CN108144448A - A kind of collecting system for rotary film device - Google Patents
A kind of collecting system for rotary film device Download PDFInfo
- Publication number
- CN108144448A CN108144448A CN201810132293.7A CN201810132293A CN108144448A CN 108144448 A CN108144448 A CN 108144448A CN 201810132293 A CN201810132293 A CN 201810132293A CN 108144448 A CN108144448 A CN 108144448A
- Authority
- CN
- China
- Prior art keywords
- water collection
- membrane
- water
- rotating shaft
- liquid
- 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.)
- Pending
Links
- 239000012528 membrane Substances 0.000 claims abstract description 119
- 238000009434 installation Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 87
- 239000007788 liquid Substances 0.000 claims description 51
- 230000001681 protective effect Effects 0.000 claims description 6
- 238000001471 micro-filtration Methods 0.000 claims description 4
- 238000000108 ultra-filtration Methods 0.000 claims description 4
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 230000002787 reinforcement Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 description 6
- 230000003014 reinforcing effect Effects 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000009295 crossflow filtration Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000010287 polarization Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000009991 scouring Methods 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 230000010412 perfusion Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/147—Microfiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/145—Ultrafiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/18—Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/04—Backflushing
Landscapes
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明涉及水净化技术领域,尤其是一种用于旋转式膜设备的集水系统。The invention relates to the technical field of water purification, in particular to a water collection system for a rotary membrane device.
背景技术Background technique
膜分离技术近年来发展十分迅速,从微滤、超滤、纳滤到反渗透,已经在污水处理、饮用水净化、海水淡化、工业分离等领域广泛应用。现在膜材料的制备技术(包括高分子有机膜和无机膜)已经相当成熟,但是膜的工业化应用方式却相对落后,比如高分子材料的平板膜和中空纤维膜,其膜组件都是静态的,靠曝气形成错流过滤;无机管式膜,主要靠泵提升待处理液的流速形成错流过滤,这些膜应用方式只是实验室技术的简单放大,膜容易堵、能耗高,而且膜的应用领域也受到限制。Membrane separation technology has developed rapidly in recent years. From microfiltration, ultrafiltration, nanofiltration to reverse osmosis, it has been widely used in sewage treatment, drinking water purification, seawater desalination, industrial separation and other fields. At present, the preparation technology of membrane materials (including polymer organic membranes and inorganic membranes) is quite mature, but the industrial application of membranes is relatively backward. For example, the membrane components of flat membranes and hollow fiber membranes of polymer materials are static. Cross-flow filtration is formed by aeration; inorganic tubular membranes mainly rely on pumps to increase the flow rate of the liquid to be treated to form cross-flow filtration. The application of these membranes is just a simple amplification of laboratory technology. The field of application is also limited.
发明内容Contents of the invention
本发明要解决的技术问题是提供一种用于旋转式膜设备的集水系统,该系统结构紧凑、流道畅通、膜效率高、安装更换方便。The technical problem to be solved by the present invention is to provide a water collection system for rotary membrane equipment, which has compact structure, smooth flow channel, high membrane efficiency and convenient installation and replacement.
为了解决上述技术问题,本发明提供了一种用于旋转式膜设备的集水系统,其包括:集水膜组件,设置在所述集水膜组件周边的集液管,与所述集液管贯通的中空转轴,所述中空转轴由驱动机构驱动其旋转,所述中空转轴带动所述集水膜组件旋转;In order to solve the above technical problems, the present invention provides a water collection system for rotary membrane equipment, which includes: a water collection membrane module, a liquid collection pipe arranged around the water collection membrane module, and the liquid collection A hollow rotating shaft through which the pipe runs, and the hollow rotating shaft is driven to rotate by a driving mechanism, and the hollow rotating shaft drives the water collection membrane assembly to rotate;
所述中空转轴的一端连接至出流导管上,所述出流导管与抽水泵相连。One end of the hollow rotating shaft is connected to an outflow conduit, and the outflow conduit is connected to a water pump.
在本发明的一个较佳实施例中,进一步包括,所述集水膜组件包括若干个集水膜组元,所述集水膜组元的一端设有出液孔和集水容腔,所述出液孔与所述集水容腔贯通,各个所述集水膜组元的集水容腔连接在一起形成水流通道,并且设置在所述集水膜组件两端的所述集水容腔与所述集液管连接,所述集液管与所述中空转轴贯通;所述集水膜组件环绕所述中空转轴固定,构成旋转式集水膜转盘,所述驱动机构通过所述中空转轴带动所述集水膜组件在水下进行浸没式或半浸没式旋转。In a preferred embodiment of the present invention, it further includes that the water-collecting membrane assembly includes several water-collecting membrane components, and one end of the water-collecting membrane components is provided with a liquid outlet hole and a water-collecting chamber, so The liquid outlet hole is connected with the water collection chamber, and the water collection chambers of each of the water collection membrane components are connected together to form a water flow channel, and the water collection chambers arranged at both ends of the water collection membrane assembly Connected with the liquid collection pipe, the liquid collection pipe is connected with the hollow shaft; the water collection membrane module is fixed around the hollow shaft to form a rotary water collection membrane turntable, and the driving mechanism passes through the hollow shaft The water collecting membrane module is driven to perform submerged or semi-submerged rotation under water.
在本发明的一个较佳实施例中,进一步包括,所述中空转轴上开设有进液孔,所述进液孔与所述集液管贯通。In a preferred embodiment of the present invention, it further includes that a liquid inlet hole is opened on the hollow rotating shaft, and the liquid inlet hole communicates with the liquid collecting pipe.
在本发明的一个较佳实施例中,进一步包括,所述集水膜组元上设有安装头,在所述集水膜组元安装时,所述安装头插入固定件的安装孔中,各个所述集水膜组元之间有0.2~1.5cm的间隙。In a preferred embodiment of the present invention, it further includes that the water-collecting membrane component is provided with a mounting head, and when the water-collecting membrane component is installed, the mounting head is inserted into the mounting hole of the fixing member, There is a gap of 0.2-1.5 cm between each of the water-collecting membrane components.
在本发明的一个较佳实施例中,进一步包括,所述集水膜组元采用中空腔式或表面导流沟槽式支撑结构,在所述支撑结构的两侧焊接超滤或微滤膜片。In a preferred embodiment of the present invention, it further includes that the water collection membrane component adopts a hollow cavity type or surface diversion groove type support structure, and ultrafiltration or microfiltration membranes are welded on both sides of the support structure piece.
在本发明的一个较佳实施例中,进一步包括,所述支撑结构为一体化注塑件。In a preferred embodiment of the present invention, it further includes that the support structure is an integral injection molded part.
在本发明的一个较佳实施例中,进一步包括,所述中空转轴的一端连接有旋转接头,通过所述旋转接头连接至所述出流导管上,所述中空转轴的另一端为封闭状态。In a preferred embodiment of the present invention, it further includes that one end of the hollow rotating shaft is connected with a rotary joint, and is connected to the outflow conduit through the rotating joint, and the other end of the hollow rotating shaft is in a closed state.
在本发明的一个较佳实施例中,进一步包括,所述中空转轴的两端固定在轴承座上。In a preferred embodiment of the present invention, it further includes that both ends of the hollow rotating shaft are fixed on the bearing seat.
在本发明的一个较佳实施例中,进一步包括,还包括集液管保护罩,所述集液管安装在所述集液管保护罩内部。In a preferred embodiment of the present invention, it further includes a liquid collecting pipe protective cover, and the liquid collecting pipe is installed inside the liquid collecting pipe protective cover.
在本发明的一个较佳实施例中,进一步包括,所述集水膜组件的两侧设有加强筋。In a preferred embodiment of the present invention, it further includes that reinforcing ribs are provided on both sides of the water collection membrane module.
本发明的技术效果:Technical effect of the present invention:
1、本发明中的集水膜组元采用中空腔式或表面导流沟槽式支撑结构,负压分配均匀,消除过滤死区,提高膜效率。1. The water-collecting membrane component in the present invention adopts a hollow cavity type or a surface diversion groove type support structure, and the negative pressure is evenly distributed, eliminating the filtration dead zone and improving the membrane efficiency.
2、集水膜组元拆装方便,牢固可靠,当单个或几个集水膜组元损坏需要更换时,无需拆卸整组集水膜组件,拿下紧固件后可直接对损坏膜组元进行更换。2. The water-collecting membrane components are easy to disassemble, firm and reliable. When one or several water-collecting membrane components are damaged and need to be replaced, there is no need to disassemble the entire set of water-collecting membrane components. The damaged membrane group can be directly repaired after the fasteners are removed. Yuan to replace.
3、集水膜组件设有出液孔和集水容腔,无需另配集水管,一体化设计节省空间,降低成本。3. The water-collecting membrane module is equipped with a liquid outlet hole and a water-collecting chamber, and no additional water-collecting pipe is required. The integrated design saves space and reduces costs.
4、各集水膜组元具有一定间距及旋转式集水膜转盘为多边形结构,使得集水膜转盘在浸没式程控旋转运行时,形成强力冲刷效果,防止滤层累积,提高稳定膜通量,通过控制转速和抽停周期等操作状态,使膜表面产生足够的剪切力、离心力及滤液湍流等,达到理想的错流式操作和消除浓差极化效果。4. Each water-collecting membrane component has a certain distance and the rotating water-collecting membrane turntable is a polygonal structure, so that the water-collecting membrane turntable forms a strong scouring effect when the water-collecting membrane turntable is in the submerged program-controlled rotation operation, prevents the accumulation of filter layers, and improves the stable membrane flux. , by controlling the operating states such as the rotational speed and the pumping stop cycle, the surface of the membrane can generate sufficient shear force, centrifugal force and filtrate turbulence, etc., to achieve the ideal cross-flow operation and eliminate the effect of concentration polarization.
5、用于旋转式膜设备的集水系统结构紧凑,流道通畅,便于在线灌注清洗,实现设备的集成化。5. The water collection system used for rotary membrane equipment has a compact structure and smooth flow channels, which is convenient for on-line perfusion cleaning and realizes the integration of equipment.
6、通过集水膜组件的浸没式程控旋转运行,达到理想的错流式操作和消除浓差极化效果。6. Through the submerged program-controlled rotating operation of the water collection membrane module, the ideal cross-flow operation and the elimination of concentration polarization effect are achieved.
附图说明Description of drawings
图1是本发明的结构示意图;Fig. 1 is a structural representation of the present invention;
图2是本发明集水膜组元的结构示意图;Fig. 2 is a schematic structural view of the water collection membrane component of the present invention;
图3是本发明集水膜组件组成的集水膜转盘的结构示意图;Fig. 3 is a schematic structural view of a water-collecting membrane turntable composed of a water-collecting membrane module of the present invention;
图中标号说明:Explanation of symbols in the figure:
1集水膜组件,2集液管,3中空转轴,4进液孔,5旋转接头,6出流导管,7抽水泵,8驱动机构,9集水膜组元,10出液孔,11集水容腔,12安装头,13,紧固件,14固定件,15加强筋,16集液管保护罩。1 Water collection membrane assembly, 2 Liquid collection pipe, 3 Hollow shaft, 4 Liquid inlet hole, 5 Rotary joint, 6 Outflow conduit, 7 Water pump, 8 Driving mechanism, 9 Water collection membrane component, 10 Liquid outlet hole, 11 Water collecting cavity, 12 installation heads, 13, fasteners, 14 fixing parts, 15 reinforcing ribs, 16 protective covers for liquid collecting pipes.
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明作进一步说明,以使本领域的技术人员可以更好地理解本发明并能予以实施,但所举实施例不作为对本发明的限定。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments, so that those skilled in the art can better understand the present invention and implement it, but the examples given are not intended to limit the present invention.
实施例Example
本发明的集水系统的一实施例,如图1-3所示,本实施中的集水系统主要包括:集水膜组件1、集液管2、中空转轴3、旋转接头5、出流导管6、抽水泵7,在上述集水膜组件1周边设置有集液管2,上述集液管2安装在集液管保护罩16内部,中空转轴3与上述集液管2贯通,上述中空转轴3由驱动机构8驱动其旋转,上述驱动机构8可以是电机,上述中空转轴3带动整个上述集水膜组件1旋转;并且,在上述中空转轴3的一端连接至出流导管6上,上述出流导管6与抽水泵7相连。An embodiment of the water collection system of the present invention, as shown in Figures 1-3, the water collection system in this implementation mainly includes: a water collection membrane module 1, a liquid collection pipe 2, a hollow rotating shaft 3, a rotary joint 5, an outflow The conduit 6 and the water pump 7 are provided with a liquid collection pipe 2 around the water collection membrane assembly 1, and the liquid collection pipe 2 is installed inside the liquid collection pipe protective cover 16. The hollow rotating shaft 3 is connected with the above liquid collection pipe 2, and the above hollow The rotating shaft 3 is driven to rotate by a drive mechanism 8, the above-mentioned driving mechanism 8 can be a motor, and the above-mentioned hollow rotating shaft 3 drives the entire above-mentioned water collection membrane assembly 1 to rotate; and, one end of the above-mentioned hollow rotating shaft 3 is connected to the outlet conduit 6, the above-mentioned Outflow conduit 6 is connected with water pump 7 .
所述集水膜组件1环绕所述中空转轴3固定,构成旋转式集水膜转盘,在本实施例中,集水膜转盘可以是多边形结构,在其它实施例中也可以是圆形结构,所述驱动机构8通过所述中空转轴3带动所述集水膜组件1在水下进行浸没式或半浸没式旋转。The water collection membrane module 1 is fixed around the hollow rotating shaft 3 to form a rotating water collection membrane turntable. In this embodiment, the water collection membrane turntable can be a polygonal structure, and it can also be a circular structure in other embodiments. The driving mechanism 8 drives the water collection membrane module 1 to rotate submerged or semi-submerged underwater through the hollow rotating shaft 3 .
具体的,在本实施例中,上述集水膜组件1包括若干个集水膜组元9,上述集水膜组元9的一端设有出液孔10和集水容腔11,上述出液孔10与上述集水容腔11贯通,各个上述集水膜组元9的集水容腔11连接在一起形成水流通道,并且设置在上述集水膜组件1两端的上述集水容腔11与上述集液管2连接,上述集液管2与上述中空转轴3贯通。集水膜组件设有出液孔10和集水容腔11,无需另配集水管,一体化设计节省空间,降低成本。Specifically, in this embodiment, the above-mentioned water-collecting membrane assembly 1 includes several water-collecting membrane components 9, one end of the above-mentioned water-collecting membrane component 9 is provided with a liquid outlet hole 10 and a water-collecting chamber 11, and the above-mentioned liquid outlet The holes 10 communicate with the above-mentioned water-collecting chambers 11, and the water-collecting chambers 11 of each of the above-mentioned water-collecting membrane components 9 are connected together to form a water flow channel, and the above-mentioned water-collecting chambers 11 arranged at both ends of the above-mentioned water-collecting membrane assembly 1 are connected to the The above-mentioned liquid collecting pipe 2 is connected, and the above-mentioned liquid collecting pipe 2 is connected with the above-mentioned hollow rotating shaft 3 . The water-collecting membrane module is provided with a liquid outlet hole 10 and a water-collecting chamber 11, and no additional water-collecting pipe is required, and the integrated design saves space and reduces costs.
上述集液管2与中空转轴3贯通方式为:上述中空转轴3上开设有进液孔4,上述进液孔4与上述集液管2贯通。The liquid collecting pipe 2 and the hollow rotating shaft 3 are connected in such a way that: the hollow rotating shaft 3 is provided with a liquid inlet hole 4 , and the liquid inlet hole 4 is connected with the liquid collecting pipe 2 .
上述集水膜组元9的安装方式:上述集水膜组元9上设有安装头12,在上述集水膜组元9安装时,上述安装头12插入固定件14的安装孔中。集水膜组元9拆装方便,牢固可靠,当单个或几个集水膜组元损坏需要更换时,无需拆卸整组集水膜组件,拿下紧固件后可直接对损坏膜组元进行更换。The installation method of the above-mentioned water-collecting membrane unit 9: the above-mentioned water-collecting membrane unit 9 is provided with an installation head 12, and when the above-mentioned water-collection membrane unit 9 is installed, the above-mentioned installation head 12 is inserted into the installation hole of the fixing member 14. The water collection membrane unit 9 is easy to disassemble, firm and reliable. When a single or several water collection membrane units are damaged and need to be replaced, there is no need to disassemble the entire set of water collection membrane units. After taking off the fasteners, the damaged membrane unit can be directly repaired Make a replacement.
集水容腔略高于为支撑结构的主体,使得各集水膜组元安装时形成一定间距,间距范围为0.2~1.5cm,各集水膜组元具有一定间距及旋转式集水膜转盘为多边形结构,使得集水膜转盘在浸没式程控旋转运行时,形成强力冲刷效果,防止滤层累积,提高稳定膜通量,通过控制转速和抽停周期等操作状态,使膜表面产生足够的剪切力、离心力及滤液湍流等,达到理想的错流式操作和消除浓差极化效果。The water collection chamber is slightly higher than the main body of the supporting structure, so that each water collection membrane component forms a certain distance when installed, and the distance range is 0.2 to 1.5cm. Each water collection membrane component has a certain distance and a rotating water collection membrane turntable It is a polygonal structure, so that when the water collection membrane turntable is in the submerged program-controlled rotation operation, it forms a strong scouring effect, prevents the accumulation of the filter layer, and improves the stable membrane flux. Shear force, centrifugal force and filtrate turbulence, etc., to achieve ideal cross-flow operation and eliminate concentration polarization effect.
上述集水膜组元9采用中空腔式或表面导流沟槽式支撑结构,在上述支撑结构的两侧焊接超滤或微滤膜片,上述支撑结构为一体化注塑件。集水膜组元9采用中空腔式或表面导流沟槽式支撑结构,负压分配均匀,消除过滤死区,提高膜效率。并且,在上述集水膜组件1的两侧设有加强筋15,通过上述加强筋15加固集水膜组件1。The above-mentioned water-collecting membrane component 9 adopts a hollow cavity type or surface diversion groove type support structure, and ultrafiltration or microfiltration membranes are welded on both sides of the above-mentioned support structure, and the above-mentioned support structure is an integrated injection molded part. The water collection membrane component 9 adopts a hollow cavity type or a surface diversion groove type support structure, the negative pressure is evenly distributed, the dead zone of filtration is eliminated, and the membrane efficiency is improved. Moreover, reinforcing ribs 15 are provided on both sides of the water-collecting membrane module 1 , and the water-collecting membrane module 1 is reinforced by the reinforcing ribs 15 .
上述中空转轴3的一端连接有旋转接头5,通过上述旋转接头5连接至上述出流导管6上,上述中空转轴3的另一端为封闭状态。并且,上述中空转轴3的两端固定在轴承座上。One end of the hollow rotating shaft 3 is connected with a rotary joint 5, and is connected to the outlet conduit 6 through the rotary joint 5, and the other end of the hollow rotating shaft 3 is in a closed state. Moreover, both ends of the above-mentioned hollow rotating shaft 3 are fixed on the bearing housing.
具体使用时,抽水泵开启,使集水膜组元的两侧产生足够的压力差,原水在压差的作用下通过膜组元两侧焊接的超滤膜表面进入到中间的腔中经出液孔进入到汇水容腔,多个膜组元的汇水容腔相连形成水流通道汇入到集液管,最后通过进液孔流进中空转轴,再经出流导管和抽水泵排出。在过滤的同时,驱动机构带动中空中转轴转动,从而带动整个集水膜转盘转动,以错流过滤的方式实现膜分离。In specific use, the water pump is turned on to generate a sufficient pressure difference on both sides of the water-collecting membrane component. The liquid hole enters the water collection chamber, and the water collection chambers of multiple membrane components are connected to form a water flow channel to flow into the liquid collection pipe, and finally flow into the hollow shaft through the liquid inlet hole, and then discharge through the outlet conduit and the pump. While filtering, the driving mechanism drives the hollow rotating shaft to rotate, thereby driving the entire water collection membrane turntable to rotate, and the membrane separation is realized by means of cross-flow filtration.
具体应用过程中必要的场合和时段,该集水系统可反冲洗,通过备用导管或切换水泵抽吸方向,将净水或清洗液反向泵入中空转轴中,然后经进液孔进入集液管和集水容腔,继而通过出液孔导入到过集水膜组元的腔中,实现对集水膜组元的清洗,保持膜组元表面清洁。The water collection system can be backwashed in the necessary occasions and time periods during the specific application process, and the clean water or cleaning liquid can be reversely pumped into the hollow shaft through the standby conduit or the suction direction of the water pump, and then enter the liquid collection through the liquid inlet hole The pipe and the water collection chamber are then introduced into the cavity of the water collection membrane component through the liquid outlet hole, so as to realize the cleaning of the water collection membrane component and keep the surface of the membrane component clean.
以上所述实施例仅是为充分说明本发明而所举的较佳的实施例,本发明的保护范围不限于此。本技术领域的技术人员在本发明基础上所作的等同替代或变换,均在本发明的保护范围之内。本发明的保护范围以权利要求书为准。The above-mentioned embodiments are only preferred embodiments for fully illustrating the present invention, and the protection scope of the present invention is not limited thereto. Equivalent substitutions or transformations made by those skilled in the art on the basis of the present invention are all within the protection scope of the present invention. The protection scope of the present invention shall be determined by the claims.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810132293.7A CN108144448A (en) | 2018-02-09 | 2018-02-09 | A kind of collecting system for rotary film device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810132293.7A CN108144448A (en) | 2018-02-09 | 2018-02-09 | A kind of collecting system for rotary film device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108144448A true CN108144448A (en) | 2018-06-12 |
Family
ID=62457089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810132293.7A Pending CN108144448A (en) | 2018-02-09 | 2018-02-09 | A kind of collecting system for rotary film device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108144448A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607684A (en) * | 2019-01-07 | 2019-04-12 | 上海海事大学 | A rotary forward osmosis membrane sewage treatment device |
| CN110075717A (en) * | 2019-03-20 | 2019-08-02 | 雅安沃克林环保科技有限公司 | Reduce rotary filtering structure, the device and method of fouling membrane |
| CN114786797A (en) * | 2019-10-10 | 2022-07-22 | 南洋理工大学 | Reverse osmosis apparatus and method |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000157849A (en) * | 1998-11-24 | 2000-06-13 | Ishikawajima Harima Heavy Ind Co Ltd | Rotary membrane separation device |
| JP2004130260A (en) * | 2002-10-11 | 2004-04-30 | Nippon Rensui Co Ltd | Rotating flat membrane filter |
| CN2744398Y (en) * | 2004-11-04 | 2005-12-07 | 浙江欧美环境工程有限公司 | Immersion ditch type gas distributing hollow fiber membrane assembly |
| CN1762555A (en) * | 2005-09-23 | 2006-04-26 | 浙江大学 | Rotary Membrane Separator |
| CN1810351A (en) * | 2005-12-27 | 2006-08-02 | 天津膜天膜工程技术有限公司 | Membrane filter |
| CN101700472A (en) * | 2009-11-20 | 2010-05-05 | 苏州工业园区意诺克环境技术有限公司 | Rotary Membrane Separation Device and Its Application |
| CN202224070U (en) * | 2011-09-29 | 2012-05-23 | 厦门绿邦膜技术有限公司 | Disposable combined membrane component |
| KR20130015870A (en) * | 2011-08-05 | 2013-02-14 | 김백암 | Water treatment apparatus using the submerged hollow fiber membrane module |
| CN103316591A (en) * | 2013-07-10 | 2013-09-25 | 厦门市威士邦膜科技有限公司 | Fan-shaped rotary film separation device |
| CN104841277A (en) * | 2015-05-21 | 2015-08-19 | 苏州膜海分离技术有限公司 | Rotating cross-flow flat ceramic membrane separation turntable |
| CN208161371U (en) * | 2018-02-09 | 2018-11-30 | 苏州膜海分离技术有限公司 | A kind of collecting system for rotary film device |
-
2018
- 2018-02-09 CN CN201810132293.7A patent/CN108144448A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000157849A (en) * | 1998-11-24 | 2000-06-13 | Ishikawajima Harima Heavy Ind Co Ltd | Rotary membrane separation device |
| JP2004130260A (en) * | 2002-10-11 | 2004-04-30 | Nippon Rensui Co Ltd | Rotating flat membrane filter |
| CN2744398Y (en) * | 2004-11-04 | 2005-12-07 | 浙江欧美环境工程有限公司 | Immersion ditch type gas distributing hollow fiber membrane assembly |
| CN1762555A (en) * | 2005-09-23 | 2006-04-26 | 浙江大学 | Rotary Membrane Separator |
| CN1810351A (en) * | 2005-12-27 | 2006-08-02 | 天津膜天膜工程技术有限公司 | Membrane filter |
| CN101700472A (en) * | 2009-11-20 | 2010-05-05 | 苏州工业园区意诺克环境技术有限公司 | Rotary Membrane Separation Device and Its Application |
| KR20130015870A (en) * | 2011-08-05 | 2013-02-14 | 김백암 | Water treatment apparatus using the submerged hollow fiber membrane module |
| CN202224070U (en) * | 2011-09-29 | 2012-05-23 | 厦门绿邦膜技术有限公司 | Disposable combined membrane component |
| CN103316591A (en) * | 2013-07-10 | 2013-09-25 | 厦门市威士邦膜科技有限公司 | Fan-shaped rotary film separation device |
| CN104841277A (en) * | 2015-05-21 | 2015-08-19 | 苏州膜海分离技术有限公司 | Rotating cross-flow flat ceramic membrane separation turntable |
| CN208161371U (en) * | 2018-02-09 | 2018-11-30 | 苏州膜海分离技术有限公司 | A kind of collecting system for rotary film device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109607684A (en) * | 2019-01-07 | 2019-04-12 | 上海海事大学 | A rotary forward osmosis membrane sewage treatment device |
| CN110075717A (en) * | 2019-03-20 | 2019-08-02 | 雅安沃克林环保科技有限公司 | Reduce rotary filtering structure, the device and method of fouling membrane |
| CN114786797A (en) * | 2019-10-10 | 2022-07-22 | 南洋理工大学 | Reverse osmosis apparatus and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101700472B (en) | Rotary membrane separation device and application thereof | |
| CN107381907B (en) | Medical ultrapure water machine | |
| CN108144448A (en) | A kind of collecting system for rotary film device | |
| CN109607684A (en) | A rotary forward osmosis membrane sewage treatment device | |
| CN103316591B (en) | Fan-shaped rotary film separation device | |
| CN201586483U (en) | A New Rotary Membrane Separation Device | |
| CN219098834U (en) | RO reverse osmosis membrane water purification treatment device | |
| CN116495942A (en) | RO reverse osmosis filtered water treatment facilities | |
| CN106731853B (en) | A kind of ultra filtering reverse osmosis bi-membrane method energy recycling system | |
| CN113842780B (en) | Ultrafiltration filter equipment for combination frame pipeline | |
| CN212492422U (en) | Vortex type membrane separation device | |
| CN212151703U (en) | Wastewater treatment recovery unit based on prevent membrane pollution | |
| CN116462276A (en) | Water purifying device of graphene induced orientation gradient functional film | |
| CN218539373U (en) | High-efficient pure water preparation device | |
| CN208161371U (en) | A kind of collecting system for rotary film device | |
| CN219072600U (en) | Reverse osmosis sea water desalination equipment | |
| CN115770485B (en) | Anti-fouling reverse osmosis membrane assembly | |
| CN207805393U (en) | A kind of reverse osmosis equipment | |
| CN105727748A (en) | Rotary ultrafiltration deoiling device | |
| CN213231617U (en) | Multistage reverse osmosis wastewater treatment equipment | |
| CN114477372A (en) | High-performance reverse osmosis membrane module | |
| CN210097409U (en) | High-efficiency ultrafiltration backwashing device | |
| CN111450708A (en) | Vortex type membrane separation device and application | |
| CN108953166B (en) | Backwashing energy-saving pump system | |
| CN204768287U (en) | Dull and stereotyped ceramic membrane separation carousel of rotatory cross -flow formula |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information |
Inventor after: Geng Ce Inventor after: Wang Kun Inventor after: Geng Xiaolei Inventor after: Xing Shiyu Inventor after: Liu Qi Inventor after: Geng Anchao Inventor before: Geng Ce Inventor before: Wang Kun Inventor before: Geng Xiaolei Inventor before: Xing Shiyu Inventor before: Liu Qi Inventor before: Geng An |
|
| CB03 | Change of inventor or designer information | ||
| CB02 | Change of applicant information |
Address after: 215010 Room 102, building 15, No.158, Jinfeng Road, Suzhou hi tech Zone, Suzhou City, Jiangsu Province Applicant after: Suzhou Menghai Water Technology Co.,Ltd. Address before: 215153, No. 158, Jinsha River Road, hi tech Zone, Jiangsu, Suzhou Applicant before: SUZHOU MOHAI SEPARATION TECHNOLOGY Co.,Ltd. |
|
| CB02 | Change of applicant information | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180612 |
|
| RJ01 | Rejection of invention patent application after publication |