CN201020345Y - Submerged columnar hollow fiber membrane module - Google Patents
Submerged columnar hollow fiber membrane module Download PDFInfo
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- CN201020345Y CN201020345Y CNU2007200954867U CN200720095486U CN201020345Y CN 201020345 Y CN201020345 Y CN 201020345Y CN U2007200954867 U CNU2007200954867 U CN U2007200954867U CN 200720095486 U CN200720095486 U CN 200720095486U CN 201020345 Y CN201020345 Y CN 201020345Y
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- hollow fiber
- distributor
- fiber bundle
- membrane module
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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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Abstract
一种用于水净化与污水处理的浸入式柱状中空纤维膜组件。中空纤维束的一端密封并固结在端头内,端头内中空纤维束之间的端面上形成一组与膜组件内部混合液流动通道连通的导流孔;中空纤维束的另一端通过加强分布器分割成纤维束簇,并与罗筒固结,各纤维束簇之间形成混合液流动通道,在端头与加强分布器之间至少设置有一根支撑杆;罗筒外安装其上设有渗透液出口的封头。该膜组件不含外壳,直接浸入含混合液的槽体内,通过抽吸作用产生透过液。其特点是可实现混合液分布均匀,膜组件的就地清洗,无死角,可防止纤维之间的粘连,系统易于管理和维修,过滤性能稳定。可应用于水净化与膜生物反应器。
A submerged columnar hollow fiber membrane module used for water purification and sewage treatment. One end of the hollow fiber bundle is sealed and consolidated in the end, and a group of diversion holes is formed on the end surface between the hollow fiber bundles in the end to communicate with the mixed liquid flow channel inside the membrane module; the other end of the hollow fiber bundle is reinforced by The distributor is divided into fiber bundle clusters, and consolidated with the drum, the mixed liquid flow channel is formed between each fiber bundle cluster, and at least one support rod is arranged between the end and the reinforced distributor; Head with permeate outlet. The membrane module does not contain a shell, and is directly immersed in the tank containing the mixed liquid, and the permeate is generated by suction. Its characteristics are that it can realize the uniform distribution of the mixed liquid, clean the membrane modules in place, have no dead angle, prevent the adhesion between fibers, the system is easy to manage and maintain, and the filtration performance is stable. It can be applied to water purification and membrane bioreactors.
Description
【技术领域】【Technical field】
本实用新型属于对水或者液体介质的过滤或者净化处理技术领域,特别涉及一种用于水净化与污水处理的浸入式柱状中空纤维膜组件,特别适用于膜生物反应器。The utility model belongs to the technical field of filtration or purification treatment of water or liquid media, in particular relates to an immersed columnar hollow fiber membrane module for water purification and sewage treatment, and is especially suitable for membrane bioreactors.
【背景技术】【Background technique】
目前,中空纤维膜已经广泛用于对水或者液体介质的过滤或者净化处理。原水透过中空纤维膜的微孔渗透而成为净水。市场上广泛使用的是带有外壳的芯-壳式膜组件,近几年来发展了浸入式膜组件,它的特点是膜组件无外壳,将膜组件直接放入含待分离液的容器内,通过抽吸作用达到产生渗透液的目的。使用中,原水中的悬浮微粒不断集中于中空纤维膜表面,造成效率降低,因此,需要进行清洗。用于膜生物反应器的中空纤维膜组件主要采用浸入帘式膜组件,存在气液分布不均,中空纤维易被污泥粘连,清洗操作繁琐,难以就地清洗,中空纤维膜组件修补维护困难,中空纤维膜易被异物损坏,从而造成膜的使用寿命降低。At present, hollow fiber membranes have been widely used to filter or purify water or liquid media. Raw water permeates through the micropores of the hollow fiber membrane to become purified water. The core-shell membrane module with a shell is widely used in the market. In recent years, the submerged membrane module has been developed. It is characterized in that the membrane module has no shell, and the membrane module is directly placed in the container containing the liquid to be separated. The purpose of generating permeate is achieved by suction. During use, the suspended particles in the raw water are continuously concentrated on the surface of the hollow fiber membrane, resulting in a decrease in efficiency. Therefore, cleaning is required. Hollow fiber membrane modules used in membrane bioreactors mainly adopt immersion curtain membrane modules, which have uneven distribution of gas and liquid, hollow fibers are easily adhered by sludge, cumbersome cleaning operations, difficult to clean in situ, and difficult to repair and maintain hollow fiber membrane modules , The hollow fiber membrane is easily damaged by foreign matter, resulting in a reduction in the service life of the membrane.
【发明内容】【Content of invention】
本实用新型的目的是解决现有技术存在的上述不足,提供一种浸入式柱状中空纤维膜组件。The purpose of the utility model is to solve the above-mentioned deficiencies in the prior art, and provide a submerged columnar hollow fiber membrane module.
本实用新型提供的浸入式柱状中空纤维膜组件,包括中空纤维束、端头、和罗筒,中空纤维束的一端密封而分散的固结在端头内,端头内中空纤维束之间的端面上形成一组与膜组件内部混合液流动通道连通的导流孔;中空纤维束的另一端通过加强分布器分割成纤维束簇,并与罗筒固结,各纤维束簇之间形成混合液流动通道,在端头与加强分布器之间至少设置有一根支撑杆;罗筒外安装其上设有渗透液出口和反洗液入口的封头,罗筒与封头之间由快装卡环锁紧联接。The submerged columnar hollow fiber membrane module provided by the utility model includes hollow fiber bundles, ends, and sleeves, one end of the hollow fiber bundles is sealed and dispersedly consolidated in the ends, and the hollow fiber bundles in the ends are A group of diversion holes is formed on the end surface to communicate with the flow channel of the mixed liquid inside the membrane module; the other end of the hollow fiber bundle is divided into fiber bundle clusters by a reinforcing distributor, and consolidated with the drum, and a mixture is formed between each fiber bundle cluster. There is at least one support rod between the end and the reinforced distributor; the head with the permeate outlet and the backwash liquid inlet is installed outside the cylinder, and the quick-installed The snap ring locks the connection.
加强分布器由分布板与支撑杆定位槽构成,分布板可以呈放射状分布,分布板数量为4至16片。加强分布器内的分布板也可以呈网状分布。The reinforced distributor is composed of a distribution plate and a support rod positioning groove. The distribution plate can be distributed radially, and the number of distribution plates is 4 to 16. The distribution plates in the reinforced distributor can also be distributed in a net shape.
工作过程是:料液在气体的作用下,从膜组件一端导流孔均匀流入膜组件内,在组件的顶部流出,在抽吸作用下透过液经过中空纤维膜的外表面透过膜的孔隙并进入中空纤维内腔流出,实现了料液的过滤分离过程。The working process is: under the action of gas, the feed liquid flows into the membrane module evenly from the diversion hole at one end of the membrane module, flows out at the top of the module, and the permeate passes through the outer surface of the hollow fiber membrane under the action of suction. The pores and enter the cavity of the hollow fiber to flow out, realizing the filtration and separation process of the feed liquid.
本实用新型的优点和积极效果:Advantage and positive effect of the utility model:
本实用新型可实现料液(包含液体与气体)分布均匀,提高了膜的运行与清洗效率,膜组件可拆卸,可以就地清洗,可防止纤维之间的粘连,系统易于管理和维修,过滤性能稳定。The utility model can realize uniform distribution of feed liquid (including liquid and gas), and improve the operation and cleaning efficiency of the membrane. Stable performance.
【附图说明】【Description of drawings】
图1是中空纤维膜组件总体结构图,Figure 1 is a general structural diagram of a hollow fiber membrane module,
图2是导流板的端面侧视图,Figure 2 is a side view of the end face of the deflector,
图3是分布器的端面侧视图。Figure 3 is an end side view of the distributor.
【具体实施方式】【Detailed ways】
如图1所示,该浸入式柱状中空纤维膜组件包括中空纤维束1,中空纤维束1的一端用树脂密封而分散的浇铸在端头5内,端头内中空纤维束之间的端面上形成一组与膜组件内部混合液流动通道9连通的导流孔12,端头及其内部中空纤维束端面一起构成混合液导流板2。中空纤维束的另一端通过加强分布器3分割成纤维束簇,并通过树脂与罗筒6浇铸粘结,各纤维束簇之间形成混合液流动通道9,此端的纤维端口被切开,用于产出渗透液。在端头与加强分布器之间至少设置有一根支撑杆4(本例为两根支撑杆);罗筒6外安装其上设有渗透液出口10和反洗液入口11的封头7,罗筒与封头之间由快装卡环8锁紧联接。As shown in Figure 1, the submerged columnar hollow fiber membrane module includes a
如图2所示,导流板2是由多个导流孔12构成,导流孔的分布密度为500-2000个/m2,孔的直径为5-20mm。As shown in FIG. 2 , the
如图3所示,分布器3由放射状分布板13与支撑杆定位槽14构成,分布板数量为4至16片,形式有多种。该分布器用于均匀地分割纤维束。As shown in FIG. 3 , the
加强分布器内的分布板也可以呈网状分布(图略)。The distribution plates in the reinforced distributor can also be distributed in a net shape (figure omitted).
该膜组件不含外壳材料,直接浸入含混合液的槽体内,通过抽吸作用产生透过液。The membrane module does not contain shell material, and is directly immersed in the tank containing the mixed liquid, and the permeate is generated by suction.
工作过程:料液在气体的作用下,从膜组件一端导流孔12中均匀流入膜组件内,在组件的顶部流出,在抽吸作用下渗透液经过中空纤维膜的外表面透过膜的孔隙并进入中空纤维内腔流出,并在封头腔内汇集,从渗透液出口10流出。当膜组件需要反洗操作时反洗液从封头侧面反洗液入口11进入膜组件内。Working process: Under the action of gas, the feed liquid flows into the membrane module evenly from the
Claims (7)
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CNU2007200954867U CN201020345Y (en) | 2007-03-14 | 2007-03-14 | Submerged columnar hollow fiber membrane module |
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CNU2007200954867U CN201020345Y (en) | 2007-03-14 | 2007-03-14 | Submerged columnar hollow fiber membrane module |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103328078A (en) * | 2011-01-04 | 2013-09-25 | 三菱丽阳株式会社 | Hollow fiber membrane module |
CN103611421A (en) * | 2013-11-28 | 2014-03-05 | 苏州中色德源环保科技有限公司 | Immersed type ultra-filtration membrane assembly |
CN105879689A (en) * | 2016-05-26 | 2016-08-24 | 天邦膜技术国家工程研究中心有限责任公司 | A detachable internal pressure double-sealed membrane separator |
CN106955598A (en) * | 2017-04-21 | 2017-07-18 | 江苏坤奕环境工程有限公司 | The open runner network pipe type high pressure reverse osmosis membrane assembly of super-pressure |
-
2007
- 2007-03-14 CN CNU2007200954867U patent/CN201020345Y/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103328078A (en) * | 2011-01-04 | 2013-09-25 | 三菱丽阳株式会社 | Hollow fiber membrane module |
CN103611421A (en) * | 2013-11-28 | 2014-03-05 | 苏州中色德源环保科技有限公司 | Immersed type ultra-filtration membrane assembly |
CN105879689A (en) * | 2016-05-26 | 2016-08-24 | 天邦膜技术国家工程研究中心有限责任公司 | A detachable internal pressure double-sealed membrane separator |
CN106955598A (en) * | 2017-04-21 | 2017-07-18 | 江苏坤奕环境工程有限公司 | The open runner network pipe type high pressure reverse osmosis membrane assembly of super-pressure |
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Granted publication date: 20080213 |