CN202724803U - Filter element of automatic cleaning membrane filter - Google Patents
Filter element of automatic cleaning membrane filter Download PDFInfo
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- CN202724803U CN202724803U CN201220415503.1U CN201220415503U CN202724803U CN 202724803 U CN202724803 U CN 202724803U CN 201220415503 U CN201220415503 U CN 201220415503U CN 202724803 U CN202724803 U CN 202724803U
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- inner support
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- petal
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- 239000012528 membrane Substances 0.000 title claims abstract description 31
- 238000004140 cleaning Methods 0.000 title claims abstract description 12
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 239000000178 monomer Substances 0.000 claims abstract description 5
- 239000007787 solid Substances 0.000 abstract description 7
- 238000001914 filtration Methods 0.000 description 12
- 238000011001 backwashing Methods 0.000 description 10
- 239000012065 filter cake Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000012535 impurity Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型涉及一种自清洗薄膜过滤器滤芯,它包括有:若干滤芯单体、出液管;所述滤芯单体由薄膜、内撑、升液管组成,内撑由若干呈柱状的中空管连体组成、呈花瓣式结构均布在升液管的外柱面上,内撑上底与升液管外缘密封连接,内撑下底封闭、内撑各中空管通过管底空间与升液管管底连通,内撑花瓣式外柱面上沿其轴线方向开有若干相隔一定间距的周向缝隙;所述薄膜制成滤筒状、罩在内撑花瓣式外柱面上,薄膜上、下两端与内撑密封连接,所述各个内撑的升液管密封连接在出液管上。本实用新型优点如下:本滤芯可成组使用,既可以过滤低悬浮物的液体,也可以过滤高悬浮物的液体,并可以收集、吹干该悬浮物,构成一种装填面积大,且反冲洗效果好。
The utility model relates to a filter core of a self-cleaning membrane filter, which comprises: a plurality of filter core monomers and liquid outlet pipes; The hollow tubes are composed of conjoined pieces, which are evenly distributed on the outer cylindrical surface of the riser in a petal-like structure. The upper bottom of the inner support is sealed and connected with the outer edge of the riser tube, the lower bottom of the inner support is closed, and the hollow tubes of the inner support pass through the bottom of the tube. The space is connected with the bottom of the riser pipe, and there are several circumferential slits at a certain distance along the axial direction on the inner support petal-type outer cylinder; On the top, the upper and lower ends of the film are sealed and connected to the inner support, and the liquid riser pipes of each inner support are sealed and connected to the liquid outlet pipe. The advantages of the utility model are as follows: the filter elements can be used in groups, can filter liquids with low suspended solids, and can also filter liquids with high suspended solids, and can collect and dry the suspended solids, forming a filter with a large filling area and a reverse filter. Rinse well.
Description
技术领域 technical field
本实用新型涉及一种分离技术,尤其涉及一种自清洗薄膜过滤器滤芯。 The utility model relates to a separation technology, in particular to a self-cleaning membrane filter element.
背景技术 Background technique
过滤是液固分离中重要的一个方法,对于大流量,大批量的液体过滤,多采用可以自动反冲洗的过滤器。目前自动反冲洗的过滤器主要有介质类过滤器,筛网类过滤器,纤维类过滤器,薄膜类过滤器等,每种过滤器都有其适用性。薄膜类过滤器作为主要的一种可清洗类过滤器在固液分离领域有着广泛的应用,薄膜过滤器过滤精度广,薄膜种类多。市面上常见的薄膜类的过滤器有多圆盘过滤器,转鼓过滤机等,该类过滤机一般都采用高压水冲洗再生,但为了满足清洗的要求,整体过滤器都不带压力运行,系统中薄膜装填面积小,系统占地大,反冲洗耗水量很大。滤饼的收集也困难。美国Aquatech 公司开发了一种薄膜滤盘过滤机,采用真空吸吮的方式反冲洗,大大的提高了薄膜装填面积,但真空吸吮的压力不超过1个大气压,对于一些比较粘的杂质很难实现有效的反冲洗。此外,该过滤机只能适用于水体过滤,不能收集滤饼。 国内也有人尝试将薄膜罩在多孔的内衬上形成烛式过滤器,但实践发现反冲洗效果非常差,也不能很好收集滤饼。基于目前的现状,本发明人认为开发出一种装填面积大,并能够高效反冲洗和有效收集滤饼的自清洗薄膜过滤器将有很大的市场前景。 Filtration is an important method in liquid-solid separation. For large-flow and large-volume liquid filtration, filters that can be automatically backwashed are often used. At present, the filters for automatic backwashing mainly include media filters, screen filters, fiber filters, film filters, etc., and each filter has its applicability. Membrane filters, as the main type of washable filters, are widely used in the field of solid-liquid separation. Membrane filters have a wide range of filtration precision and various types of membranes. Common membrane filters on the market include disc filters, drum filters, etc. These filters are generally washed and regenerated with high-pressure water, but in order to meet the cleaning requirements, the overall filter does not operate under pressure. The film filling area in the system is small, the system occupies a large area, and the water consumption for backwashing is large. Filter cake collection is also difficult. The American Aquatech company has developed a membrane filter disc filter, which uses vacuum suction to backwash, which greatly increases the membrane filling area, but the vacuum suction pressure does not exceed 1 atmosphere, and it is difficult to achieve effective filtration for some sticky impurities. backwash. In addition, the filter is only suitable for water filtration and cannot collect filter cakes. Some people in China also tried to cover the membrane on the porous lining to form a candle filter, but it was found that the backwashing effect was very poor and the filter cake could not be collected well. Based on the current situation, the inventor believes that developing a self-cleaning membrane filter with a large filling area, high-efficiency backwashing and effective collection of filter cakes will have a great market prospect.
实用新型内容 Utility model content
本实用新型的目的是针对现有技术不足之处而提供一种自清洗薄膜过滤器滤芯。该过滤器滤芯可以过滤含有悬浮物的液体,降低滤液中的悬浮物,也可以收集悬浮物滤饼。 The purpose of the utility model is to provide a self-cleaning membrane filter element for the deficiencies of the prior art. The filter element can filter the liquid containing suspended matter, reduce the suspended matter in the filtrate, and can also collect the suspended matter filter cake.
本实用新型通过以下技术方案于以实现:一种自清洗薄膜过滤器滤芯,其特征在于,它包括有若干滤芯单体、出液管;所述滤芯单体由薄膜、内撑、升液管组成,内撑由若干呈柱状的中空管连体组成、呈花瓣式结构均布在升液管的外柱面上,内撑上底与升液管外缘密封连接,内撑下底封闭、内撑各中空管通过管底空间与升液管管底连通,内撑花瓣式外柱面上沿其轴线方向开有若干相隔一定间距的周向缝隙;所述薄膜制成滤筒状、罩在内撑花瓣式外柱面上,薄膜上、下两端与内撑密封连接,所述各个内撑的升液管密封连接在出液管上。
The utility model is realized through the following technical solutions: a self-cleaning membrane filter element, which is characterized in that it includes several filter element monomers and liquid outlet pipes; The inner support is composed of a number of cylindrical hollow tubes, and the petal structure is evenly distributed on the outer cylindrical surface of the liquid riser. The upper bottom of the inner support is sealed and connected with the outer edge of the liquid riser, and the lower bottom of the inner support is closed. Each hollow tube of the inner support communicates with the bottom of the riser pipe through the space at the bottom of the tube, and there are several circumferential slits at certain intervals on the outer cylinder of the inner support petals along the axis direction; the film is made into a
所述内撑花瓣式外柱面上布有竖向沟槽。 Vertical grooves are arranged on the inner support petal-shaped outer cylinder surface.
本实用新型的积极效果是:本实用新型提出的一种自清洗薄膜过滤器滤芯,具有如下优点:薄膜在过滤压差的作用下紧贴在花瓣式内撑柱面上,利用柱面上众多的沟槽及周向缝隙收集薄膜过滤下来的液体;反洗时薄膜在反冲洗水或气的作用下快速膨胀为圆周状,附在薄膜上的杂质在反冲洗压力和薄膜膨胀力作用下被清洗干净。本滤芯可成组使用安装在过滤器上,既可以过滤低悬浮物的液体,也可以过滤高悬浮物的液体,并可以收集、吹干该悬浮物,构成一种装填面积大,反冲洗效果好,并能有效回收滤饼的自清洗薄膜过滤器,具有很大的市场前景。 The positive effects of the utility model are: a self-cleaning membrane filter element proposed by the utility model has the following advantages: the membrane is closely attached to the surface of the petal-type inner support cylinder under the action of the filter pressure difference, and many The grooves and circumferential gaps collect the liquid filtered by the membrane; during backwashing, the membrane rapidly expands into a circular shape under the action of backwash water or air, and the impurities attached to the membrane are removed under the action of backwash pressure and membrane expansion force. Clean up. The filter elements can be used in groups and installed on the filter, which can filter liquids with low suspended solids and liquids with high suspended solids, and can collect and dry the suspended solids, forming a large filling area and backwashing effect. Good, and the self-cleaning membrane filter that can effectively recover the filter cake has great market prospects.
附图说明 Description of drawings
图1为本实用新型一个实施例安装在过滤器内的结构剖面示意图。 Fig. 1 is a schematic cross-sectional view of an embodiment of the utility model installed in a filter.
图2为图1 A部放大图。 Figure 2 is an enlarged view of part A of Figure 1.
图3为滤芯在过滤状态下的截面示意图。 Fig. 3 is a schematic cross-sectional view of the filter element in a filtering state.
图4为滤芯在反洗状态下的截面示意图。 Fig. 4 is a schematic cross-sectional view of the filter element in a backwashing state.
下面结合实施例对本实用新型作进一步的描述: Below in conjunction with embodiment the utility model is further described:
图1~图2为本实用新型一个实施例安装在过滤器内的结构剖面示意图。图中,一种自清洗薄膜过滤器滤芯,它包括有:若干滤芯单体1、出液管3;所述滤芯单体由薄膜11、内撑12、升液管13组成,内撑12由若干呈柱状的中空管连体组成、呈花瓣式结构均布在升液管13的外柱面上,本实施例中花瓣数为六瓣,内撑12上底与升液管13外缘密封连接,内撑12下底封闭、内撑12各中空管通过管底空间与升液管13管底连通,内撑12花瓣式外柱面上沿其轴线方向开有若干相隔一定间距的周向缝隙14;所述薄膜11制成滤筒状、罩在内撑12花瓣式外柱面上,薄膜11上、下两端与内撑12密封连接,所述各个内撑12的升液管密封连接在出液管3上。
Figures 1 to 2 are schematic cross-sectional views of an embodiment of the utility model installed in a filter. In the figure, a self-cleaning membrane filter element, it includes: several
本实用新型进一步采取如下措施:所述内撑花瓣式外柱面上布有竖向沟槽15。
The utility model further adopts the following measures:
本实用新型是这样工作的: The utility model works like this:
过滤过程如图3所示,液体由过滤芯的外部透过薄膜,汇集到内撑上的沟槽,并依次通过细缝,花瓣中空管内管,升液管,最后由升液管上端流出。薄膜在过滤压差的作用下紧贴花瓣内撑也呈花瓣状,液体中的颗粒被拦截在薄膜表面。 可以选择不同型号的薄膜以满足对过滤精度,过滤温度,过滤介质的需要。 The filtration process is shown in Figure 3. The liquid passes through the membrane from the outside of the filter element, collects into the groove on the inner support, and passes through the slits, the inner tube of the petal hollow tube, the riser tube, and finally flows out from the upper end of the riser tube. Under the action of the filter pressure difference, the membrane clings to the inner support of the petals and is also petal-shaped, and the particles in the liquid are intercepted on the surface of the membrane. Different types of membranes can be selected to meet the needs of filtration accuracy, filtration temperature, and filtration media.
反冲洗过程如图4所示:当压差或时间达到设定值时反冲洗液体在液压或气压的作用下由升液管上部向下高速流动, 通过花瓣中空管内管,细缝快速并均匀反冲洗薄膜。 薄膜在反冲洗水或气的作用下,由花瓣状快速膨胀为圆周状,杂质在反冲洗压力和薄膜膨胀力作用下被清洗干净,各组滤液管可依次反冲洗,反冲洗时还可加入助滤剂,以助滤剂在薄膜上形成滤饼过滤,提高过滤精度。 The backwash process is shown in Figure 4: when the pressure difference or time reaches the set value, the backwash liquid flows downward at high speed from the upper part of the riser tube under the action of hydraulic pressure or air pressure, and passes through the inner tube of the petal hollow tube, and the slit is fast and uniform Backwash membrane. Under the action of backwashing water or air, the membrane rapidly expands from a petal shape to a circular shape. Impurities are cleaned under the action of backwashing pressure and membrane expansion force. Each group of filtrate tubes can be backwashed in turn, and can be added during backwashing. Filter aid, use filter aid to form a filter cake on the membrane for filtration to improve filtration accuracy.
上面结合附图及实施例描述了本实用新型的实施方式,实施例给出的结构并不构成对本实用新型的限制,本领域内熟练的技术人员可依据实示需要做出调整,在所附权利要求的范围内做出各种变形或修改均在保护范围内。 The above describes the implementation of the utility model in conjunction with the accompanying drawings and the examples. The structure given in the examples does not constitute a limitation to the utility model. Those skilled in the art can make adjustments according to the actual needs. Various changes or modifications within the scope of the claims are within the scope of protection.
Claims (2)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220415503.1U CN202724803U (en) | 2012-08-21 | 2012-08-21 | Filter element of automatic cleaning membrane filter |
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| CN201220415503.1U CN202724803U (en) | 2012-08-21 | 2012-08-21 | Filter element of automatic cleaning membrane filter |
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| CN202724803U true CN202724803U (en) | 2013-02-13 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463988A (en) * | 2013-07-24 | 2013-12-25 | 乐金电子研发中心(上海)有限公司 | Self-cleaning MBR flat sheet membrane module and cleaning method thereof |
| CN107261626A (en) * | 2017-06-07 | 2017-10-20 | 常州兆威不锈钢有限公司 | A kind of cobalt hydroxide slurry filtration wash unit |
| CN108310834A (en) * | 2017-01-18 | 2018-07-24 | 黄学锋 | Three-level backwashing system and purging method |
-
2012
- 2012-08-21 CN CN201220415503.1U patent/CN202724803U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463988A (en) * | 2013-07-24 | 2013-12-25 | 乐金电子研发中心(上海)有限公司 | Self-cleaning MBR flat sheet membrane module and cleaning method thereof |
| CN103463988B (en) * | 2013-07-24 | 2015-09-23 | 乐金电子研发中心(上海)有限公司 | Self-cleaning MBR flat sheet membrane module and cleaning method thereof |
| CN108310834A (en) * | 2017-01-18 | 2018-07-24 | 黄学锋 | Three-level backwashing system and purging method |
| CN107261626A (en) * | 2017-06-07 | 2017-10-20 | 常州兆威不锈钢有限公司 | A kind of cobalt hydroxide slurry filtration wash unit |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| 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: 20130213 Termination date: 20200821 |
