WO2014117303A1 - 可移动一体化超滤膜饮用水生产机 - Google Patents

可移动一体化超滤膜饮用水生产机 Download PDF

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Publication number
WO2014117303A1
WO2014117303A1 PCT/CN2013/000332 CN2013000332W WO2014117303A1 WO 2014117303 A1 WO2014117303 A1 WO 2014117303A1 CN 2013000332 W CN2013000332 W CN 2013000332W WO 2014117303 A1 WO2014117303 A1 WO 2014117303A1
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WIPO (PCT)
Prior art keywords
pump
water
ultrafiltration membrane
tank
drinking water
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PCT/CN2013/000332
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English (en)
French (fr)
Inventor
刘朝南
Original Assignee
Liu Chaonan
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Publication date
Application filed by Liu Chaonan filed Critical Liu Chaonan
Publication of WO2014117303A1 publication Critical patent/WO2014117303A1/zh

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20—Controlling water pollution; Waste water treatment
    • Y02A20/208—Off-grid powered water treatment

Definitions

  • the utility model belongs to a water supply device in a water treatment system, in particular to a movable mobile ultrafiltration membrane drinking water production machine, which is applied to the water source of rural, agricultural and small and medium-sized enterprises for ozone treatment.
  • B ij , W has developed very maturely in the water treatment industry. From flocculation to ion exchange, membrane filtration and distillation, electronic processing, reverse osmosis and so on, it is also very effective.
  • the volume is large and the area is large;
  • the water treatment equipment is targeted: 1-, singleness; such as membrane filtration can achieve sterile drinking water, but for rural natural water It is not suitable, it needs to deal with deep sucking, etc.;
  • Second, the water source is not cleaned by ozone.
  • the pool is easy to produce dirt and bacteria pollution; Fourth, it is mostly fixed and non-movable, there is no whole machine product.
  • the utility model aims to provide a mobile-body ultrafiltration membrane drinking buffalo production machine with simple structure, convenient movement, ozone treatment, water sterilizing and water quality safety.
  • the technical solution adopted by the utility model to solve the technical problem is as follows: It comprises a cabinet and a pulley, and the two sides of the cabinet are respectively provided with a micro vortex flocculation reaction tank and a sterile pool, and the characteristics are: the micro vortex flocculation reaction
  • the self-cleaning filter, the water supply pump, the ultrafiltration membrane device and the ozone generator are connected by a water pipe between the pool and the toothless pool.
  • the ultrafiltration membrane device is connected to the cleaning liquid tank and the cleaning pump on one side, and the backwashing filter and the backwashing pump are connected to the other side, and the backwashing pump is connected to the aseptic pool.
  • a user water supply pipe is connected below the aseptic water tank, and the user water supply pipe is provided with a frequency conversion water supply pump.
  • the top of the cabinet is provided with a ventilating fan.
  • the side of the micro vortex flocculation reaction tank is connected to a mixer and a source water pump.
  • a metering pump is connected to the mixer, and the metering pump is connected to the solution tank.
  • the new benefits of this utility are: - It is small footprint, movable, easy to operate, and installed once in use; Second, the water source is not easily soiled after the ozone treatment, the water quality ensures sterility; Flocculation to the ultrafiltration membrane has an automatic cleaning system, which is safe and reliable. Fourth, there is no need to add disinfection equipment, no need to add chlorinated fungicide, avoiding the formation of various carcinogens such as chloroform in water; V. The emergency function is good, especially the nj is used for flooding and sudden pollution events.
  • Figure 1 is a small appearance of the utility model
  • Figure 2 is a schematic view of the internal ⁇ face structure of the cabinet of Figure 1;
  • Figure 3 is a small intent of the A- ⁇ structure in Figure 2;
  • Figure 4 is a schematic view of the structure B B of Figure 2;
  • Figure 5 is a schematic view showing the structure of C C in Figure 2;
  • Figure 6 shows the D-D structure in Figure 2
  • Figure 8 is a schematic view of the F-F structure of Figure 2;
  • FIG. 1 Micro-vortex flocculation reaction tank, 2. Water supply pump, 3. Drainage pipe, 4. Air-disintegration, 5. Backflushing pipe, 6. Ultrafiltration membrane device, 7. Aseptic pool, 8. Mixer, 9. Metering pump, 10. Washing pump control cabinet, 1 1. Pump control cabinet, 12. Cleaning tank, 13. Washing pump, 14. Backwashing filter, 15. Backwashing pump, 16. Power cabinet 17. Ultrafiltration membrane device control cabinet, 18. Recoil pump control cabinet, 19. Frequency conversion water supply pump control cabinet, 20. User water supply pipe, 21. Frequency conversion water supply pump, 22. Source water pump, 23. Self-cleaning filter, 24. Solution tank, 25. Water level control valve, 26. Pulley, 27. Cabinet, 28. Ozone generator.
  • the movable integrated ultrafiltration membrane drinking water production machine includes a cabinet 27 and a pulley 26, and the inside of the cabinet 27 is respectively A micro vortex flocculation reaction tank 1 and a sterile water tank 7 are provided.
  • the micro vortex flocculation reaction tank 1 and the aseptic water tank 7 are connected to the ultrafiltration membrane device 6 through a water pipe, and the water pipe between the ultrafiltration membrane device 6 and the micro vortex flocculation reaction tank 1 is connected to the self-cleaning filter 23 and the water supply pump. 2; an ozone generator 28 is disposed between the ultrafiltration membrane device 6 and the aseptic pool 7.
  • a water level control valve 25 is disposed in the aseptic pool 7, and the water level control valve 25 controls the opening or closing of the water pump 22. When the water of the aseptic pool 7 is full, the signal is reflected to the water pump 22 through the water level control valve 25.
  • a user water supply pipe 20 is connected below the aseptic water tank 7, and the user water supply pipe 20 is provided with a variable frequency water supply pump 21.
  • the micro vortex flocculation reaction tank 1 is provided with a solution tank 24 on the side, and the solution tank 24 is connected to the mixer 8 , and the water pump 22 is arranged on the inlet pipe and communicates with the micro vortex flocculation reaction tank 1 via the mixer 8 .
  • a metering pump 9 is disposed on the conduit to facilitate metering of the amount of liquid medicine output from the solution tank 24.
  • the power supply cabinet 16 controls the total power supply; the cleaning pump control cabinet 10 controls the cleaning liquid tank 12; the ultrafiltration membrane device control cabinet 17 controls the activation or shutdown of the ultrafiltration membrane device 6; the recoil pump control cabinet 18 controls the reverse The startup or shutdown of the flushing pump 15; the variable frequency water supply pump control cabinet 19 effectively controls the startup or shutdown of the variable frequency water supply pump 21; the water pump control cabinet 11 controls the source water pump 22 to be turned on or off.
  • the water to be treated from the water pump 22 into the mixer 8 and the solution tank 24 is discharged through the conduit in the mixer 8 After the combination, the micro vortex flocculation reaction tank 1 is introduced to carry out flocculation reaction.
  • the water pump control cabinet 11 realizes the control of the water supply pump 2, and the effluent of the micro vortex flocculation reaction tank 1 is sent to the A cleaning filter 23, because the pumping water pressure causes the water flow to rapidly swirl, the flocculant encapsulates the naked impurities, the organic matter Both are sent to the bottom of the self-cleaning filter 23 and discharged through the drain pipe 3 to achieve the first-stage filtration.
  • the water source is pressurized by the water supply pump 2 and then enters the ultrafiltration membrane device 6 for fine filtration.
  • the ozone generator 28 emits ozone. The ozone enters the ultrafiltration membrane device 6 and is finely filtered to achieve the second filtration.
  • the leeches are sterilized and then flowed into the aseptic tank 7 to ensure that the water quality is completely nj to achieve sterile water standards.
  • the variable frequency water supply pump 21 can well adjust the water supply pressure, ensure the completion of the water supply system operation, and realize automatic water supply and water supply.
  • the ventilating fan 4 realizes the string 27 of the cabinet. It exchanges with the outside air, and plays the role of exchanging air and cooling the whole device in the cabinet 23.
  • the cleaning liquid tank 12 pumps the chemical cleaning liquid to the ultrafiltration membrane unit 6 through the cleaning pump 13, and is used for chemical cleaning of the ultrafiltration membrane unit 6.
  • the ultrafiltration membrane unit 6 is connected to the backwash filter 14 and the backwash pump 15 via a conduit and connected to the aseptic tank 7 to constitute a backwash cycle. Due to the secondary filtration of the ultrafiltration membrane device 6, a very small amount of impurities are deposited on the backwash filter 14, and the backwash pump 15 is started to flush the aseptic pool 7 and the water is pumped back through the backwash filter 14 to achieve backwashing from the backflushing drain 5 excluded.

Abstract

可移动一体化超滤膜饮用水生产机，它包括箱柜（27）、滑轮（26），箱柜（27）内两侧分别设有微涡流絮凝反应池（1）和无菌水池（7），其特征是：微涡流絮凝反应池（1）和无菌水池（7）之间通过水管连接自清洗过滤器（23）、供水泵（2）、超滤膜装置（6）和臭氧发生器（28）；超滤膜装置（6）—侧连接清洗液箱（12）和清洗泵（13），另一侧连接反冲洗过滤器（14）、反冲洗泵（15），反冲洗泵（15）与无菌水池（7）连接。该饮用水生产机占地面积小、移动操作简便、安装使用一次到位；水源经过净化臭氧处理后水池中的水确保无菌；无需添加消毒设备，无需添加氯化杀菌剂，避免水中生成三氯甲垸等多种致癌物质。

Description

可移动一体化超滤膜饮用水生产机 所属技术领域
本实用新型属于水处理系统中的供水设备 ,具体地讲是涉及 - -种可移动 休化超滤膜饮川水生产机， 应用于农村、 农业、 中小企业的水源进行净化 臭氧处理。
背景技术
B ij , W内外在水处理行业已经发展得很成熟。 从絮凝沉降到离子交换、 膜过滤以及蒸馏、 电子处理、 反渗透等琳琅满目， 而且也确是很有效果。 但 是普遍存在四大缺点： 一是体积大、 占地大； 二是水处理设备是以针对性为 :1- , 单一性多； 如膜过滤能达到无菌饮用水， 但是对于农村的天然水就不适 应， 需要前处理深沉吸咐等； 二是水源没有经过净化臭氧处理水池容易产生 污垢和细菌污染； 四是多为固定式不可移动， 没有整机产品。
发明内容
为了克服以上技术存在的不足， 本实用新型的目的在于提供一种结构简 单、 移动方便、 臭氧处理， 出水无菌、 水质安全的可移动 -体化超滤膜饮用 水牛.产机。
本实用新型解决技术问题所采用的技术方案是： 它包括箱柜、 滑轮， 所 述箱柜内两侧分别设有微涡流絮凝反应池和无菌水池， 其特征是： 所述微涡 流絮凝反应池和无齒水池之间通过水管连接自清洗过滤器、 供水泵、 超滤膜 装置和臭氧发生器。
所述超滤膜装置一侧连接清洗液箱和清洗泵， 另一侧连接反冲洗过滤器、 反冲洗泵， 所述反冲洗泵与无菌水池连接。 所述无菌水池下方连接用户给水管， 所述用户给水管设有变频供水泵。 所述箱柜的顶端设有换气扇。
所述微涡流絮凝反应池侧面连接混合器、 源水泵。
所述混合器上连接计量泵， 所述计量泵与溶液箱连接。
本实用新 的冇益效果是： -是占地面积小、 可移动使用、 操作简便、 安装使用一次到位； 二是水源经过净化臭氧处理后水池不容易产生污垢， 水 质确保无菌； 三是从絮凝到超滤膜都有自动清洗系统， 安全可靠； 四是无需 添加消毒设备， 无需添加氯化杀菌剂， 避免水中生成三氯甲烷等多种致癌物 质； 五是对源水水质突变的 /、V.急功能好， 尤其是 nj用于洪涝、 突发污染事件。 附图说明
下面结合附图和实施例对本实用新型进一步说明。
图 1是本实用新型的外观结构小 ·意图；
图 2是图 1中箱柜的内部 Τ·面结构不意图；
图 3是图 2中 A- Α结构小意图；
图 4是图 2中 B B结构示意图；
图 5是图 2中 C C结构示意图；
图 6足图 2中 D-D结构 意图；
阁 7是图 2中 E-E结构示意图；
图 8是图 2中 F-F结构示意图；
图屮所 ： 1.微涡流絮凝反应池， 2.供水泵， 3.排污管， 4.换气崩， 5. 反冲排水管， 6.超滤膜装置， 7.无菌水池， 8.混合器， 9.计量泵， 10.清洗泵 控制柜， 1 1.水泵控制柜， 12.清洗液箱， 13.清洗泵， 14.反冲洗过滤器， 15. 反冲洗泵， 16.电源柜， 17.超滤膜装置控制柜， 18.反冲泵控制柜， 19.变频 供水泵控制柜， 20.用户给水管， 21.变频供水泵， 22.源水泵， 23.自清洗过 滤器， 24.溶液箱， 25.水位控制阀， 26.滑轮， 27.箱柜， 28.臭氧发生器。 具体实施方式 如图 1、 2、 3、 4、 5、 6、 7和 8所示， 可移动一体化超滤膜饮用水生产 机， 它包括箱柜 27、 滑轮 26， 所述箱柜 27内两侧分别设有微涡流絮凝反应 池 1和无菌水池 7。所述微涡流絮凝反应池 1和无菌水池 7之间通过水管连接 超滤膜装置 6，超滤膜装置 6和微涡流絮凝反应池 1之间的水管上连接自清洗 过滤器 23、 供水泵 2 ; 所述超滤膜装置 6和无菌水池 7之间设有臭氧发生器 28。所述超滤膜装置 6—侧连接清洗液箱 12和清洗泵 13， 另一侧连接反冲洗 过滤器 14、 反冲洗泵 15， 所述反冲洗泵 15与无菌水池 7连接， 反冲洗过滤 器 M和反冲洗泵 15构成反冲洗循环装置。 所述无菌水池 7下方连接用户给 水管 20， 所述用户给水管 20设有变频供水泵 21。 所述箱柜 27的顶端设有换 气扇 4。所述微涡流絮凝反应池 1侧面连接混合器 8、 源水泵 22。 所述混合器 8 卜.连接计量泵 9， 所述计量泵 9与溶液箱连接 24。所述无菌水池 7内设有一 个水位控制阀 25， 由水位控制阀 25控制水泵 22的开启或关闭， 当无菌水池 7的水满时， 通过水位控制阀 25信号反射到水泵 22， 实现水泵控制柜 1 1 电 源断幵， 停止抽水。 所述无菌水池 7下方连接用户给水管 20， 所述用户给水 管 20上设有变频供水泵 21。 所述微涡流絮凝反应池 1 ，侧设有溶液箱 24， 溶液箱 24导管连接于混合器 8上， 进水管上设有水泵 22并连通混合器 8与 微涡流絮凝反应池 1相通。 所述导管上设有计量泵 9， 便于计量从溶液箱 24 输出药液量。
如图 2所小， 电源柜 16控制总电源； 清洗泵控制柜 10控制清洗液箱 12 ; 超滤膜装置控制柜 17控制超滤膜装置 6的启动或关闭； 反冲泵控制柜 18控 制反冲洗泵 15的启动或关闭； 变频供水泵控制柜 19有效控制变频供水泵 21 的启动或关闭； 水泵控制柜 11控制源水泵 22开启或关闭。 需要处理的水源 从水泵 22进入到混合器 8与溶液箱 24内的药液经导管流出在混合器 8里混 合后进入微涡流絮凝反应池 1进行絮凝反应。 提水泵控制柜 11实现控制供水 泵 2丌启， 微涡流絮凝反应池 1的出水送到 A清洗过滤器 23中， 由于泵送水 压促使水流迅速旋流， 被絮凝剂包裸的杂质， 有机质都被送到自清洗过滤器 23的底部经排污管 3排出， 实现第- -次过滤。 第一次过滤后的水源经过供水 泵 2提压后进入超滤膜装置 6进行精滤， 臭氧发生器 28发牛.的臭氧进入超滤 膜装置 6精滤实现第二次过滤， 精滤后的水屮进行杀菌， 然后流入无菌水池 7 确保水质完全 nj以达到无菌水标准。 通过用户给水管 20输送到用户， 变频供 水泵 21可以很好的调节供水压力， 确保供水系统作业完成， 实现全自动制水 及供水。 换气扇 4实现箱柜 27串.与外界的空气交换， 对箱柜 23内整个装置 工作时候起到交换空气和降温的作用。 使用后， 清洗液箱 12 通过清洗泵 13 将化学清洗液泵到超滤膜装置 6， 史好的用于对超滤膜装置 6进行化学清洗。
为丫延长超滤膜装置 6的使用寿命， 超滤膜装置 6通过导管连接反冲洗 过滤器 14和反冲洗泵 15并连接到无菌水池 7构成反冲洗循环。 因超滤膜装 置 6二次过滤形成极少数的杂质沉淀于反冲洗过滤器 14，启动反冲洗泵 15冲 无菌水池 7反抽清水经过反冲洗过滤器 14实现反冲洗后从反冲排水管 5排除。
以上揭露仅为本实用新型较佳实施例而已， 然不能以此来限定本实用 新型的权利范围， 凡其他未脱离本实用新型的实质范围下， 所完成的润饰及 其等效的修改或修饰是允许的， 其专利保护范围应当视为包含在本专利申请 范围及其等同领域中。

Claims

WO 2014/117303 权 禾 ,】 要 求 书 PCT/CN2013/000332
1. nj移动一体化超滤膜饮用水生产机， 它包括箱柜 （27)、 滑轮 （26)， 所述箱柜 （27) 内两侧分别设有微涡流絮凝反应池 （1) 和无菌水池 （7)， 其 特征是： 所述微涡流絮凝反应池 （1) 和无菌水池 （7) 之间通过水管连接自 清洗过滤器 （23)、 供水泵 （2)、 超滤膜装置 （6) 和臭氧发生器 （28)。
2.根据权利要求 1 所述可移动 -体化超滤膜饮用水生产机， 其特征是： 所述超滤膜装置 （6) —侧连接清洗液箱 （12) 和清洗泵 （13)， 另一侧连接 反冲洗过滤器 （14)、 反冲洗泵 （15)， 所述反冲洗泵 （15) 与无菌水池 （7) 连接。
3.根据权利要求 1或 2所述可移动 ·体化超滤膜饮用水生产机， 其特征 是： 所述无菌水池 （7) 下方连接用户给水管 （20)， 所述用户给水管 （20) 设有变频供水泵 （21)。
4.根据权利要求 1 所述可移动一体化超滤膜饮用水生产机， 其特征是： 所述箱柜 （27) 的顶端设有换气扇 （4)。
5.根据权利要求 1 所述可移动 · 体化超滤膜饮用水生产机， 其特征是： 所述微涡流絮凝反应池 （1) 侧面连接混合器 （8)、 源水泵 （22)。
6.根据权利要求 5 所述可移动一体化超滤膜饮用水生产机， 其特征是： 所述混合器 (8) k连接计量泵 (9) ， 所述计量泵 (9) 与溶液箱 (24)连接。
PCT/CN2013/000332 2013-02-04 2013-03-21 可移动一体化超滤膜饮用水生产机 WO2014117303A1 (zh)

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Application Number Priority Date Filing Date Title
CN2013200631118U CN203079775U (zh) 2013-02-04 2013-02-04 可移动一体化超滤膜饮用水生产机
CN201320063111.8 2013-02-04

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WO2014117303A1 true WO2014117303A1 (zh) 2014-08-07

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CN106167336A (zh) * 2016-08-20 2016-11-30 南方创业（天津）科技发展有限公司 集成化水处理设备

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