the muddy water quickly separate out the particle size of the particles with two kinds of partition sizes, such as coarse and fine particles.
惟，實際使用後發現，習知該攪拌分離裝置1僅能藉由人為作動之方式，來針對水力漩流作動的控制，同時分離後之顆粒仍需透過一雷射分析才能確實所分離之顆粒粒徑係為所需的，因此在等待雷射分析之過程是需要約7天的等待期，雖然可有效分離出土壤粒徑，但分析期間過於耗時且效率差，故在分離效果不彰的情況下，又在單一流速狀況下是無法在短期間內有效且快速分離出較細顆粒物質，導致無法在一貫流程作業中精準有效地進行土壤粒徑之分離篩選，而造成有分離效果不佳之缺失，實有待改進。However, after actual use, it was found that the stirring and separation device 1 can only control the hydraulic swirling motion manually, and the separated particles still need to be analyzed by a laser to determine the separated particles. The particle size is required, so waiting for laser analysis requires a waiting period of about 7 days. Although the soil particle size can be effectively separated, the analysis period is too time-consuming and inefficient, so the separation effect is not good. In the case of a single flow rate, it is impossible to effectively and quickly separate the finer particulate matter in a short period of time, resulting in the inability to accurately and effectively perform soil particle size separation and screening in a consistent process operation, resulting in a separation effect. The lack of good needs to be improved.
因此，本發明之目的，是在提供一種反饋式水力漩流分離系統，其可針對進行水力漩流分選作用中之不同高低泥水流速進行監測與偵測，以適時針對高低泥水之流速所排出之顆粒的流量、流速訊息進行分析、反饋、調整，以達到精準地分離出不同顆粒粒度效果。Therefore, the object of the present invention is to provide a feedback type hydrocyclone separation system, which can monitor and detect different high and low muddy water flow speeds during the hydrocyclone sorting action, so as to timely discharge the high and low mud water flow rates The particle flow and velocity information are analyzed, fed back, and adjusted to achieve the effect of accurately separating different particle sizes.
於是，本發明反饋式水力漩流分離系統包含有一攪拌機構，一分離機構，以及一分別與該攪拌機構、分離機構連接之反饋監控機構；其中，該反饋監控機構具有一設於該攪拌機構之輸送管與該分離機構之入口間之流量偵測件，二分別設於該分離機構之接收管與承接斗處之粒徑監測件，一設於該入口與輸送管間之流量控制件，以及一分別與該流量偵測件、粒徑監測件及流量控制件連接之控制裝置，故當該分離機構與該攪拌機構正針對受到重金屬污染之土壤進行泥水分選處理時，該反饋監控機構之控制裝置得以透過該流量偵測件、粒徑監測件分別針對流出之粒徑進行偵測與監測之訊息的傳送，以供該控制裝置針對所接收之偵測與監測訊息進行比對、分析，以適時針對所傳輸之狀況進行反饋改善，故可針對不同泥水進行水力漩流分離作業，且精準有效地分離出所欲顆粒粒度效果。Therefore, the feedback type hydrocyclone separation system of the present invention includes a stirring mechanism, a separation mechanism, and a feedback monitoring mechanism connected to the stirring mechanism and the separation mechanism, respectively, wherein the feedback monitoring mechanism has a A flow detection element between the conveying pipe and the entrance of the separation mechanism, two particle size monitoring elements respectively provided at the receiving pipe and the receiving bucket of the separation mechanism, a flow control element provided between the inlet and the conveying pipe, and A control device connected to the flow detection part, the particle size monitoring part and the flow control part respectively, so when the separation mechanism and the stirring mechanism are performing sludge water selection treatment for soil contaminated by heavy metals, the feedback monitoring mechanism The control device can transmit the detection and monitoring information for the outflow particle size through the flow detection element and the particle size monitoring element, respectively, for the control device to compare and analyze the received detection and monitoring information. Provide feedback and improvement on the transmitted conditions in a timely manner, so hydraulic hydrocyclone separation operations can be performed for different muddy water, accurately and effectively. Particle size from the desired effect.
圖1是習知攪拌分離裝置之示意圖。 圖2是本發明一較佳實施例之示意圖。 圖3是該較佳實施例之反饋監控模式之方塊示意圖。FIG. 1 is a schematic diagram of a conventional stirring separation device. FIG. 2 is a schematic diagram of a preferred embodiment of the present invention. FIG. 3 is a schematic block diagram of a feedback monitoring mode of the preferred embodiment.
有關本發明之前述及其他技術內容、特點與功效，在以下配合參考圖式之較佳實施例的詳細說明中，將可清楚的明白。The foregoing and other technical contents, features, and effects of the present invention will be clearly understood in the following detailed description of the preferred embodiments with reference to the accompanying drawings.
參閱圖2，本發明之一較佳實施例，該反饋式水力漩流分離系統3包含有一攪拌機構31，一分離機構32，以及一分別與該攪拌機構31、分離機構32連接之反饋監控機構33(圖中以簡圖表示)；其中，該攪拌機構31具有一容器311，一伸置於該容器311內之作動件312，以及一設於該容器311底端用以與該分離機構32連接之輸送管313，而前述該容器311可供欲進行攪拌之受重金屬污染之土壤置入，以及相對該土壤之重量對應注入適當比例之水量，而該作動件312即會在驅動作用下於該容器311中進行攪拌，使得該土壤與水在該作動件312的作動下於該容器311中混合呈泥水狀，同時在控制該作動件312的攪動速度設定，可依據混合之土壤與水之比例的不同，以進一步控制該作動件312之攪拌速度的驅動設定，同時在進行攪拌的過程中可適時於該容器311中注入一氣體(圖中未示)，利用所注入之氣體配合該作動件312的作動，而於該容器311內形成一壓力，以使受攪拌而形成之泥水受到壓力作用下經該輸送管313往該分離機構32處輸送。Referring to FIG. 2, according to a preferred embodiment of the present invention, the feedback type hydrocyclone separation system 3 includes a stirring mechanism 31, a separation mechanism 32, and a feedback monitoring mechanism connected to the stirring mechanism 31 and the separation mechanism 32 respectively. 33 (shown as a simplified diagram in the figure); wherein the stirring mechanism 31 has a container 311, an actuator 312 extending into the container 311, and a bottom end of the container 311 for connecting with the separating mechanism 32 The conveying pipe 313, and the container 311 described above can be used for the soil contaminated by heavy metals to be stirred, and an appropriate proportion of water can be injected corresponding to the weight of the soil, and the actuator 312 will be driven by the The container 311 is stirred so that the soil and water are mixed in the container 311 in the form of muddy water under the action of the moving member 312. At the same time, the stirring speed of the moving member 312 is controlled to be set according to the mixed soil and water ratio. In order to further control the driving setting of the stirring speed of the actuating member 312, at the same time, a gas (not shown in the figure) can be injected into the container 311 at the same time during the stirring process. The gas is fitted into the actuating member 312 is actuated to form a pressure in the container 311, so that the muddy water by stirring to form under pressure by the separating means to the conveyor 32 through the delivery tube 313.
接續前述，另，該分離機構32具有一呈上寬下窄且內部開設有一容置空間322之錐形本體321，一設於該錐形本體321上且與該輸送管313連接之入口323，一設於該錐形本體321上方且一端伸至於該錐形本體321內之集收管324，以及一設於該錐形本體321下方之承接斗325，而前述該入口323可承接經該輸送管313輸出之具有壓力之泥水至該容置空間322內，利用該錐形本體321所呈之上寬下窄的特殊設計，藉此能使該泥水進入該容置空間322後即瞬間形成具高流速水力漩流現象，且順沿該錐形本體321之特殊設置而於該容置空間322內產生一水流離心力作用，因此在水流離心力與高流速所形成之離沉下降力量，得以進一步使泥水中顆粒在流速中形出較重、較粗及較輕、較細之粒徑區分，即較輕、較細之顆粒會受到水力漩流所形成之離心力的水流作用往上升，而較重、較粗之顆粒便會順水力漩流離心力的作用而往下流沉，且分別透過該集收管324與該承接斗325向外排出。Continuing from the foregoing, in addition, the separating mechanism 32 has a tapered body 321 which is wide up and narrow and has an accommodation space 322 inside, an inlet 323 provided on the tapered body 321 and connected to the conveying pipe 313. A collecting tube 324 provided above the tapered body 321 and one end extending into the tapered body 321, and a receiving bucket 325 provided below the tapered body 321, and the inlet 323 can be received by the conveyor. The pressured mud and water output from the tube 313 enters the containing space 322, and the special design of the tapered body 321 is wide and narrow, so that the mud and water can enter the containing space 322 and form a tool instantly. High-speed hydraulic swirling phenomenon, and along the special setting of the cone body 321, a water flow centrifugal force is generated in the accommodation space 322, so the sinking and lowering force formed by the water flow centrifugal force and high flow rate can further make The particles in the muddy water form a heavier, coarser, lighter, and finer particle size in the flow rate, that is, the lighter and finer particles will be increased by the centrifugal force of the hydrodynamic swirling flow, and the heavier Coarser particles It will smooth swirl force and the centrifugal force to flow down sink, respectively, through the current collector and closing the discharge pipe 324 to the receiving hopper 325 outwardly.
最後，該反饋監控機構33具有一設於該入口323與該輸送管313間之流量偵測件331，二分別設於該集收管324與該承接斗325處之粒徑監測件332，一設於該入口323與該輸送管313間之流量控制件333，以及一分別與該流量偵測件331、粒徑監測件332及流量控制件333連結之控制裝置334；其中，該流量偵測件331可偵測由該入口323承接該輸送管313輸入之泥水的流量，同時該等粒徑監測件332可監測向該集收管324與該承接斗325之流速的變化，且將所偵測及監測所得之數據連結至該控制裝置334處，另，該控制裝置334內預先存有一預設值，以使該控制裝置334將所得之流量、流速之數據可與預設值進行比對、分析，以得出一比對結果，並適時針對結果發出一控制訊號連接至該流量控制件333，以使該流量控制件333接收到該控制裝置334的指示後於該入口323與該輸送管313間執行指示作動。Finally, the feedback monitoring mechanism 33 has a flow detection element 331 provided between the inlet 323 and the conveying pipe 313, and a particle size monitoring element 332 provided at the collecting and collecting pipe 324 and the receiving bucket 325, respectively. A flow control member 333 provided between the inlet 323 and the conveying pipe 313, and a control device 334 connected to the flow detection member 331, the particle size monitoring member 332, and the flow control member 333, respectively. Among them, the flow detection The piece 331 can detect the flow of mud water input by the inlet pipe 313 from the conveying pipe 313, and the particle size monitoring pieces 332 can monitor the change of the flow velocity to the collecting pipe 324 and the receiving bucket 325, and detect the detected flow rate. The measured and monitored data is linked to the control device 334. In addition, a preset value is stored in the control device 334 in advance, so that the control device 334 can compare the obtained flow and velocity data with the preset value And analysis to obtain a comparison result, and send a control signal to the flow control member 333 in time for the result, so that the flow control member 333 receives the instruction of the control device 334 and communicates with the inlet 323 and the conveyance. Tube 313 execute instructions
參閱圖2及圖3，使用時，集收已於事前先經過初步篩分後且小於2mm以下之固體粒子之受重金屬污染的土壤(圖中未示)，同時針對該土壤之重量備置相對應比例的水置入於該攪拌機構31之該容器311內，而後驅動該作動件312於該容器311內進行攪拌的作動，如此可使置於該容器311內之該土壤與水在該作動件312的攪拌下，進而混合呈如泥水態樣，這時更可在攪拌過程中於該容器311中注入一氣體(圖中未示)，利用該氣體的加入來增加該容器311內的壓力，使得攪拌中而形成的泥水在受到壓力的作用下，即以高流速之方式透過該輸送管313經該入口323進入該錐形本體321之容置空間322內，這時在該泥水流入該錐形本體321內的過程中，該流量偵測件331便會針對該泥水的流量進行偵測，且將偵測所得之數據連接至該控制裝置334，而該控制裝置334便會針對所接收之流量數據與預設於內之數據進行比對，以利後續針對該泥水之流速與流量進行控制調整，同時在該泥水進入該錐形本體321內時，便會受到該錐形本體321之上寬下窄之特殊設計影響，而於該容置空間322中產生具有強烈之高流速與離心力的水力漩流作用，藉由在水力漩流離心力與高流速所形成之離沉下降力量，進而使該泥水中顆粒在流速中形成出較重、較粗及較輕、較細之顆粒區分，即較輕、較細之顆粒會順延離心力之水流作用往上升，而較重、較粗之顆粒便會順水流離心而向下沉，這時設於該集收管324與該承接斗處325之該等粒徑監測件332，便會各別在該泥水分別形成往上升與向下沉的向外排出過程中，針對往上升之泥水流況與向下沉之泥水流況中的顆粒大小進行數據集收，且將該等泥水流況之顆粒大小的數據連接至該控制裝置334接收，使得該控制裝置334針對所接收之該泥水流況數據來與預設值進行比對、分析，此時若正監測往上升之該泥水流況中呈現出具有多數粒徑粗及大之顆粒時，這時該控制裝置334便會發出一控制訊號至該流量控制件333接收，以使該流量控制件333得以於該攪拌機構31與該分離機構32間，適當針對該泥水的輸入速度、流量進行調整控制，同時再藉由該流量偵測件331適時配合針對泥水流量輸入狀況進行偵測數據傳送，以利進行相互比對，藉以確實調整至適合該泥水進給地流入該容置空間322內之水力漩流速度。Refer to Figure 2 and Figure 3. When using, collect the soil contaminated by heavy metals (not shown in the figure) with solid particles less than 2mm in size after preliminary screening beforehand, and prepare the corresponding weight for the soil. Proportion of water is placed in the container 311 of the stirring mechanism 31, and then the actuator 312 is driven to perform the stirring operation in the container 311, so that the soil and water placed in the container 311 can be in the actuator. Under the stirring of 312, the mixture is in the state of mud and water. At this time, a gas (not shown) can be injected into the container 311 during the stirring process, and the pressure in the container 311 is increased by adding the gas, so that Under the action of pressure, the muddy water formed during stirring passes through the conveying pipe 313 through the inlet 323 and enters the containing space 322 of the tapered body 321 at a high flow rate. At this time, the muddy water flows into the tapered body During the process in 321, the flow detection element 331 will detect the mud water flow, and connect the detected data to the control device 334, and the control device 334 will respond to the received flow data. versus The data set inside are compared to facilitate subsequent control and adjustment of the muddy water flow rate and flow rate. At the same time, when the muddy water enters the tapered body 321, it will be affected by the width of the tapered body 321. Due to the special design influence, a strong hydrodynamic vortex with high flow velocity and centrifugal force is generated in the accommodation space 322. The sedimentation and descending force formed by the hydrodynamic vortex centrifugal force and high velocity makes the particles in the muddy water In the flow velocity, heavier, coarser, lighter, and finer particles are formed, that is, the lighter and thinner particles will continue to flow along the centrifugal force, and the heavier and coarser particles will be centrifuged along the water. And sinking down, the particle size monitoring pieces 332 set in the collecting and collecting pipe 324 and the receiving bucket 325 at this time will be respectively discharged during the outward discharge process of the mud water rising and sinking, Collect and collect data on the particle size in the rising muddy water flow and the sinking muddy water flow, and connect the data of the size of the muddy water particle size to the control device 334 to receive, so that the control device 334 Connected The mud water flow data is collected for comparison and analysis with the preset value. At this time, if the mud water flow condition that is rising upwards shows a large number of coarse and large particles, the control device 334 will then A control signal will be sent to the flow control member 333 to receive, so that the flow control member 333 can adjust and control the mud water input speed and flow appropriately between the stirring mechanism 31 and the separation mechanism 32, and then, The flow detecting element 331 cooperates with the transmission of detection data for the mud water flow input condition in time to facilitate the comparison with each other, so as to accurately adjust the speed of the hydraulic swirling flow suitable for the mud water feed flow into the accommodating space 322.
反之，若正監測向下沉之該泥水流況中呈現具有多數粒徑細及小之顆粒時，這時該控制裝置334便會發出一控制訊號至該流量控制件333接收，以使該流量控制件333得以控制減緩該泥水輸入該容置空間322內之速度，以針對該容置空間322內之水力漩流之速度進行適當的調整，因此藉由該等粒徑監測件332與流量偵測件331適時將所監測、偵測之數據反饋至該控制裝置334接收，以使該控制裝置334得以依據反饋接收之訊息需求，進一步改善流速與流量的調配控制，並適時增加或減緩該容置空間322內之水力漩流速度，如此一來便可大大有效且確實精準地分離出泥水中之不同顆粒粒度效果；是以，應用不同之流速偵測、監測等反饋之訊息來與預設之數值進行比對、分析，以適時針對所傳輸之狀況進行反饋改善，進而有效達到自動控制流速、流量，使得土壤顆粒粒徑之分離篩選得以於短時間內在一貫化之作業進行，不但可針對不同泥水適合進行水力漩流分離作業，對於受到重金屬污染之土壤進行分離篩選作用，更可有效將含重金屬顆粒較細之粒徑與大粒徑之土壤，以分別完全獨立篩選出，以進行後續處理，且精準有效地分離出所欲顆粒粒度效果。On the contrary, if there are many fine and small particles in the muddy water flow that is sinking, the control device 334 will send a control signal to the flow control member 333 to receive the flow control. The piece 333 can control and slow down the speed of the muddy water entering the containing space 322 to appropriately adjust the speed of the hydraulic swirling flow in the containing space 322. Therefore, the particle size monitoring pieces 332 and the flow detection The device 331 timely feeds back the monitored and detected data to the control device 334 for receiving, so that the control device 334 can further improve the flow velocity and flow allocation control according to the information demand of the feedback and receive, and increase or slow down the accommodation in time. The speed of the hydrodynamic vortex in the space 322 can effectively and accurately separate the different particle size effects of muddy water; therefore, different feedback information such as flow velocity detection and monitoring are used to preset the The values are compared and analyzed to feedback and improve the transmitted conditions in a timely manner, so as to effectively achieve automatic control of the flow rate and flow rate, so that the particle size of the soil Isolation screening can be carried out in a short period of time. It can not only be suitable for hydrocyclone separation operation for different mud waters, but also can be used for separation and screening of soil contaminated by heavy metals. Large particle size soils are completely and independently selected for subsequent processing, and the desired particle size effect is accurately and effectively separated.
歸納前述，本發明反饋式水力漩流分離系統，藉由具有反饋監控機構之設置，係有別習知僅能單一分離篩選流程之作業，其不僅利用流量偵測件及粒徑監測件的設置，以針對進行分離作業之上升之泥水流況與向下沉之泥水流況進行數據集收，且將該等泥水流況之數據連接至該控制裝置接收，並與預設值進行比對、分析，以使該反饋監控機構之控制裝置得以依據監測、偵測所得之訊息，依需求改善流速與流量，來適時增加或減緩分離機構之容置空間內之水力漩流速度，進而有效達到自動控制流速、流量，使得土壤顆粒粒徑之分離篩選得以有效於短時間內在一貫化之作業進行，且有精準地分離出不同顆粒粒度效果，故確實能達到本發明之目的。Summarizing the foregoing, the feedback type hydrodynamic swirl separation system of the present invention has a feedback monitoring mechanism, which is different from a conventional operation that can only perform a single separation and screening process, which not only uses the settings of the flow detection element and the particle size monitoring element. In order to collect data for rising mud water flow and sinking mud water flow for separation operation, and connect the data of the mud water flow to the control device to receive and compare with the preset value, Analysis, so that the control device of the feedback monitoring mechanism can improve the flow rate and flow according to the information obtained from the monitoring and detection, so as to increase or slow down the speed of the hydraulic vortex in the accommodation space of the separation mechanism in a timely manner, thereby effectively achieving automatic By controlling the flow velocity and flow rate, the separation and screening of soil particle size can be effectively carried out in a consistent operation in a short time, and the effect of accurately separating different particle sizes can be achieved.
惟以上所述者，僅為說明本發明之較佳實施例而已，當不能以此限定本發明實施之範圍，即大凡依本發明申請專利範圍及發明說明書內容所作之簡單的等效變化與修飾，皆應仍屬本發明專利涵蓋之範圍內。However, the above are only for describing the preferred embodiments of the present invention. When the scope of implementation of the present invention cannot be limited by this, that is, the simple equivalent changes and modifications made according to the scope of the patent application and the content of the invention specification of the present invention , All should still fall within the scope of the invention patent.
(習知) 1 攪拌分離裝置 11 攪拌機構 12 分離機構 111 容器 112 作動件 113 輸接管 121 錐形本體 122 容置空間 123 入口 124 集收管 125 承接斗(Knowledge) 1 Agitation and separation device 11 Agitation mechanism 12 Separation mechanism 111 Container 112 Actuator 113 Delivery tube 121 Conical body 122 Receiving space 123 Inlet 124 Collecting tube 125 Receiving bucket
3‧‧‧反饋式水力漩流分離系統 3‧‧‧Feedback hydraulic vortex separation system
31‧‧‧攪拌機構 31‧‧‧mixing mechanism
32‧‧‧分離機構 32‧‧‧ Separation agency
33‧‧‧反饋監控機構 33‧‧‧Feedback monitoring agency
311‧‧‧容器 311‧‧‧container
312‧‧‧作動件 312‧‧‧Activator
313‧‧‧輸送管 313‧‧‧conduit
321‧‧‧錐形本體 321‧‧‧conical body
322‧‧‧容置空間 322‧‧‧accommodation space
323‧‧‧入口 323‧‧‧Entrance
324‧‧‧集收管 324‧‧‧collection
325‧‧‧承接斗 325‧‧‧ Undertake bucket
331‧‧‧流量偵測件 331‧‧‧Flow detection
332‧‧‧粒徑監測件 332‧‧‧Particle size monitor
333‧‧‧流量控制件 333‧‧‧Flow Control
334‧‧‧控制裝置 334‧‧‧Control
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| TWM372209U (en) * | 2009-04-03 | 2010-01-11 | wen-liang Zheng | Stirring separation device |
| CN201431923Y (en) * | 2009-06-24 | 2010-03-31 | 中国石化集团胜利石油管理局钻井工艺研究院 | Vertical cyclone separator |
| CN102004070A (en) * | 2009-09-01 | 2011-04-06 | 杭州绿洁水务科技有限公司 | Detection system of particles in liquid |
| CN205133209U (en) * | 2015-10-12 | 2016-04-06 | 成都汉昆环保设备有限公司 | High -efficient tube settler |
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| TW201700191A (en) * | 2015-06-30 | 2017-01-01 | 中臺科技大學 | A treating method of removing heavy metals in soil grains with mobility |
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| TWM372209U (en) * | 2009-04-03 | 2010-01-11 | wen-liang Zheng | Stirring separation device |
| CN201431923Y (en) * | 2009-06-24 | 2010-03-31 | 中国石化集团胜利石油管理局钻井工艺研究院 | Vertical cyclone separator |
| CN102004070A (en) * | 2009-09-01 | 2011-04-06 | 杭州绿洁水务科技有限公司 | Detection system of particles in liquid |
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