CN104925901A - Sewage treatment device applying membrane technology - Google Patents

Sewage treatment device applying membrane technology Download PDF

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Publication number
CN104925901A
CN104925901A CN201510278205.0A CN201510278205A CN104925901A CN 104925901 A CN104925901 A CN 104925901A CN 201510278205 A CN201510278205 A CN 201510278205A CN 104925901 A CN104925901 A CN 104925901A
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membrane
membrane module
liquid
waste disposal
disposal plant
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李兴
徐效清
王勇
勾芒芒
秦福莹
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Inner Mongolia Normal University
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Inner Mongolia Normal University
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Abstract

本发明公开了一种应用膜技术的污水处理装置,包括外壳和触控器,外壳的一端设有进液管,进液管上设置有第一抽液泵,外壳内串联设置有第一膜组件、第二膜组件和第三膜组件,每个膜组件的前侧设置一个回流管,回流管上设置电控开关阀,回流管上设置第二抽液泵,第一膜组件、第二膜组件和第三膜组件的进水侧设置有压力传感器和负压吸嘴,负压吸嘴连接在伸缩杆上,第一膜组件、第二膜组件和第三膜组件均包括由空心圆柱支撑体组成支撑板,在支撑板一侧覆盖的膜。本发明污水处理效果好,实现了回流液自动收集再利用的功能,提高了过滤比率,缩短了维护时间,同时使用寿命长。

The invention discloses a sewage treatment device using membrane technology, which includes a casing and a touch controller, one end of the casing is provided with a liquid inlet pipe, a first liquid suction pump is arranged on the liquid inlet pipe, and a first membrane is arranged in series in the casing module, the second membrane module and the third membrane module, a return pipe is arranged on the front side of each membrane module, an electronically controlled on-off valve is arranged on the return pipe, a second pump is arranged on the return pipe, the first membrane module, the second The water inlet side of the membrane module and the third membrane module is provided with a pressure sensor and a negative pressure nozzle, and the negative pressure nozzle is connected to the telescopic rod. The support body constitutes a support plate, and the membrane is covered on one side of the support plate. The invention has good sewage treatment effect, realizes the function of automatic collection and reuse of reflux liquid, improves filtration rate, shortens maintenance time and has long service life.

Description

一种应用膜技术的污水处理装置A sewage treatment device using membrane technology

技术领域 technical field

本发明涉及污水处理领域,具体涉及一种应用膜技术的污水处理装置。 The invention relates to the field of sewage treatment, in particular to a sewage treatment device using membrane technology.

背景技术 Background technique

水资源不仅是基础性的自然资源,也是战略性的经济资源,现代社会的进步和发展离不开水资源。随着城市人口的增加和工农业生产的发展,工业污水和城市生活用水排放量也日益增大,远远超过了环境的自净能力,使得水体污染日益严重。随着水资源的不断紧缺和对环境污染治理的不断加强,人们已经开始关注对城市医院产生的污水进行专项治理工作。 Water resources are not only basic natural resources, but also strategic economic resources. The progress and development of modern society cannot be separated from water resources. With the increase of urban population and the development of industrial and agricultural production, the discharge of industrial sewage and urban domestic water is also increasing, far exceeding the self-purification capacity of the environment, making water pollution increasingly serious. With the continuous shortage of water resources and the continuous strengthening of environmental pollution control, people have begun to pay attention to the special treatment of sewage generated by urban hospitals.

在国际中,超滤膜技术已得到了广泛应用,我国的超滤膜技术有了很大的进展,膜技术已在许多领域中得到广泛地应用,被公认为是当代最有发展前途的高新技术之一。 In the world, ultrafiltration membrane technology has been widely used. my country's ultrafiltration membrane technology has made great progress. Membrane technology has been widely used in many fields and is recognized as the most promising high-tech technology in the contemporary era. One of the techniques.

现有净水器按水质处理方式多为超滤、纳滤、活性碳吸附等,当一种工艺难以去除水中有害物质时,采用二种或两种以上的工艺即为复合型;如活性炭吸附结合纳透、活性炭吸附结合超过滤、聚丙烯超细纤维结合活性炭结合超过滤等;在复合型净水器中,膜技术复合净水器净水性能优良,特别在去除微生物(细菌、藻类等)方面有比较显著的效果,其中一些品质优良的净水器出水可以直接生饮,得到了广大消费者的欢迎,已成为净水器当前发展的热点。 Existing water purifiers are mostly ultrafiltration, nanofiltration, activated carbon adsorption, etc. according to water quality treatment methods. When one process is difficult to remove harmful substances in water, two or more processes are used to be a composite type; such as activated carbon adsorption Combined with nanofiltration, activated carbon adsorption combined with ultrafiltration, polypropylene ultrafine fiber combined with activated carbon combined with ultrafiltration, etc.; among composite water purifiers, membrane technology composite water purifiers have excellent water purification performance, especially in the removal of microorganisms (bacteria, algae, etc. ) has a more significant effect. Some of the high-quality water purifiers can directly drink raw water, which has been welcomed by consumers and has become a hot spot in the current development of water purifiers.

发明内容 Contents of the invention

为解决上述问题,本发明提供了一种应用膜技术的污水处理装置,污水处理效果好,实现了回流液自动收集再利用的功能,提高了过滤比率,缩短了维护时间,同时使用寿命长。 In order to solve the above problems, the present invention provides a sewage treatment device using membrane technology, which has good sewage treatment effect, realizes the function of automatic collection and reuse of reflux liquid, improves the filtration rate, shortens maintenance time, and has a long service life.

为实现上述目的,本发明采取的技术方案为: In order to achieve the above object, the technical scheme that the present invention takes is:

一种应用膜技术的污水处理装置,包括外壳和触控器,外壳的一端设有进液管,进液管上设置有第一抽液泵,外壳内串联设置有第一膜组件、第二膜组件和第三膜组件,每个膜组件的前侧设置一个回流管,回流管上设置电控开关阀,回流管上设置第二抽液泵,第一膜组件、第二膜组件和第三膜组件的进水侧设置有压力传感器和负压吸嘴,负压吸嘴连接在伸缩杆上,第一膜组件、第二膜组件和第三膜组件均包括由空心圆柱支撑体组成支撑板,在支撑板一侧覆盖的膜,以及在膜的边缘设置有密封压环,负压吸嘴紧贴膜设置;膜由下列质量份数的原料组成: A sewage treatment device using membrane technology, including a casing and a touch controller, one end of the casing is provided with a liquid inlet pipe, a first liquid suction pump is arranged on the liquid inlet pipe, and a first membrane module, a second membrane module, and a second Membrane module and the third membrane module, a return pipe is arranged on the front side of each membrane module, an electric control switch valve is arranged on the return pipe, a second liquid suction pump is arranged on the return pipe, the first membrane module, the second membrane module and the second membrane module The water inlet side of the three-membrane module is provided with a pressure sensor and a negative pressure nozzle, and the negative pressure nozzle is connected to the telescopic rod. plate, a film covered on one side of the support plate, and a sealing pressure ring is arranged on the edge of the film, and the negative pressure nozzle is set close to the film; the film is composed of the following raw materials in parts by mass:

聚偏氟乙烯20-30份、聚砜酰胺聚20-30、乙烯吡咯烷酮3-9份、聚丙烯腈6-12份、聚乙二醇5-20份、碳纳米管0.08-0.52份; 20-30 parts of polyvinylidene fluoride, 20-30 parts of polysulfoneamide, 3-9 parts of vinylpyrrolidone, 6-12 parts of polyacrylonitrile, 5-20 parts of polyethylene glycol, 0.08-0.52 parts of carbon nanotubes;

外壳1的另一端通过管道连接有陶瓷膜过滤器,陶瓷膜过滤器内设置有螺旋盘管,螺旋盘管内壁设置有吸附网,螺旋盘管的末端设置有陶瓷过滤膜,螺旋盘管上连接有反洗进水管和反洗出水管。 The other end of the casing 1 is connected to a ceramic membrane filter through a pipeline, and a spiral coil is arranged inside the ceramic membrane filter, and the inner wall of the spiral coil is provided with an adsorption net, and the end of the spiral coil is provided with a ceramic filter membrane, and the spiral coil is connected to There are backwash inlet pipes and backwash outlet pipes.

优选的,所述陶瓷膜过滤器下端设有出液口。 Preferably, a liquid outlet is provided at the lower end of the ceramic membrane filter.

优选的,所述负压吸嘴为锥形,开口处的内径与底部的内径之比为1∶5。 Preferably, the negative pressure nozzle is tapered, and the ratio of the inner diameter of the opening to the inner diameter of the bottom is 1:5.

优选的,所述陶瓷过滤膜采用二氧化硅陶瓷过滤膜。 Preferably, the ceramic filter membrane is a silica ceramic filter membrane.

优选的,所述触控器与所述第一抽液泵、第二抽液和电控开关阀之间设置通讯连接。 Preferably, a communication connection is provided between the touch controller and the first liquid suction pump, the second liquid suction, and the electronically controlled on-off valve.

优选的,所述第一膜组件、第二膜组件和第三膜组件两侧设有密封卡槽。 Preferably, sealing grooves are provided on both sides of the first membrane module, the second membrane module and the third membrane module.

优选的,所述第一膜组件、第二膜组件和第三膜组件过滤精度从进液端到出液端依次增大。 Preferably, the filtration precision of the first membrane module, the second membrane module and the third membrane module increases sequentially from the liquid inlet end to the liquid outlet end.

优选的,所述触控器的芯片采用单片机。 Preferably, the chip of the touch controller adopts a single-chip microcomputer.

优选的,所述出液口上设有阀门。 Preferably, the liquid outlet is provided with a valve.

本发明具有以下有益效果: The present invention has the following beneficial effects:

污水处理效果好,实现了回流液自动收集再利用的功能,提高了杂质过滤 比率,缩短了维护时间,同时使用寿命长。 The sewage treatment effect is good, the function of automatic collection and reuse of the reflux liquid is realized, the impurity filtration rate is improved, the maintenance time is shortened, and the service life is long.

附图说明 Description of drawings

图1为本发明实施例一种应用膜技术的污水处理装置的结构示意图。 Fig. 1 is a schematic structural view of a sewage treatment device using membrane technology according to an embodiment of the present invention.

图2为图1中第一膜组件、第二膜组件和第三膜组件的内部结构示意图。 Fig. 2 is a schematic diagram of the internal structure of the first membrane module, the second membrane module and the third membrane module in Fig. 1 .

具体实施方式 Detailed ways

为了使本发明的目的及优点更加清楚明白,以下结合实施例对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。 In order to make the objects and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the examples. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

如图1-2所示,本发明实施例提供了一种应用膜技术的污水处理装置,包括外壳1和触控器2,外壳1的一端设有进液管4,进液管4上设置有第一抽液泵6,外壳1内串联设置有第一膜组件16、第二膜组件17和第三膜组件18,每个膜组件7的前侧设置一个回流管8,回流管8上设置电控开关阀9,回流管8上设置第二抽液泵10,第一膜组件16、第二膜组件17和第三膜组件18的进水侧设置有压力传感器12和负压吸嘴20,负压吸嘴20连接在伸缩杆19上,第一膜组件16、第二膜组件17和第三膜组件18均包括由空心圆柱支撑体21组成支撑板22,在支撑板22一侧覆盖的膜23,以及在膜23的边缘设置有密封压环24,负压吸嘴20紧贴膜23设置;膜23由下列质量份数的原料组成: As shown in Figure 1-2, the embodiment of the present invention provides a sewage treatment device using membrane technology, including a housing 1 and a touch controller 2, one end of the housing 1 is provided with a liquid inlet pipe 4, and the liquid inlet pipe 4 is set There is a first liquid suction pump 6, a first membrane module 16, a second membrane module 17 and a third membrane module 18 are arranged in series in the casing 1, and a return pipe 8 is arranged on the front side of each membrane module 7, and on the return pipe 8 An electronically controlled switch valve 9 is set, a second liquid suction pump 10 is set on the return pipe 8, and pressure sensors 12 and negative pressure nozzles are set on the water inlet sides of the first membrane module 16, the second membrane module 17 and the third membrane module 18 20. The negative pressure suction nozzle 20 is connected to the telescopic rod 19. The first membrane assembly 16, the second membrane assembly 17 and the third membrane assembly 18 all include a support plate 22 composed of a hollow cylindrical support body 21. On the side of the support plate 22 The film 23 covered, and the edge of the film 23 is provided with a sealing pressure ring 24, and the negative pressure nozzle 20 is arranged close to the film 23; the film 23 is composed of the following raw materials in parts by mass:

聚偏氟乙烯20-30份、聚砜酰胺聚20-30、乙烯吡咯烷酮3-9份、聚丙烯腈6-12份、聚乙二醇5-20份、碳纳米管0.08-0.52份; 20-30 parts of polyvinylidene fluoride, 20-30 parts of polysulfoneamide, 3-9 parts of vinylpyrrolidone, 6-12 parts of polyacrylonitrile, 5-20 parts of polyethylene glycol, 0.08-0.52 parts of carbon nanotubes;

外壳1的另一端通过管道连接有陶瓷膜过滤器3,陶瓷膜过滤器3内设置有螺旋盘管5,螺旋盘管5内壁设置有吸附网13,螺旋盘管5的末端设置有陶瓷过滤膜15,螺旋盘管5上连接有反洗进水管11和反洗出水管14。 The other end of the casing 1 is connected to a ceramic membrane filter 3 through a pipeline, and the ceramic membrane filter 3 is provided with a spiral coil 5, the inner wall of the spiral coil 5 is provided with an adsorption net 13, and the end of the spiral coil 5 is provided with a ceramic filter membrane 15. The spiral coil pipe 5 is connected with a backwash water inlet pipe 11 and a backwash water outlet pipe 14 .

所述陶瓷膜过滤器3下端设有出液口11。 The lower end of the ceramic membrane filter 3 is provided with a liquid outlet 11 .

所述负压吸嘴7为锥形,开口处的内径与底部的内径之比为1∶5。 The negative pressure suction nozzle 7 is conical, and the ratio of the inner diameter of the opening to the inner diameter of the bottom is 1:5.

所述陶瓷过滤膜11采用二氧化硅陶瓷过滤膜。 The ceramic filter membrane 11 is a silicon dioxide ceramic filter membrane.

所述触控器2与所述第一抽液泵6、第二抽液10和电控开关阀9之间设 置通讯连接。 A communication connection is set between the touch controller 2 and the first liquid suction pump 6, the second liquid suction 10 and the electric control switch valve 9.

所述第一膜组件16、第二膜组件17和第三膜组件18两侧设有密封卡槽。 The two sides of the first membrane module 16, the second membrane module 17 and the third membrane module 18 are provided with sealing grooves.

所述第一膜组件16、第二膜组件17和第三膜组件18过滤精度从进液端到出液端依次增大。 The filtration accuracy of the first membrane module 16 , the second membrane module 17 and the third membrane module 18 increases sequentially from the liquid inlet end to the liquid outlet end.

所述触控器2的芯片采用单片机。 The chip of the touch controller 2 adopts a single-chip microcomputer.

所述出液口11上设有阀门。 The liquid outlet 11 is provided with a valve.

本具体实施所采用的膜的强度较高,亲水性较好,具有较高的孔隙率,降低了膜的阻力,提高了水通量,设计三个不同过滤精度的膜组件,通过第一抽液泵将药液抽入外壳内进行逐级过滤。每个膜组件前设置有回流管,回流管上设置有电控开关阀和第二抽液泵,通过触控器的控制,未经过膜组件的回流液通过回流管进入储液罐,进行二次分离。由于每一根回流管上都设置有电控开关阀,可实现不同回流管的开闭状态的单独控制。膜组件被安装在密封卡槽中,可根据实际使用需要安装和拆卸,实现了多个膜组件串联同时工作和单个膜组件单独工作的切换。每个膜组件前设置有压力传感器,可将药液压力实时传回触控器进行监控,触控器根据得到的数据,自动调节第一抽液泵的转速,防止由于压力过大损坏膜组件,随着杂质的累积,过滤网的通过性逐渐变差,这就使砂石过滤器内过滤网进水端一侧的压力逐渐增高,当压力传感器测量到压力超过限定值后,打开负压吸嘴,并通过伸缩杆的上下伸缩对过滤网上附着的杂质进行清理。与此同时,关闭截止阀,使用反冲管对吸附网上和陶瓷过滤膜上吸附的杂质进行反洗清洁。两个模块同时进行清洁,节约维护时间。 The membrane used in this specific implementation has high strength, good hydrophilicity, and high porosity, which reduces the resistance of the membrane and improves the water flux. Three membrane modules with different filtration precisions are designed. Through the first The liquid suction pump draws the liquid medicine into the shell for step-by-step filtration. There is a return pipe in front of each membrane module, and the return pipe is equipped with an electric control switch valve and a second liquid suction pump. Through the control of the touch controller, the return liquid that has not passed through the membrane module enters the liquid storage tank through the return pipe for two separation. Since each return pipe is provided with an electronically controlled on-off valve, the individual control of the opening and closing states of different return pipes can be realized. The membrane module is installed in the sealed card slot, which can be installed and disassembled according to actual needs, realizing the switching between multiple membrane modules working in series at the same time and a single membrane module working alone. There is a pressure sensor in front of each membrane module, which can transmit the pressure of the liquid medicine back to the touch controller for monitoring in real time. The touch controller automatically adjusts the speed of the first pumping pump according to the obtained data to prevent damage to the membrane module due to excessive pressure. , with the accumulation of impurities, the passability of the filter gradually deteriorates, which gradually increases the pressure on the water inlet side of the filter in the gravel filter. When the pressure sensor detects that the pressure exceeds the limit value, the negative pressure is turned on. suction nozzle, and clean up the impurities attached to the filter through the up and down expansion and contraction of the telescopic rod. At the same time, close the shut-off valve, and use the recoil pipe to backwash and clean the impurities adsorbed on the adsorption net and the ceramic filter membrane. Both modules are cleaned simultaneously, saving maintenance time.

以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以作出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。 The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, and these improvements and modifications should also be It is regarded as the protection scope of the present invention.

Claims (9)

1. apply the waste disposal plant of membrane technique for one kind, it is characterized in that, comprise shell (1) and touch controller (2), one end of shell (1) is provided with liquid-inlet pipe (4), liquid-inlet pipe (4) is provided with the first liquid absorbing pump (6), the first membrane module (16) has been arranged in series in shell (1), second membrane module (17) and tertiary membrane assembly (18), the front side of each membrane module (7) arranges a return line (8), return line (8) is arranged electric-controlled switch valve (9), return line (8) is arranged the second liquid absorbing pump (10), first membrane module (16), the influent side of the second membrane module (17) and tertiary membrane assembly (18) is provided with pressure transmitter (12) and negative pressure suction nozzle (20), negative pressure suction nozzle (20) is connected on expansion link (19), first membrane module (16), second membrane module (17) and tertiary membrane assembly (18) include and form back up pad (22) by hollow cylinder supporter (21), the film (23) covered in back up pad (22) side, and the edge of film (23) is provided with seal joint (24), negative pressure suction nozzle (20) is close to film (23) and is arranged, film (23) is made up of the raw material of following masses number:
Polyvinylidene difluoride (PVDF) 20-30 part, polysulfonamides gather 20-30, V-Pyrol RC 3-9 part, polyacrylonitrile 6-12 part, polyoxyethylene glycol 5-20 part, carbon nanotube 0.08-0.52 part;
The other end of shell (1) is connected with purpose ceramic-film filter (3) by pipeline, spiral pipe (5) is provided with in purpose ceramic-film filter (3), spiral pipe (5) inwall is provided with adsorption net (13), the end of spiral pipe (5) is provided with ceramic filter membrane (15), spiral pipe (5) is connected with backwash water inlet pipe (11) and backwash rising pipe (14).
2. a kind of waste disposal plant applying membrane technique according to claim 1, is characterized in that, described purpose ceramic-film filter (3) lower end is provided with liquid outlet (11).
3. a kind of waste disposal plant applying membrane technique according to claim 1, is characterized in that, described negative pressure suction nozzle (7) is taper, and the internal diameter of opening part is 1: 5 with the ratio of the internal diameter of bottom.
4. a kind of waste disposal plant applying membrane technique according to claim 1, is characterized in that, described ceramic filter membrane (11) adopts SiO 2-ceramic filtering membrane.
5. a kind of waste disposal plant applying membrane technique according to claim 1, it is characterized in that, described touch controller (2) and described first liquid absorbing pump (6), between the second drawing liquid (10) and electric-controlled switch valve (9), communication is set is connected.
6. a kind of waste disposal plant applying membrane technique according to claim 1, is characterized in that, described first membrane module (16), the second membrane module (17) and tertiary membrane assembly (18) both sides are provided with sealing draw-in groove.
7. a kind of waste disposal plant applying membrane technique according to claim 1, it is characterized in that, described first membrane module (16), the second membrane module (17) and tertiary membrane assembly (18) filtering accuracy increase successively from liquid feeding end to outlet end.
8. a kind of waste disposal plant applying membrane technique according to claim 1, is characterized in that, the chip of described touch controller (2) adopts micro-chip.
9. a kind of waste disposal plant applying membrane technique according to claim 1, is characterized in that, described liquid outlet (11) is provided with valve.
CN201510278205.0A 2015-05-23 2015-05-23 Sewage treatment device applying membrane technology Pending CN104925901A (en)

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CN113908697A (en) * 2021-10-18 2022-01-11 成都凯成轻工药业装备有限公司 High-performance ceramic membrane component applied to beer filtration field

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109966924A (en) * 2019-03-21 2019-07-05 清华苏州环境创新研究院 A kind of control system of pressure type plate membrane filter system
CN113908697A (en) * 2021-10-18 2022-01-11 成都凯成轻工药业装备有限公司 High-performance ceramic membrane component applied to beer filtration field

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Application publication date: 20150923