TWM621813U - Movable solar water purifying system applying tubular membrane filter device - Google Patents

Movable solar water purifying system applying tubular membrane filter device Download PDF

Info

Publication number
TWM621813U
TWM621813U TW110209921U TW110209921U TWM621813U TW M621813 U TWM621813 U TW M621813U TW 110209921 U TW110209921 U TW 110209921U TW 110209921 U TW110209921 U TW 110209921U TW M621813 U TWM621813 U TW M621813U
Authority
TW
Taiwan
Prior art keywords
filter device
tubular membrane
water purification
water
purification system
Prior art date
Application number
TW110209921U
Other languages
Chinese (zh)
Inventor
張晏銓
顏義軒
黃祥凱
蔡志宏
曾堯宣
Original Assignee
東睿材科股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 東睿材科股份有限公司 filed Critical 東睿材科股份有限公司
Priority to TW110209921U priority Critical patent/TWM621813U/en
Publication of TWM621813U publication Critical patent/TWM621813U/en

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

A water purifying system comprises an unpurified solution tank, a purified water tank, a tubular membrane filter device, an ion exchange filter device and an active carbon filter device. The unpurified solution tank has a solution to be purified therein. The tubular membrane filter device connects to the unpurified solution tank. The active carbon filter device and the ion exchange filter device connect between the tubular membrane filter device and the purified water tank. The purified water tank has a purified water therein. The purified water is formed by filtering the solution to be purified through the tubular membrane filter device, the ion exchange filter device and the active carbon filter device.

Description

應用管式膜過濾裝置的移動式太陽能淨水系統Mobile solar water purification system using tubular membrane filtration device

本揭露是有關於一種淨水系統,特別是有關於一種應用管式膜過濾裝置的移動式太陽能淨水系統。The present disclosure relates to a water purification system, in particular, to a mobile solar water purification system using a tubular membrane filtration device.

水危機是泛指世界性的水資源相對人類需求的狀況,主要的危機來源是可用水的匱乏以及水體污染,因此如何尋找可利用的水資源及解決水體污染是各國目前亟需解決的問題之一。Water crisis generally refers to the global situation of water resources relative to human needs. The main source of crisis is the lack of available water and water pollution. Therefore, how to find available water resources and solve water pollution is one of the problems that countries need to solve urgently. one.

現有技術針對水危機的問題,目前已有針對海水淡化及過濾工業廢水等方式進行。海水是地球上數量最大的資源,包括取之不盡、用之不竭的水資源,開發和利用海水淡化技術,不僅是現代海洋開發的一項重要任務,也是未來開發新水源解決全球性水資源危機的重要途徑之一。The prior art is aimed at the problem of water crisis, such as desalination of sea water and filtration of industrial waste water. Seawater is the largest resource on earth, including inexhaustible and inexhaustible water resources. The development and utilization of seawater desalination technology is not only an important task of modern ocean development, but also the future development of new water sources to solve global water problems. One of the important ways of resource crisis.

而在工業廢水上,因傳統或科技產業的生產過程中,水源可說是工廠營運的生命線,相對於需求水量大,廢水處理後的排出水量也就相當可觀,且在生產過程中,通常會排放有機溶劑,此些溶劑不管流入河川或海洋,都會因此危害人類身體健康或影響自然生態,若能以適當的方法回收部份廢水,除可提供另一穩定的供水水源外,更可降低總廢水排放量,將能落實水資源的有效利用,而現有技術針對廢水處理此問題,多是採用薄膜法。然,薄膜法所需能源消耗大,且若薄膜受到固體微粒的積垢,往往得為了更換薄膜或其他元件而停止整個過濾系統的運作,大幅降低過濾的效率,也使成本相對提高。As for industrial wastewater, in the production process of traditional or technological industries, water source can be said to be the lifeline of factory operation. Compared with the large amount of water demanded, the amount of discharged water after wastewater treatment is also considerable, and in the production process, usually Discharge of organic solvents, whether these solvents flow into rivers or oceans, will endanger human health or affect natural ecology. If part of the wastewater can be recycled in an appropriate way, in addition to providing another stable water supply source, it can also reduce the total amount of water. The amount of wastewater discharged will enable the effective utilization of water resources, and the existing technologies mostly use the membrane method for wastewater treatment. However, the membrane method requires high energy consumption, and if the membrane is fouled by solid particles, it is often necessary to stop the operation of the entire filtration system in order to replace the membrane or other components, which greatly reduces the filtration efficiency and increases the cost.

有鑑於此,本創作之目的在於提出一種應用錯流式過濾概念的管式膜過濾裝置的淨水系統,能長時間有效進行過濾。In view of this, the purpose of this creation is to propose a water purification system of a tubular membrane filtration device using the concept of cross-flow filtration, which can effectively filter for a long time.

根據本揭露之實施例,提出一種淨水系統,其包括原液槽、淨水槽、管式膜過濾裝置、離子交換過濾裝置以及活性碳過濾裝置。原液槽具有待過濾溶液於其中。管式膜過濾裝置連通原液槽。活性碳過濾裝置與離子交換過濾裝置連通在管式膜過濾裝置與淨水槽之間。淨水槽具有待過濾溶液經管式膜過濾裝置、離子交換過濾裝置與活性碳過濾裝置過濾後所形成的淨化水於其中。According to an embodiment of the present disclosure, a water purification system is provided, which includes a raw solution tank, a water purification tank, a tubular membrane filter device, an ion exchange filter device, and an activated carbon filter device. The stock solution tank has the solution to be filtered therein. The tubular membrane filtration device communicates with the original solution tank. The activated carbon filter device and the ion exchange filter device are communicated between the tubular membrane filter device and the water purification tank. The water purification tank has the purified water formed after the solution to be filtered is filtered by the tubular membrane filter device, the ion exchange filter device and the activated carbon filter device.

為了對本揭露之上述及其他方面有更佳的瞭解,下文特舉實施例,並配合所附圖式詳細說明如下:In order to have a better understanding of the above-mentioned and other aspects of the present disclosure, the following embodiments are given and described in detail with the accompanying drawings as follows:

以下係以一些實施例做說明。須注意的是,本揭露並非顯示出所有可能的實施例,未於本揭露提出的其他實施態樣也可能可以應用。再者,圖式上的尺寸比例並非按照實際產品等比例繪製。因此,說明書和圖示內容僅作敘述實施例之用,而非作為限縮本揭露保護範圍之用。另外,實施例中之敘述,例如細部結構、製程步驟和材料應用等等,僅為舉例說明之用,並非對本揭露欲保護之範圍做限縮。實施例之步驟和結構各自細節可在不脫離本揭露之精神和範圍內根據實際應用製程之需要而加以變化與修飾。以下是以相同/類似的符號表示相同/類似的元件做說明。The following are some examples to illustrate. It should be noted that this disclosure does not show all possible embodiments, and other implementation aspects not proposed in this disclosure may also be applicable. Furthermore, the size ratios in the drawings are not drawn according to the actual product scale. Therefore, the contents of the description and illustrations are only used to describe the embodiments, rather than to limit the protection scope of the present disclosure. In addition, the descriptions in the embodiments, such as detailed structures, process steps, and material applications, etc., are for illustrative purposes only, and are not intended to limit the scope of protection of the present disclosure. The details of the steps and structures of the embodiments can be changed and modified according to the needs of the actual application process without departing from the spirit and scope of the present disclosure. In the following, the same/similar symbols are used to represent the same/similar elements for description.

請參照第1A圖與第1B圖,其分別繪示一實施例之管式膜過濾裝置110的外觀圖與透視圖。管式膜過濾裝置110包括外部套管120。外部套管120包括入水管口121、出水管口122與側壁淨水出口123。入水管口121與出水管口122分別位在外部套管120的相對端部。側壁淨水出口123在入水管口121與出水管口122之間,且較靠近入水管口121。外部套管120可以是金屬外管或是聚氯乙烯(PVC)、聚丙烯(PP)材質的塑膠外管。Please refer to FIG. 1A and FIG. 1B , which illustrate an external view and a perspective view of a tubular membrane filtration device 110 according to an embodiment, respectively. The tubular membrane filtration device 110 includes an outer sleeve 120 . The outer casing 120 includes a water inlet port 121 , a water outlet port 122 and a side wall water purification outlet 123 . The water inlet port 121 and the water outlet port 122 are respectively located at opposite ends of the outer sleeve 120 . The water purification outlet 123 of the side wall is between the water inlet pipe port 121 and the water outlet pipe port 122 , and is closer to the water inlet pipe port 121 . The outer sleeve 120 may be a metal outer tube or a plastic outer tube made of polyvinyl chloride (PVC) or polypropylene (PP).

如第1B圖所示,管式膜過濾裝置110還包括管式膜130。管式膜130設置於外部套管120內。管式膜130包含過濾薄膜層131、內層支撐管132及外層支撐管133。內層支撐管132夾設在過濾薄膜層131與外層支撐管133之間。管式膜130的內徑約為5-50毫米。管式膜130的濾孔徑可為超濾(Ultrafiltration,0.1μm~0.001μm)模組。管式膜130為高分子管式過濾膜。內層支撐管132和外層支撐管133的材料可選用PET或PP不織布,但不限於此,亦可使用任何其他具有通透性及一定強度之材料。內層支撐管132可作為強化層。過濾薄膜層131可以是高分子塗層,例如聚苯乙烯(PS)、聚乙烯(PE)、聚偏二氟乙烯(PVDF)、聚醚碸(PES)或聚四氟乙烯(PTFE)或其組合。聚四氟乙烯材質的過濾薄膜層131的氣孔孔徑介於0.01μm至10μm之間,該聚四氟乙烯孔過濾薄膜層的氣孔分布率介於10%至99%之間、聚四氟乙烯孔過濾薄膜層的薄膜厚度介於1μm至100μm之間。過濾薄膜層131的氣孔孔徑、氣孔分布率及薄膜厚度可以依據使用者所要處理的溶液(如海水、工業廢水及民生廢水)品質不同而做變化,本創作不應以此為限。As shown in FIG. 1B , the tubular membrane filtration device 110 further includes a tubular membrane 130 . The tubular membrane 130 is disposed within the outer sleeve 120 . The tubular membrane 130 includes a filter membrane layer 131 , an inner layer support tube 132 and an outer layer support tube 133 . The inner layer support tube 132 is sandwiched between the filter membrane layer 131 and the outer layer support tube 133 . The inner diameter of the tubular membrane 130 is about 5-50 mm. The pore size of the tubular membrane 130 may be an ultrafiltration (Ultrafiltration, 0.1 μm˜0.001 μm) module. The tubular membrane 130 is a polymer tubular filtration membrane. The material of the inner layer support tube 132 and the outer layer support tube 133 can be selected from PET or PP non-woven fabric, but is not limited to this, and any other material with permeability and certain strength can also be used. The inner layer support tube 132 may serve as a reinforcement layer. The filter membrane layer 131 may be a polymer coating such as polystyrene (PS), polyethylene (PE), polyvinylidene fluoride (PVDF), polyether sintered (PES) or polytetrafluoroethylene (PTFE) or its combination. The pore diameter of the filter film layer 131 made of PTFE is between 0.01 μm and 10 μm, and the pore distribution ratio of the PTFE pore filter film layer is between 10% and 99%. The film thickness of the filter film layer is between 1 μm and 100 μm. The pore diameter, pore distribution ratio and membrane thickness of the filtering membrane layer 131 can be changed according to the quality of the solution (such as seawater, industrial waste water and civil waste water) to be treated by the user, and this creation should not be limited to this.

待過濾溶液可從入水管口121進入管式膜過濾裝置110,以錯流方式進行過濾。詳細來說,管式膜過濾裝置110內的待過濾溶液沿徑方向,依序通過濾薄膜層131、內層支撐管132與外層支撐管133,形成淨化水之後,從外層支撐管133之外壁外側的側壁淨水出口123流出外部套管120。管式膜過濾裝置110內的待過濾溶液沿軸方向,穿過過具有管形狀的過濾薄膜層131定義出的管路,形成濃縮廢液,流出出水管口122。濃縮廢液不會滯留在管路中,能避免管式膜130發生堵塞。管式膜過濾裝置110以錯流方式進行過濾的優點為穩定性高且使用時間較長,且過濾薄膜層131堵塞可能性較低,不太需要反覆沖洗,流體在其內的流動狀態良好。管式膜130的內徑可為約8~12.7 mm,或8~12 mm,可處理黏度較高、固體含量較高、雜質濃度較高等的料液,使用過程中定期清洗和保養,可維持一定的通量,具有長的使用壽命,可作為多種廢水的預處理,或是較嚴苛的進料要求。管式膜過濾裝置110可進行機械式或化學式清洗再生重複使用,並可單根換膜,使用簡單、便利。管式膜過濾裝置110為複合膜結構,耐壓性高,不易損壞。The solution to be filtered can enter the tubular membrane filtration device 110 from the water inlet pipe port 121 to be filtered in a cross-flow manner. In detail, the solution to be filtered in the tubular membrane filtration device 110 passes through the filter membrane layer 131 , the inner layer support tube 132 and the outer layer support tube 133 in sequence in the radial direction to form purified water, and then flows from the outer wall of the outer layer support tube 133 to form purified water. The outer sidewall clean water outlet 123 flows out of the outer casing 120 . The solution to be filtered in the tubular membrane filtration device 110 passes through the pipeline defined by the filter membrane layer 131 having a tubular shape along the axial direction to form concentrated waste liquid, which flows out of the water outlet 122 . The concentrated waste liquid will not stay in the pipeline, which can prevent the tubular membrane 130 from clogging. The advantages of the cross-flow filtration of the tubular membrane filtration device 110 are high stability and long service time, and the filter membrane layer 131 is less likely to be blocked, and repeated flushing is not required, and the fluid flows in a good state. The inner diameter of the tubular membrane 130 can be about 8~12.7 mm, or 8~12 mm, which can handle feed liquids with high viscosity, high solid content, high impurity concentration, etc. Regular cleaning and maintenance during use can maintain With a certain flux and long service life, it can be used as the pretreatment of various wastewaters, or with stricter feed requirements. The tubular membrane filtration device 110 can be mechanically or chemically cleaned, regenerated and reused, and a single membrane can be replaced, which is simple and convenient to use. The tubular membrane filtration device 110 has a composite membrane structure, which has high pressure resistance and is not easily damaged.

第2圖繪示一實施例之淨水系統。淨水系統包括管式膜過濾裝置110、原液槽200、淨水槽300、離子交換過濾裝置400與活性碳過濾裝置500。FIG. 2 shows a water purification system according to an embodiment. The water purification system includes a tubular membrane filter device 110 , a raw solution tank 200 , a water purification tank 300 , an ion exchange filter device 400 and an activated carbon filter device 500 .

管式膜過濾裝置110藉由輸送管612、輸送管622連通在原液槽200與離子交換過濾裝置400之間。其中,輸送管612連接在管式膜過濾裝置110的入水管口121與原液槽200之間。輸送管622連接在管式膜過濾裝置110的出水管口122與原液槽200之間。輸送管614連接在管式膜過濾裝置110的側壁淨水出口123與離子交換過濾裝置400之間。管式膜過濾裝置110的數量不限於一個,也可使用多數個管式膜過濾裝置110,以並聯方式或串聯方式連接,構成模組結構,可有效提升待過濾溶液的過濾效果。The tubular membrane filtration device 110 is communicated between the raw solution tank 200 and the ion exchange filtration device 400 through the conveying pipe 612 and the conveying pipe 622 . Wherein, the conveying pipe 612 is connected between the water inlet pipe port 121 of the tubular membrane filtration device 110 and the raw solution tank 200 . The conveying pipe 622 is connected between the water outlet port 122 of the tubular membrane filtration device 110 and the raw solution tank 200 . The conveying pipe 614 is connected between the water purification outlet 123 of the side wall of the tubular membrane filter device 110 and the ion exchange filter device 400 . The number of tubular membrane filtration devices 110 is not limited to one, and a plurality of tubular membrane filtration devices 110 can also be used and connected in parallel or in series to form a module structure, which can effectively improve the filtering effect of the solution to be filtered.

活性碳過濾裝置500藉由輸送管645連通在離子交換過濾裝置400與淨水槽300之間。其它實施例中,離子交換過濾裝置400藉由輸送管連通在活性碳過濾裝置500與淨水槽300之間。The activated carbon filter device 500 is communicated between the ion exchange filter device 400 and the water purification tank 300 through the conveying pipe 645 . In other embodiments, the ion exchange filter device 400 is communicated between the activated carbon filter device 500 and the water purification tank 300 through a conveying pipe.

加壓幫浦712設置在輸送管612上。加壓幫浦735設置在輸送管635上。太陽能模組800電性連接加壓幫浦712與加壓幫浦735,用以控制供電至加壓幫浦推動流體,達到綠能省電效果。太陽能模組800包括太陽能板810及電池與電源管理系統820。電池與電源管理系統820耦接在加壓幫浦712與太陽能板810之間,並耦接在加壓幫浦735與太陽能板810之間。電池與電源管理系統820可包括電性耦接的儲能模組與電源控制器。電源控制器可電性連接在太陽能板810與加壓幫浦之間。實施例中,由太陽能模組800供電的加壓幫浦亦可設置在其它輸送管上。輸送管上可設置水流計。The pressurized pump 712 is provided on the delivery tube 612 . The pressurization pump 735 is provided on the delivery pipe 635 . The solar module 800 is electrically connected to the pressurized pump 712 and the pressurized pump 735 to control the power supply to the pressurized pump to push the fluid, so as to achieve the effect of green energy and power saving. The solar module 800 includes a solar panel 810 and a battery and power management system 820 . The battery and power management system 820 is coupled between the pressurized pump 712 and the solar panel 810 , and between the pressurized pump 735 and the solar panel 810 . The battery and power management system 820 may include an energy storage module and a power controller that are electrically coupled. The power controller can be electrically connected between the solar panel 810 and the pressurized pump. In the embodiment, the pressurized pump powered by the solar module 800 can also be arranged on other conveying pipes. A water flow meter can be set on the delivery pipe.

實施例中,原液槽200具有待過濾溶液於其中。原液槽200中的待過濾溶液在經過管式膜過濾裝置110、離子交換過濾裝置400與活性碳過濾裝置500過濾之後形成淨化水進入淨水槽300中。In an embodiment, the raw solution tank 200 has the solution to be filtered therein. The solution to be filtered in the raw solution tank 200 is filtered by the tubular membrane filter device 110 , the ion exchange filter device 400 and the activated carbon filter device 500 to form purified water and enter the water purification tank 300 .

待過濾溶液可為果汁、海水、河水、工業廢水、民生廢水、化學濃縮液、高揮發性溶液(VOC)、染整廢水、電鍍廢水、電泳漆等,該溶液也可以是經過管式膜過濾裝置110過濾後的濃縮廢液,進行循環過濾以提高廢水的回收率。The solution to be filtered can be fruit juice, seawater, river water, industrial wastewater, livelihood wastewater, chemical concentrate, highly volatile solution (VOC), dyeing and finishing wastewater, electroplating wastewater, electrophoretic paint, etc. The solution can also be filtered through tubular membranes The concentrated waste liquid filtered by the device 110 is subjected to circulating filtration to improve the recovery rate of the waste water.

第3圖繪示另一實施例之淨水系統,其與第2圖的淨水系統之間的差異說明如下。淨水系統可使用如第4A圖與第4B圖所示的管式膜過濾裝置150。管式膜過濾裝置150與第1A圖與第1B圖的管式膜過濾裝置110之間的差異在於,管式膜過濾裝置150的外部套管160更包括側壁廢液出口164。側壁廢液出口164在入水管口121與出水管口122之間,且較靠近出水管口122。管式膜過濾裝置150中的濃縮廢液也可經由靠近出水管口122的側壁廢液出口164流出外部套管160,經過輸送管624後至原液槽200中,如第3圖所示,輸送管615連接在管式膜過濾裝置150的側壁淨水出口123與活性碳過濾裝置500之間。離子交換過濾裝置400藉由輸送管645與輸送管634連通在活性碳過濾裝置500與淨水槽300之間。加壓幫浦735設置在輸送管634上。其它實施例中,活性碳過濾裝置500藉由輸送管連通在離子交換過濾裝置400與淨水槽300之間。FIG. 3 shows a water purification system of another embodiment, and the difference between it and the water purification system of FIG. 2 is explained as follows. The water purification system can use the tubular membrane filtration device 150 shown in FIGS. 4A and 4B . The difference between the tubular membrane filtration device 150 and the tubular membrane filtration device 110 of FIGS. 1A and 1B is that the outer sleeve 160 of the tubular membrane filtration device 150 further includes a sidewall waste outlet 164 . The sidewall waste liquid outlet 164 is located between the water inlet pipe port 121 and the water outlet pipe port 122 , and is closer to the water outlet pipe port 122 . The concentrated waste liquid in the tubular membrane filtration device 150 can also flow out of the external casing 160 through the side wall waste liquid outlet 164 close to the water outlet pipe 122, and then pass through the conveying pipe 624 to the raw liquid tank 200, as shown in FIG. The pipe 615 is connected between the water purification outlet 123 of the side wall of the tubular membrane filter device 150 and the activated carbon filter device 500 . The ion exchange filter device 400 communicates between the activated carbon filter device 500 and the water purification tank 300 through the transfer pipe 645 and the transfer pipe 634 . A pressurized pump 735 is provided on the delivery tube 634 . In other embodiments, the activated carbon filter device 500 is communicated between the ion exchange filter device 400 and the water purification tank 300 through a conveying pipe.

一實施例中,舉例來說,原液槽200中的待過濾溶液為高含沙量的河川/池塘水。輸送管612中的待過濾溶液經管式膜過濾裝置150過濾後,形成低含沙量的溶液至輸送管615中。輸送管615 中的溶液流至活性碳過濾裝置500過濾後形成低毒素的溶液,其經離子交換過濾裝置400過濾之後形成潔淨的淨化水,可作為民生用水或供飲用。In one embodiment, for example, the solution to be filtered in the raw solution tank 200 is river/pond water with high sand content. After the solution to be filtered in the conveying pipe 612 is filtered by the tubular membrane filtration device 150 , a solution with low sand content is formed into the conveying pipe 615 . The solution in the delivery pipe 615 flows to the activated carbon filter device 500 to be filtered to form a low-toxic solution, which is filtered by the ion exchange filter device 400 to form clean purified water, which can be used as water for people's livelihood or for drinking.

第5圖繪示實施例之淨水系統,其包括可移動式載體900,具有滾輪910設置在基板920的底下。參照第1圖或第3圖說明的系統裝置可設置在可移動式載體900上,從而形成移動式淨水系統,方便移動,機動性高。FIG. 5 shows the water purification system of the embodiment, which includes a movable carrier 900 with rollers 910 disposed under the base plate 920 . The system device described with reference to FIG. 1 or FIG. 3 can be installed on the movable carrier 900 to form a mobile water purification system, which is convenient to move and has high mobility.

綜上所述,雖然本揭露已以實施例揭露如上,然其並非用以限定本創作。本揭露所屬技術領域中具有通常知識者,在不脫離本揭露之精神和範圍內,當可作各種之更動與潤飾。因此,本揭露之保護範圍當視後附之申請專利範圍所界定者為準。To sum up, although the present disclosure has been disclosed above with embodiments, it is not intended to limit the present invention. Those with ordinary knowledge in the technical field to which the present disclosure pertains can make various changes and modifications without departing from the spirit and scope of the present disclosure. Therefore, the scope of protection of the present disclosure should be determined by the scope of the appended patent application.

110:管式膜過濾裝置 120:外部套管 121:入水管口 122:出水管口 123:側壁淨水出口 130:管式膜 131:過濾薄膜層 132:內層支撐管 133:外層支撐管 150:管式膜過濾裝置 160:外部套管 164:側壁廢液出口 200:原液槽 300:淨水槽 400:離子交換過濾裝置 500:活性碳過濾裝置 612, 614, 615, 622, 624, 634, 635, 645:輸送管 712, 735:加壓幫浦 800:太陽能模組 810:太陽能板 820:電池與電源管理系統 900:可移動式載體 910:滾輪 920:基板110: Tubular membrane filtration device 120: Outer casing 121: water inlet 122: outlet pipe 123: Sidewall water purification outlet 130: Tubular membrane 131: filter membrane layer 132: inner support tube 133: Outer support tube 150: Tubular membrane filtration device 160: Outer casing 164: Sidewall waste liquid outlet 200: stock solution tank 300: water purification tank 400: Ion exchange filter device 500: Activated carbon filter device 612, 614, 615, 622, 624, 634, 635, 645: Delivery pipes 712, 735: Pressurized Pump 800: Solar Module 810: Solar Panels 820: Battery and Power Management Systems 900: Removable Carrier 910: Roller 920: Substrate

第1A圖繪示一實施例之管式膜過濾裝置的外觀圖。 第1B圖繪示一實施例之管式膜過濾裝置的透視圖。 第2圖繪示一實施例之淨水系統。 第3圖繪示另一實施例之淨水系統。 第4A圖繪示一實施例之管式膜過濾裝置的外觀圖。 第4B圖繪示一實施例之管式膜過濾裝置的透視圖。 第5圖繪示實施例之淨水系統。 FIG. 1A shows an external view of a tubular membrane filtration device according to an embodiment. FIG. 1B shows a perspective view of a tubular membrane filtration device according to an embodiment. FIG. 2 shows a water purification system according to an embodiment. FIG. 3 shows another embodiment of a water purification system. FIG. 4A shows an external view of a tubular membrane filtration device according to an embodiment. FIG. 4B shows a perspective view of a tubular membrane filtration device according to an embodiment. Fig. 5 shows the water purification system of the embodiment.

110:管式膜過濾裝置 110: Tubular membrane filtration device

120:外部套管 120: Outer casing

121:入水管口 121: water inlet

122:出水管口 122: outlet pipe

123:側壁淨水出口 123: Sidewall water purification outlet

130:管式膜 130: Tubular membrane

200:原液槽 200: stock solution tank

300:淨水槽 300: water purification tank

400:離子交換過濾裝置 400: Ion exchange filter device

500:活性碳過濾裝置 500: Activated carbon filter device

612,614,622,635,645:輸送管 612, 614, 622, 635, 645: Delivery pipes

712,735:加壓幫浦 712,735: Pressurized pump

800:太陽能模組 800: Solar Module

810:太陽能板 810: Solar Panels

820:電池與電源管理系統 820: Battery and Power Management Systems

Claims (10)

一種淨水系統,包括: 一原液槽,具有一待過濾溶液於其中; 一淨水槽; 一管式膜過濾裝置,連通該原液槽; 一離子交換過濾裝置;以及 一活性碳過濾裝置,與該離子交換過濾裝置連通在該管式膜過濾裝置與該淨水槽之間,其中該淨水槽具有該待過濾溶液經該管式膜過濾裝置、該離子交換過濾裝置與該活性碳過濾裝置過濾後所形成的一淨化水於其中。 A water purification system comprising: a stock solution tank with a solution to be filtered therein; a clean sink; a tubular membrane filtration device, communicated with the raw solution tank; an ion exchange filter device; and An activated carbon filter device communicated with the ion exchange filter device between the tubular membrane filter device and the water purification tank, wherein the water purification tank has the solution to be filtered through the tubular membrane filter device, the ion exchange filter device and the A purified water formed after filtering by the activated carbon filter device is contained therein. 如請求項1所述的淨水系統,更包括數個輸送管,分別連接在該原液槽、該淨水槽、該離子交換過濾裝置、該管式膜過濾裝置與該活性碳過濾裝置其中二者之間。The water purification system according to claim 1, further comprising a plurality of conveying pipes, respectively connected to two of the raw solution tank, the water purification tank, the ion exchange filter device, the tubular membrane filter device and the activated carbon filter device between. 如請求項2所述的淨水系統,更包括至少一加壓幫浦,分別設置在該些輸送管其中之一上。The water purification system according to claim 2, further comprising at least one pressurized pump, respectively disposed on one of the conveying pipes. 如請求項3所述的淨水系統,更包括一太陽能模組,電性連接該至少一加壓幫浦。The water purification system according to claim 3, further comprising a solar module electrically connected to the at least one pressurized pump. 如請求項4所述的淨水系統,其中該太陽能模組包括: 一太陽能板;以及 一電池與電源管理系統,耦接在該至少一加壓幫浦與該太陽能板間。 The water purification system of claim 4, wherein the solar module comprises: a solar panel; and A battery and power management system is coupled between the at least one pressurized pump and the solar panel. 如請求項2所述的淨水系統,更包括: 一加壓幫浦,設置在該些輸送管其中之一個輸送管上,該一個輸送管連接在該原液槽與該管式膜過濾裝置之間;以及 另一加壓幫浦,設置在該些輸送管其中之另一個輸送管上,該另一個輸送管連接在該活性碳過濾裝置及該離子交換過濾裝置其中之一與該淨水槽之間。 The water purification system according to claim 2, further comprising: a pressurized pump, disposed on one of the conveying pipes, and the one conveying pipe is connected between the raw solution tank and the tubular membrane filtration device; and Another pressurized pump is arranged on the other one of the conveying pipes, and the other conveying pipe is connected between one of the activated carbon filter device and the ion exchange filter device and the water purification tank. 如請求項1所述的淨水系統,更包括一可移動式載體,其中該原液槽、該淨水槽、該離子交換過濾裝置、該管式膜過濾裝置與該活性碳過濾裝置設置在該可移動式載體上。The water purification system according to claim 1, further comprising a movable carrier, wherein the raw solution tank, the water purification tank, the ion exchange filter device, the tubular membrane filter device and the activated carbon filter device are arranged in the movable carrier. on a mobile carrier. 如請求項1所述的淨水系統,其中該管式膜過濾裝置包括: 一外部套管;以及 一管式膜,設置於該外部套管內,該管式膜包含: 一過濾薄膜層; 一外層支撐管;以及 一內層支撐管,作為強化層,並夾設在該過濾薄膜層與該外層支撐管之間,該管式膜可經清洗再生而重複使用。 The water purification system of claim 1, wherein the tubular membrane filtration device comprises: an outer sleeve; and A tubular membrane disposed within the outer sleeve, the tubular membrane comprising: a filter membrane layer; an outer support tube; and An inner layer support tube, as a strengthening layer, is sandwiched between the filter membrane layer and the outer layer support tube, and the tubular membrane can be reused after cleaning and regeneration. 如請求項8所述的淨水系統,其中該外部套管包括: 一入水管口; 一出水管口,相對於該入水管口;以及 一側壁淨水出口,在該入水管口與該出水管口之間,該待過濾溶液從該入水管口進入該管式膜過濾裝置,以錯流方式進行過濾形成淨化水與濃縮廢液,該淨化水從該側壁淨水出口流出該外部套管,該濃縮廢液流出該出水管口,從而降低該管式膜的堵塞可能性。 The water purification system of claim 8, wherein the outer casing comprises: a water inlet; an outlet opening, relative to the inlet opening; and A water purification outlet on the side wall, between the water inlet nozzle and the water outlet nozzle, the solution to be filtered enters the tubular membrane filtration device from the water inlet nozzle, and is filtered in a cross-flow manner to form purified water and concentrated waste liquid, The purified water flows out of the outer casing from the side wall water outlet, and the concentrated waste liquid flows out of the water outlet, thereby reducing the possibility of clogging of the tubular membrane. 如請求項9所述的淨水系統,其中該外部套管更包括一側壁廢液出口,鄰近該出水管口,其中該側壁淨水出口鄰近該入水管口,以該錯流方式進行過濾形成的該濃縮廢液流出該側壁廢液出口,從而降低該管式膜的堵塞可能性。The water purification system according to claim 9, wherein the outer casing further comprises a sidewall waste liquid outlet adjacent to the water outlet, wherein the sidewall water purification outlet is adjacent to the water inlet, and is filtered in the cross-flow manner to form The concentrated waste liquid flows out of the side wall waste liquid outlet, thereby reducing the possibility of clogging of the tubular membrane.
TW110209921U 2021-08-23 2021-08-23 Movable solar water purifying system applying tubular membrane filter device TWM621813U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW110209921U TWM621813U (en) 2021-08-23 2021-08-23 Movable solar water purifying system applying tubular membrane filter device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW110209921U TWM621813U (en) 2021-08-23 2021-08-23 Movable solar water purifying system applying tubular membrane filter device

Publications (1)

Publication Number Publication Date
TWM621813U true TWM621813U (en) 2022-01-01

Family

ID=80785386

Family Applications (1)

Application Number Title Priority Date Filing Date
TW110209921U TWM621813U (en) 2021-08-23 2021-08-23 Movable solar water purifying system applying tubular membrane filter device

Country Status (1)

Country Link
TW (1) TWM621813U (en)

Similar Documents

Publication Publication Date Title
CN202152294U (en) Electro-adsorption desalting plant for high-salinity waste water
CN102674590A (en) Method for treating and recycling heavy metal wastewater by double-membrane process
CN202430070U (en) Heavy metal wastewater treatment and recycling equipment using two-membrane process
CN105293787B (en) A kind of cold rolling alkalescence waste discharge advanced treatment recycling technique system and method
CN113023880A (en) Aeration device of MBR (membrane bioreactor)
CN101767890A (en) Method applying membrane combining process to dispose garbage percolate
TWM621813U (en) Movable solar water purifying system applying tubular membrane filter device
CN106007040A (en) Heavy metal wastewater treatment system and method
CN207567042U (en) A kind of ultra-pure-water treatment system
KR101031673B1 (en) Stacked membrane filtration system and stacking method thereof
CN207546236U (en) A kind of sewage-treatment plant for improving membrane filtration system performance
CN202046959U (en) Reclaimed water reusing equipment
CN104529087A (en) Complete equipment and technology for reutilization and energy regeneration treatment of wastewater
CN205419859U (en) Sand filtration backwash pretreatment of water system
JP2011041907A (en) Water treatment system
CN208949028U (en) A kind of processing system of coal mine drainage water
CN110950457A (en) Advanced treatment device for mine water micro-pollutants
TWI745642B (en) Filteration system with tubular membrane and the operating method thereof
CN206103720U (en) A ultrafiltration system for leachate treatment
CN102219321B (en) Recycled water recycling equipment and process
CN209759170U (en) Tubular membrane filtration system
CN205222890U (en) Deep purifying device for micro contaminated water source
CN201380045Y (en) Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water
CN110314552A (en) A kind of stacked ultra-filtration membrane device
CN215828441U (en) Aeration device of MBR (membrane bioreactor)