CN220485407U - Bitter two-stage nanofiltration device - Google Patents

Bitter two-stage nanofiltration device Download PDF

Info

Publication number
CN220485407U
CN220485407U CN202322028687.7U CN202322028687U CN220485407U CN 220485407 U CN220485407 U CN 220485407U CN 202322028687 U CN202322028687 U CN 202322028687U CN 220485407 U CN220485407 U CN 220485407U
Authority
CN
China
Prior art keywords
water
nanofiltration
nanofiltration device
equipment
level
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Fee Related
Application number
CN202322028687.7U
Other languages
Chinese (zh)
Inventor
高凡
付秋萍
刘坤
姚小晨
龚栋栋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xinjiang Agricultural University
Original Assignee
Xinjiang Agricultural University
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 Xinjiang Agricultural University filed Critical Xinjiang Agricultural University
Priority to CN202322028687.7U priority Critical patent/CN220485407U/en
Application granted granted Critical
Publication of CN220485407U publication Critical patent/CN220485407U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

本实用新型公开了一种苦咸水双级纳滤装置,其包括一级纳滤设备和二级纳滤设备,一级纳滤设备和二级纳滤设备均包括通过纳滤膜分隔的浓水腔和清水腔,一级纳滤设备的浓水腔通过预处理过滤设备与进水管连接,且进水管上设置有驱动泵,一级纳滤设备的清水腔与二级纳滤设备的浓水腔连接,二级纳滤设备的清水腔与产水管连接,一级纳滤设备的浓水腔通过第一回流管路与进水管连接,二级纳滤设备的浓水腔通过第二回流管路与一级纳滤设备的浓水腔连接,第一回流管路和第二回流管路上均设置有单向阀,本方案通过双级过滤,提高了苦咸水的净化效果;同时可实现对苦咸水多次过滤后再排放,避免直接排放造成水资源的浪费。

The utility model discloses a two-stage nanofiltration device for brackish water, which includes a first-level nanofiltration equipment and a second-level nanofiltration equipment. Both the first-level nanofiltration equipment and the second-level nanofiltration equipment include concentrated water separated by a nanofiltration membrane. The water chamber and the clean water chamber. The concentrated water chamber of the first-level nanofiltration equipment is connected to the water inlet pipe through the pretreatment filtration equipment, and the water inlet pipe is equipped with a driving pump. The clean water chamber of the first-level nanofiltration equipment and the concentrated water chamber of the second-level nanofiltration equipment are connected. The water cavity is connected, the clean water cavity of the second-level nanofiltration equipment is connected to the water production pipe, the concentrated water cavity of the first-level nanofiltration equipment is connected to the water inlet pipe through the first return pipeline, and the concentrated water cavity of the second-level nanofiltration equipment is connected through the second return flow The pipeline is connected to the concentrated water chamber of the first-level nanofiltration equipment. One-way valves are installed on both the first return pipeline and the second return pipeline. This solution improves the purification effect of brackish water through two-stage filtration; at the same time, The brackish water can be filtered multiple times before being discharged to avoid the waste of water resources caused by direct discharge.

Description

一种苦咸水双级纳滤装置A two-stage nanofiltration device for brackish water

技术领域Technical field

本实用新型涉及苦咸水处理技术领域,具体涉及一种苦咸水双级纳滤装置。The utility model relates to the technical field of brackish water treatment, in particular to a two-stage nanofiltration device for brackish water.

背景技术Background technique

我国水资源短缺且不均匀,特别是西北地区,很多水源是苦咸,长期饮用没有有效净化的苦咸水会对人体造成巨大的损害,为此我国在很多农村地区建立的农村安全饮水工程,其中纳滤技术已逐步成为净水设备采用的主流工艺,可以实现饮用水深度净化。Our country’s water resources are scarce and uneven, especially in the northwest region. Many water sources are brackish. Long-term drinking of brackish water without effective purification will cause huge damage to the human body. For this reason, our country has established rural safe drinking water projects in many rural areas. Among them, nanofiltration technology has gradually become the mainstream process used in water purification equipment, which can achieve deep purification of drinking water.

纳滤是一种介于反渗透和超滤之间的压力驱动膜分离过程,其所依赖的纳滤膜的孔径范围在几个纳米左右,截留的分子量在80-1000范围内,用于将相对分子质量较小的物质,如无机盐或葡萄糖、蔗糖等小分子有机物从溶剂中分离出来,从而达到分离的效果;纳滤主要运用于饮用水和工业用水的纯化,废水净化处理,工艺流体中有价值成份的浓缩等方面。Nanofiltration is a pressure-driven membrane separation process between reverse osmosis and ultrafiltration. The nanofiltration membrane it relies on has a pore size in the range of several nanometers and a molecular weight cutoff in the range of 80-1000. It is used to Substances with smaller relative molecular weights, such as inorganic salts or small molecular organic substances such as glucose and sucrose, are separated from solvents to achieve separation effects; nanofiltration is mainly used in the purification of drinking water and industrial water, wastewater purification treatment, and process fluids. Concentration of valuable ingredients, etc.

但现有饮用水用的纳滤装置只设置有一级纳滤,净化效果较差,在过滤过程中效率较低,而且过滤后的浓水直接排出,没有进行回收利用,易造成水资源的浪费;同时,现有纳滤设备的纳滤膜结构简单,导致纳滤膜在过滤过程中与水的接触面积较小,从而影响过滤效率。However, the existing nanofiltration devices for drinking water are only equipped with one-stage nanofiltration, which has poor purification effect and low efficiency during the filtration process. Moreover, the filtered concentrated water is discharged directly without recycling, which can easily cause a waste of water resources. ; At the same time, the nanofiltration membrane structure of the existing nanofiltration equipment is simple, resulting in a small contact area between the nanofiltration membrane and water during the filtration process, thus affecting the filtration efficiency.

实用新型内容Utility model content

针对现有技术的上述不足,本实用新型提供了一种苦咸水双级纳滤装置,解决了现有纳滤设备过滤效率低下且易造成水资源浪费的问题。In view of the above-mentioned deficiencies of the prior art, the present utility model provides a two-stage brackish water nanofiltration device, which solves the problems of low filtration efficiency of existing nanofiltration equipment and easy waste of water resources.

为实现上述目的,本实用新型所采用的技术方案为:In order to achieve the above purpose, the technical solution adopted by the present utility model is:

提供一种苦咸水双级纳滤装置,其包括一级纳滤设备和二级纳滤设备,一级纳滤设备和二级纳滤设备均包括通过纳滤膜分隔的浓水腔和清水腔,一级纳滤设备的浓水腔通过预处理过滤设备与进水管连接,且进水管上设置有驱动泵,一级纳滤设备的清水腔与二级纳滤设备的浓水腔连接,二级纳滤设备的清水腔与产水管连接,一级纳滤设备的浓水腔通过第一回流管路与进水管连接,二级纳滤设备的浓水腔通过第二回流管路与一级纳滤设备的浓水腔连接,第一回流管路和第二回流管路上均设置有单向阀。A two-stage brackish water nanofiltration device is provided, which includes a first-level nanofiltration device and a second-level nanofiltration device. Both the first-level nanofiltration device and the second-level nanofiltration device include a concentrated water chamber and clean water separated by a nanofiltration membrane. cavity, the concentrated water cavity of the first-level nanofiltration equipment is connected to the water inlet pipe through the pretreatment filtering equipment, and the water inlet pipe is provided with a driving pump, and the clean water cavity of the first-level nanofiltration equipment is connected to the concentrated water cavity of the second-level nanofiltration equipment. The clean water chamber of the second-level nanofiltration equipment is connected to the water production pipe, the concentrated water chamber of the first-level nanofiltration equipment is connected to the water inlet pipe through the first return pipe, and the concentrated water chamber of the second-level nanofiltration equipment is connected to the first return pipe through the second return pipe. The concentrated water chamber of the first-level nanofiltration equipment is connected, and one-way valves are provided on both the first return pipeline and the second return pipeline.

进一步地,一级纳滤设备和二级纳滤设备均包括壳体,壳体内设置有安装板,安装板上设置有若干过水孔,过水孔的一端设置有纳滤膜组件,且纳滤膜组件位于浓水腔内,纳滤膜组件包括筒状纳滤膜,筒状纳滤膜的两端分别设置有堵头和套环,套环的外壁与过水孔的内壁通过螺纹配合固定连接,筒状纳滤膜的内腔通过过水孔与清水腔连通。Further, both the first-level nanofiltration equipment and the second-level nanofiltration equipment include a shell, a mounting plate is provided in the shell, a number of water holes are provided on the installation plate, and a nanofiltration membrane module is provided at one end of the water hole, and the nanofiltration membrane module is provided at one end of the water hole. The filter membrane assembly is located in the concentrated water chamber. The nanofiltration membrane assembly includes a cylindrical nanofiltration membrane. The two ends of the cylindrical nanofiltration membrane are respectively provided with plugs and collars. The outer wall of the collar is threaded with the inner wall of the water hole. Fixed connection, the inner cavity of the cylindrical nanofiltration membrane is connected with the clean water cavity through the water hole.

进一步地,筒状纳滤膜的外侧壁和内侧壁上均设置有支撑钢网,支撑钢网的两端分别固定在堵头和套环上。Further, a supporting steel mesh is provided on both the outer and inner walls of the cylindrical nanofiltration membrane, and the two ends of the supporting steel mesh are respectively fixed on the plug and the collar.

进一步地,壳体的前端设置有可拆卸的端盖。Further, the front end of the housing is provided with a detachable end cover.

进一步地,二级纳滤设备的清水腔与反洗管路连接,且反洗管路上设置有反洗泵,驱动泵与预处理过滤设备之间的连接管路上设置有出水支路,一级纳滤设备和二级纳滤设备的浓水腔上均设置有排水管,出水支路、排水管、产水管、第一回流管路、第二回流管路、驱动泵的出水端以及反洗泵的出水端上均设置有开关阀,驱动泵的开关阀位于出水支路的前端。Further, the clean water chamber of the secondary nanofiltration equipment is connected to the backwash pipeline, and a backwash pump is provided on the backwash pipeline, and a water outlet branch is provided on the connection pipeline between the drive pump and the pretreatment filtration equipment. The concentrated water chamber of the nanofiltration equipment and the secondary nanofiltration equipment is equipped with a drainage pipe, a water outlet branch, a drainage pipe, a water production pipe, a first return pipeline, a second return pipeline, the water outlet end of the driving pump and backwashing The water outlet end of the pump is equipped with an on-off valve, and the on-off valve that drives the pump is located at the front end of the water outlet branch.

进一步地,驱动泵和反洗泵的出水端均设置有自动调压阀,一级纳滤设备和二级纳滤设备的浓水腔的侧壁上均设置有压力表。Further, the water outlets of the driving pump and the backwash pump are equipped with automatic pressure regulating valves, and pressure gauges are installed on the side walls of the concentrated water chambers of the first-level nanofiltration equipment and the second-level nanofiltration equipment.

进一步地,预处理过滤设备包括过滤网、活性炭过滤器和/或保安过滤器。Further, the pretreatment filtration equipment includes a filter screen, an activated carbon filter and/or a security filter.

本实用新型的有益效果为:The beneficial effects of this utility model are:

1.本方案通过一级纳滤设备和二级纳滤设备对苦咸水进行双级过滤,相比于单级纳滤,提高了苦咸水的净化效果;同时一级纳滤设备过滤后的浓缩水可通过第一回流管路回流至进水管,二级纳滤设备过滤后的浓缩水可通过第二回流管路回流至一级纳滤设备中,从而实现对苦咸水多次过滤后再排放,避免直接排放造成水资源的浪费。1. This solution uses one-stage nanofiltration equipment and two-stage nanofiltration equipment to perform two-stage filtration of brackish water. Compared with single-stage nanofiltration, it improves the purification effect of brackish water; at the same time, after filtration by the first-stage nanofiltration equipment The concentrated water can flow back to the inlet pipe through the first return line, and the concentrated water filtered by the second-level nanofiltration equipment can flow back to the first-level nanofiltration equipment through the second return line, thereby achieving multiple filtration of brackish water. before discharging to avoid wasting water resources caused by direct discharge.

2.通过设置若干筒状纳滤膜,使得在有限的壳体空间内,可增大纳滤膜与水的接触面积,从而提高了过滤效率;同时筒状纳滤膜拆装便捷,以便于后期的维护更换;通过支撑钢网可对筒状纳滤膜进行支撑,防止筒状纳滤膜的侧壁在受压过滤时出现凹陷或凸起的情况而导致筒状纳滤膜失效。2. By arranging several cylindrical nanofiltration membranes, the contact area between the nanofiltration membrane and water can be increased in a limited shell space, thereby improving the filtration efficiency; at the same time, the cylindrical nanofiltration membranes are easy to disassemble and assemble for convenience. Later maintenance and replacement; the cylindrical nanofiltration membrane can be supported by the supporting steel mesh to prevent the side wall of the cylindrical nanofiltration membrane from being sunk or bulged during pressure filtration, causing the cylindrical nanofiltration membrane to fail.

3.通过设置反洗管路和出水支路可实现对一级纳滤设备、二级纳滤设备和预处理过滤设备的反向冲洗,避免设备的堵塞,保证本方案装置正常运行时的净化效率和净化效果。3. By setting up the backwash pipeline and water outlet branch, the backwash of the first-level nanofiltration equipment, the second-level nanofiltration equipment and the pretreatment filtration equipment can be realized to avoid equipment clogging and ensure purification during normal operation of the device of this solution. efficiency and purification effect.

附图说明Description of the drawings

图1为本方案苦咸水双级纳滤装置的结构示意图。Figure 1 is a schematic structural diagram of the two-stage brackish water nanofiltration device of this solution.

图2为一级纳滤设备的结构示意图。Figure 2 is a schematic structural diagram of the first-level nanofiltration equipment.

其中,1、一级纳滤设备,2、二级纳滤设备,3、纳滤膜,4、浓水腔,5、清水腔,6、预处理过滤设备,7、进水管,8、驱动泵,9、产水管,10、第一回流管路,11、第二回流管路,12、单向阀,13、壳体,14、安装板,15、过水孔,16、筒状纳滤膜,17、堵头,18、套环,19、端盖,20、反洗管路,21、反洗泵,22、出水支路,23、排水管,24、开关阀,25、自动调压阀,26、压力表。Among them, 1. First-level nanofiltration equipment, 2. Second-level nanofiltration equipment, 3. Nanofiltration membrane, 4. Concentrated water chamber, 5. Clean water chamber, 6. Pretreatment filtration equipment, 7. Water inlet pipe, 8. Drive Pump, 9. Water production pipe, 10. First return pipeline, 11. Second return pipeline, 12. One-way valve, 13. Shell, 14. Installation plate, 15. Water hole, 16. Cylindrical tank Filter membrane, 17. Plug, 18. Collar, 19. End cap, 20. Backwash pipeline, 21. Backwash pump, 22. Water outlet branch, 23. Drainage pipe, 24. On/off valve, 25. Automatic Pressure regulating valve, 26, pressure gauge.

具体实施方式Detailed ways

下面对本实用新型的具体实施方式进行描述,以便于本技术领域的技术人员理解本实用新型,但应该清楚,本实用新型不限于具体实施方式的范围,对本技术领域的普通技术人员来讲,只要各种变化在所附的权利要求限定和确定的本实用新型的精神和范围内,这些变化是显而易见的,一切利用本实用新型构思的实用新型创造均在保护之列。Specific embodiments of the present utility model are described below to facilitate those skilled in the art to understand the utility model. However, it should be clear that the present utility model is not limited to the scope of the specific embodiments. For those of ordinary skill in the technical field, as long as Various changes are obvious within the spirit and scope of the present utility model as defined and determined by the appended claims, and all utility model creations utilizing the concepts of the present utility model are protected.

实施例1Example 1

如图1所示,本方案的苦咸水双级纳滤装置包括一级纳滤设备1和二级纳滤设备2,一级纳滤设备1和二级纳滤设备2均包括通过纳滤膜3分隔的浓水腔4和清水腔5,一级纳滤设备1的浓水腔4通过预处理过滤设备6与进水管7连接,且进水管7上设置有驱动泵8,预处理过滤设备6包括过滤网以及活性炭过滤器和/或保安过滤器,一级纳滤设备1的清水腔5与二级纳滤设备2的浓水腔4连接,二级纳滤设备2的清水腔5与产水管9连接,一级纳滤设备1的浓水腔4通过第一回流管路10与进水管7连接,二级纳滤设备2的浓水腔4通过第二回流管路11与一级纳滤设备1的浓水腔4连接,第一回流管路10和第二回流管路11上均设置有单向阀12,一级纳滤设备1和二级纳滤设备2的浓水腔4上均设置有排水管23。As shown in Figure 1, the brackish water two-stage nanofiltration device of this solution includes first-level nanofiltration equipment 1 and second-level nanofiltration equipment 2. Both first-level nanofiltration equipment 1 and second-level nanofiltration equipment 2 include nanofiltration equipment. The concentrated water chamber 4 and the clean water chamber 5 are separated by the membrane 3. The concentrated water chamber 4 of the first-level nanofiltration equipment 1 is connected to the water inlet pipe 7 through the pretreatment filtration equipment 6, and the water inlet pipe 7 is provided with a driving pump 8. The pretreatment filtration The equipment 6 includes a filter screen and an activated carbon filter and/or a security filter. The clean water chamber 5 of the first-level nanofiltration equipment 1 is connected to the concentrated water chamber 4 of the second-level nanofiltration equipment 2. The clean water chamber 5 of the second-level nanofiltration equipment 2 is Connected to the water production pipe 9, the concentrated water chamber 4 of the first-level nanofiltration equipment 1 is connected to the water inlet pipe 7 through the first return pipeline 10, and the concentrated water chamber 4 of the second-level nanofiltration equipment 2 is connected to a second return pipeline 11 through the second return pipeline 11. The concentrated water chamber 4 of the first-level nanofiltration equipment 1 is connected. The first return pipeline 10 and the second return pipeline 11 are both provided with one-way valves 12. The concentrated water of the first-level nanofiltration equipment 1 and the second-level nanofiltration equipment 2 Drainage pipes 23 are provided on each cavity 4 .

实施时,纳滤膜3的孔径为1~2nm,一级纳滤设备1内纳滤膜3的孔径大于二级纳滤设备2内纳滤膜3的孔径,且材质均为聚酰胺材质,使得该纳滤膜3具有良好的成膜性、热稳定性、化学稳定性、机械强度高、耐酸碱及微生物侵蚀、耐氯和其它氧化性物质,还具有高水通量及高盐截留率、抗胶体及悬浮物污染以及价格便宜的优点;驱动泵8的操作压力不高于0.85Mpa,一级纳滤设备1的工作压力在0.65-0.85Mpa之间,二级纳滤设备2的工作压力在0.5-0.65Mpa之间,有利于防止纳滤膜3发生严重变形,从而提高了纳滤膜3的使用寿命。During implementation, the pore size of the nanofiltration membrane 3 is 1 to 2 nm. The pore size of the nanofiltration membrane 3 in the first-level nanofiltration equipment 1 is larger than the pore size of the nanofiltration membrane 3 in the second-level nanofiltration equipment 2, and the materials are all made of polyamide. This makes the nanofiltration membrane 3 have good film-forming properties, thermal stability, chemical stability, high mechanical strength, resistance to acid, alkali and microbial erosion, resistance to chlorine and other oxidizing substances, and also has high water flux and high salt interception efficiency, resistance to colloid and suspended matter pollution, and low price; the operating pressure of the driving pump 8 is not higher than 0.85Mpa, the working pressure of the first-level nanofiltration equipment 1 is between 0.65-0.85Mpa, and the operating pressure of the second-level nanofiltration equipment 2 The working pressure is between 0.5-0.65Mpa, which is beneficial to preventing serious deformation of the nanofiltration membrane 3, thereby increasing the service life of the nanofiltration membrane 3.

本方案通过一级纳滤设备1和二级纳滤设备2对苦咸水进行双级过滤,相比于单级纳滤,提高了苦咸水的净化效果;同时一级纳滤设备1过滤后的浓缩水可通过第一回流管路10回流至进水管7,二级纳滤设备2过滤后的浓缩水可通过第二回流管路11回流至一级纳滤设备1中,从而实现对苦咸水多次过滤后再通过排水管23排放,避免直接排放造成水资源的浪费。This solution uses primary nanofiltration equipment 1 and secondary nanofiltration equipment 2 to perform dual-stage filtration of brackish water. Compared with single-stage nanofiltration, the purification effect of brackish water is improved; at the same time, primary nanofiltration equipment 1 filters The concentrated water can be returned to the water inlet pipe 7 through the first return line 10, and the concentrated water filtered by the second-level nanofiltration equipment 2 can be returned to the first-level nanofiltration equipment 1 through the second return line 11, thereby realizing the control. The brackish water is filtered multiple times and then discharged through the drainage pipe 23 to avoid waste of water resources caused by direct discharge.

实施例2Example 2

如图2所示,本实施例在实施例1的基础上,给出了一级纳滤设备1和二级纳滤设备2的具体方案,其中一级纳滤设备1和二级纳滤设备2结构相同,其均包括壳体13,壳体13的前端设置有可拆卸的端盖19,壳体13内设置有安装板14,安装板14上设置有若干过水孔15,过水孔15的一端设置有纳滤膜3组件,且纳滤膜3组件位于浓水腔4内,纳滤膜3组件包括筒状纳滤膜16,筒状纳滤膜16的两端分别设置有堵头17和套环18,套环18的外壁与过水孔15一端的内壁通过螺纹配合固定连接,筒状纳滤膜16的内腔通过过水孔15与清水腔5连通,筒状纳滤膜16的外侧壁和内侧壁上均设置有支撑钢网,支撑钢网的两端分别固定在堵头17和套环18上。As shown in Figure 2, on the basis of Example 1, this embodiment provides specific solutions for the first-level nanofiltration equipment 1 and the second-level nanofiltration equipment 2, wherein the first-level nanofiltration equipment 1 and the second-level nanofiltration equipment 2 have the same structure, including a shell 13. The front end of the shell 13 is provided with a detachable end cover 19. The shell 13 is provided with a mounting plate 14. The mounting plate 14 is provided with a number of water holes 15. The water holes One end of 15 is provided with a nanofiltration membrane 3 component, and the nanofiltration membrane 3 component is located in the concentrated water chamber 4. The nanofiltration membrane 3 component includes a cylindrical nanofiltration membrane 16, and the two ends of the cylindrical nanofiltration membrane 16 are respectively provided with plugs. The head 17 and the collar 18, the outer wall of the collar 18 and the inner wall of one end of the water hole 15 are fixedly connected through threaded fit, the inner cavity of the cylindrical nanofiltration membrane 16 is connected with the clean water chamber 5 through the water hole 15, and the cylindrical nanofiltration A supporting steel mesh is provided on both the outer and inner walls of the membrane 16, and the two ends of the supporting steel mesh are respectively fixed on the plug 17 and the collar 18.

本方案通过设置若干筒状纳滤膜16,使得在有限的壳体13空间内,可增大纳滤膜3与水的接触面积,从而提高了过滤效率;同时筒状纳滤膜16拆装便捷,以便于后期的维护更换;通过支撑钢网可对筒状纳滤膜16进行支撑,防止筒状纳滤膜16的侧壁在受压过滤时出现凹陷或凸起的情况而导致筒状纳滤膜16失效。In this solution, by arranging several cylindrical nanofiltration membranes 16, the contact area between the nanofiltration membrane 3 and water can be increased in the limited space of the housing 13, thereby improving the filtration efficiency; at the same time, the cylindrical nanofiltration membranes 16 can be disassembled and assembled Convenient to facilitate later maintenance and replacement; the cylindrical nanofiltration membrane 16 can be supported by the supporting steel mesh to prevent the side wall of the cylindrical nanofiltration membrane 16 from being sunk or bulged during pressure filtration, causing the cylindrical shape Nanofiltration membrane 16 failed.

实施例3Example 3

本实施例在实施例1的基础上,所作出的进一步限定,二级纳滤设备2的清水腔5与反洗管路20连接,且反洗管路20上设置有反洗泵21,驱动泵8与预处理过滤设备6之间的连接管路上设置有出水支路22,出水支路22、排水管23、产水管9、第一回流管路10、第二回流管路11、驱动泵8的出水端以及反洗泵21的出水端上均设置有开关阀24,驱动泵8的开关阀24位于出水支路22的前端,驱动泵8和反洗泵21的出水端均设置有自动调压阀25,一级纳滤设备1和二级纳滤设备2的浓水腔4的侧壁上均设置有压力表26。This embodiment is further limited on the basis of Embodiment 1. The clean water chamber 5 of the secondary nanofiltration equipment 2 is connected to the backwash pipeline 20, and the backwash pipeline 20 is provided with a backwash pump 21 to drive The connection pipeline between the pump 8 and the pretreatment filtering equipment 6 is provided with a water outlet branch 22, a water outlet branch 22, a drainage pipe 23, a water production pipe 9, a first return pipeline 10, a second return pipeline 11, and a driving pump. 8 and the water outlet of the backwash pump 21 are provided with a switch valve 24. The switch valve 24 of the drive pump 8 is located at the front end of the water outlet branch 22. The water outlets of the drive pump 8 and the backwash pump 21 are equipped with automatic valves 24. The pressure regulating valve 25, the side walls of the concentrated water chamber 4 of the primary nanofiltration equipment 1 and the secondary nanofiltration equipment 2 are all provided with pressure gauges 26.

本方案通过设置反洗管路20和出水支路22可实现对一级纳滤设备1、二级纳滤设备2和预处理过滤设备6的反向冲洗,且在进行反向冲洗时,关闭排水管23、产水管9、第一回流管路10、第二回流管路11和驱动泵8的出水端的开关阀24,使反向冲洗的水流依次经过二级纳滤设备2的清水腔5、浓水腔4、一级纳滤设备1的清水腔5、浓水腔4、预处理过滤设备6后,通过出水支路22排出,达到清洗整个过滤设备的目的,避免设备的堵塞,保证本方案装置正常运行时的净化效率和净化效果。This solution can realize the backwashing of the first-level nanofiltration equipment 1, the second-level nanofiltration equipment 2 and the pretreatment filtration equipment 6 by setting up the backwashing pipeline 20 and the water outlet branch 22, and during the backwashing, the system is closed The drainage pipe 23, the water production pipe 9, the first return pipe 10, the second return pipe 11 and the switch valve 24 at the water outlet of the drive pump 8 allow the reverse flushing water flow to pass through the clean water chamber 5 of the secondary nanofiltration equipment 2 in sequence. , the concentrated water chamber 4, the clean water chamber 5 of the first-level nanofiltration equipment 1, the concentrated water chamber 4, and the pretreatment filtration equipment 6 are discharged through the water outlet branch 22 to achieve the purpose of cleaning the entire filtration equipment, avoid clogging of the equipment, and ensure The purification efficiency and purification effect of the device of this solution during normal operation.

Claims (6)

1. The utility model provides a brackish water doublestage nanofiltration device which characterized in that, including one-level nanofiltration device and second grade nanofiltration device, one-level nanofiltration device and second grade nanofiltration device all include through nanofiltration membrane partition's dense water cavity and clear water cavity, one-level nanofiltration device's dense water cavity is connected with the inlet tube through pretreatment filtration device, and is provided with the actuating pump on the inlet tube, one-level nanofiltration device's clear water cavity is connected with second grade nanofiltration device's dense water cavity, second grade nanofiltration device's clear water cavity is connected with the water production pipe, one-level nanofiltration device's dense water cavity is connected with the inlet tube through first return line, second grade nanofiltration device's dense water cavity is connected with one-level nanofiltration device's dense water cavity through the second return line, all be provided with the check valve on first return line and the second return line;
the one-level nanofiltration equipment and the two-level nanofiltration equipment comprise a shell, a mounting plate is arranged in the shell, a plurality of water passing holes are formed in the mounting plate, one end of each water passing hole is provided with a nanofiltration membrane component, the nanofiltration membrane component is located in a concentrated water cavity, the nanofiltration membrane component comprises a cylindrical nanofiltration membrane, plugs and lantern rings are respectively arranged at two ends of the cylindrical nanofiltration membrane, the outer wall of the lantern ring is fixedly connected with the inner wall of each water passing hole through screw thread fit, and an inner cavity of the cylindrical nanofiltration membrane is communicated with a clear water cavity through the water passing holes.
2. The two-stage nanofiltration device for brackish water according to claim 1, wherein the outer side wall and the inner side wall of the cylindrical nanofiltration membrane are respectively provided with a supporting steel mesh, and two ends of the supporting steel mesh are respectively fixed on the plug and the lantern ring.
3. The brackish water dual stage nanofiltration device of claim 1 wherein the front end of the housing is provided with a removable end cap.
4. The brackish water double-stage nanofiltration device according to claim 1, wherein the clear water cavity of the secondary nanofiltration device is connected with a backwash pipeline, a backwash pump is arranged on the backwash pipeline, a water outlet branch is arranged on a connecting pipeline between the driving pump and the pretreatment filtration device, drain pipes are arranged on the concentrated water cavities of the primary nanofiltration device and the secondary nanofiltration device, and a switch valve is arranged on the water outlet branch, the drain pipe, the water production pipe, the first return pipeline, the second return pipeline, the water outlet end of the driving pump and the water outlet end of the backwash pump, and the switch valve of the driving pump is arranged at the front end of the water outlet branch.
5. The brackish water double-stage nanofiltration device according to claim 4, wherein the water outlet ends of the driving pump and the backwash pump are provided with automatic pressure regulating valves, and the side walls of the concentrated water chambers of the primary nanofiltration device and the secondary nanofiltration device are provided with pressure gauges.
6. The brackish water dual stage nanofiltration device of claim 1 wherein the pretreatment filtration equipment comprises a filter screen, an activated carbon filter, and/or a cartridge filter.
CN202322028687.7U 2023-07-28 2023-07-28 Bitter two-stage nanofiltration device Expired - Fee Related CN220485407U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202322028687.7U CN220485407U (en) 2023-07-28 2023-07-28 Bitter two-stage nanofiltration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202322028687.7U CN220485407U (en) 2023-07-28 2023-07-28 Bitter two-stage nanofiltration device

Publications (1)

Publication Number Publication Date
CN220485407U true CN220485407U (en) 2024-02-13

Family

ID=89831729

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202322028687.7U Expired - Fee Related CN220485407U (en) 2023-07-28 2023-07-28 Bitter two-stage nanofiltration device

Country Status (1)

Country Link
CN (1) CN220485407U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118289886A (en) * 2024-04-30 2024-07-05 郑州正源净水科技有限公司 Dual-mode water purification system and water purification equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118289886A (en) * 2024-04-30 2024-07-05 郑州正源净水科技有限公司 Dual-mode water purification system and water purification equipment

Similar Documents

Publication Publication Date Title
CN212091725U (en) A composite filter element assembly and water purification system
CN1245249C (en) Hollow fiber membrane separation device and its operating method
CN105217721B (en) A kind of photocatalysis compound-split membrane water treatment device and water treatment system
CN220485407U (en) Bitter two-stage nanofiltration device
CN204039126U (en) A kind of membrane bioreactor
CN110790344A (en) Novel drinking water advanced treatment and purification device and method
CN201094903Y (en) Multilevel combined pipeline type ultra-filtering water purifier
CN104192994B (en) A kind of membrane bioreactor
CN101264975B (en) A column membrane module
CN101670240B (en) Filtering tank
CN201040233Y (en) Pipeline ultrafiltration water purifier
CN104743703B (en) A kind of unpowered emergent water purifier suitable for disaster area after shake
CN113060831A (en) Antifouling stifled aeration equipment of MBR
CN202460484U (en) Easily-assembled integrated enhanced-type external-pressure hollow fiber membrane assembly
CN110316845A (en) A kind of RO reverse osmosis water purifier of the household with auto-flushing
CN215756582U (en) Utilize domestic water purification unit in whole room of dull and stereotyped ceramic membrane drainage
CN105984984A (en) Dye wastewater deep purification and reuse system as well as method thereof
CN211570291U (en) Ceramic membrane second-stage reverse osmosis advanced treatment system
CN210340497U (en) Domestic RO reverse osmosis water purification machine of automatic washing of taking
CN2625381Y (en) Hollow fiber membrane system filter
CN115487675A (en) Filter element and water purification device including the filter element
CN201182951Y (en) Water purifier with pollution discharge apparatus
CN202465362U (en) Continuous aeration external pressure type hollow fiber membrane system for water supply system
CN214570917U (en) Novel microfiltration device for seawater desalination pretreatment
CN218931906U (en) Modularized membrane treatment water purification device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20240213