CN207072829U - A kind of membrane module filter - Google Patents

A kind of membrane module filter Download PDF

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Publication number
CN207072829U
CN207072829U CN201720697981.9U CN201720697981U CN207072829U CN 207072829 U CN207072829 U CN 207072829U CN 201720697981 U CN201720697981 U CN 201720697981U CN 207072829 U CN207072829 U CN 207072829U
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CN
China
Prior art keywords
membrane
filtering machine
filtrate receiver
membrane filtering
membrane module
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
CN201720697981.9U
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Chinese (zh)
Inventor
顾健
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.)
TAICANG PLASTIC ADDITIVES FACTORY CO Ltd
Original Assignee
TAICANG PLASTIC ADDITIVES FACTORY CO Ltd
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 TAICANG PLASTIC ADDITIVES FACTORY CO Ltd filed Critical TAICANG PLASTIC ADDITIVES FACTORY CO Ltd
Priority to CN201720697981.9U priority Critical patent/CN207072829U/en
Application granted granted Critical
Publication of CN207072829U publication Critical patent/CN207072829U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a kind of membrane module filter, including material fluid bath, constant pump, circulating pump, Membrane filtering machine, filtrate receiver;Material fluid bath is connected by constant pump with Membrane filtering machine, and Membrane filtering machine is connected with filtrate receiver, and filtrate receiver is connected by circulating pump with material fluid bath, and Membrane filtering machine is placed on magnetic stirrer and Membrane filtering machine is provided with pressure gauge, and filtrate receiver is placed on weighing device.The utility model can interpolate that the relation between flow velocity, pressure, filter medium resistance, is placed in control filtrate filter type on magnetic stirrer by Membrane filtering machine, can use filtration enhancement measure, reach and preferably separate purpose, realizes that engineering is magnified.

Description

A kind of membrane module filter
Technical field
It the utility model is related to a kind of membrane module filter.
Background technology
In field of waste water treatment, conventional method mainly realizes mud-water separation to traditional active sludge using sedimentation basin, but locates Reason processing is limited, and membrane module filter method is so that its separation of solid and liquid rate is high, effluent quality is good, treatment effeciency is high, space is small, fortune The features such as row management is simple, is used successfully to the processing of the sanitary wastewaters such as effluent sewerage, fecal sewage, percolate.But work Partial impurities particle diameter is small in industry wastewater treatment, and membrane module filtering and flux, service life and the close phase of the water quality of water outlet of film Close, existing membrane module filter fluctuation of service, be difficult to control.
The content of the invention
Goal of the invention:In view of the shortcomings of the prior art, membrane module filter provided by the utility model, can realize film Component is to the stably and controllable of wastewater treatment.
Technical scheme:Membrane module filter described in the utility model, including material fluid bath, constant pump, circulating pump, film mistake Filter, filtrate receiver;Material fluid bath is connected by constant pump with Membrane filtering machine, and Membrane filtering machine is connected with filtrate receiver, and filtrate receiver is by following Ring pump is connected with material fluid bath, and Membrane filtering machine is placed on magnetic stirrer and Membrane filtering machine is provided with pressure gauge, and filtrate receiver is placed in title Refitting is put.
Above-mentioned technical proposal is further improved, the Membrane filtering machine uses flat board filtering type membrane module;The flat board filters The membrane aperture of formula membrane module is 0.25 ~ 0.50um.It is conveniently replaceable, is controlled using flat board filtering type membrane module.
Further, regulating valve is provided between the Membrane filtering machine and the filtrate receiver.
Further, constant pump both ends pipeline is provided with control valve, on the pipeline between the filtrate receiver and circulating pump Provided with control valve.
Beneficial effect:Compared with prior art, the advantages of the utility model:The utility model controls feed liquid by constant pump The fluid flow that groove enters in Membrane filtering machine, by pressure gauge acquisition filter pressure, judge to block up by filtrate receiver weigh Plug, can interpolate that the relation between flow velocity, pressure, filter medium resistance, is placed on magnetic stirrer and controlled by Membrane filtering machine Filtrate filter type, filtration enhancement measure can be used, reaches and preferably separates purpose, realize that engineering is magnified.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Technical solutions of the utility model are described in detail below by accompanying drawing.
Embodiment 1:Membrane module filter as shown in Figure 1, including material fluid bath 1, constant pump 2, circulating pump 9, membrane filtration Machine 3, filtrate receiver 7, Membrane filtering machine 3 use flat board filtering type membrane module, and the membrane aperture of flat board filtering type membrane module is 0.45um;Material Liquid bath 1 is connected by constant pump 2 with Membrane filtering machine 3, and the both ends pipeline of constant pump 2 is provided with control valve, Membrane filtering machine 3 and filtrate receiver 7 It is connected, regulating valve 6 is provided between Membrane filtering machine 3 and filtrate receiver 7, filtrate receiver 7 is connected by circulating pump 9 with material fluid bath 1, filtrate receiver Pipeline between 7 and circulating pump 9 is provided with control valve;Membrane filtering machine 3 is placed on magnetic stirrer 4 and Membrane filtering machine 3 is provided with Pressure gauge 5, filtrate receiver 7 are placed on weighing device 8.
Secondary filter is carried out using membrane module, pressure is filtered in filter process to be increased with the rise of filtration resistance, By fixed speed control filtering rate, pressure is gathered in real time, filter medium resistance, control filter type, which is realized, preferably to be separated.
As above, although the utility model has been represented and described with reference to specific preferred embodiment, it must not be explained For the limitation to the utility model itself.In the spirit and scope premise of the present utility model for not departing from appended claims and defining Under, can various changes can be made in the form and details to it.

Claims (5)

  1. A kind of 1. membrane module filter, it is characterised in that:Including material fluid bath, constant pump, circulating pump, Membrane filtering machine, filtrate receiver; Material fluid bath is connected by constant pump with Membrane filtering machine, and Membrane filtering machine is connected with filtrate receiver, and filtrate receiver passes through circulating pump and material fluid bath It is connected, Membrane filtering machine is placed on magnetic stirrer and Membrane filtering machine is provided with pressure gauge, and filtrate receiver is placed on weighing device.
  2. 2. membrane module filter according to claim 1, it is characterised in that:The Membrane filtering machine uses flat board filtering type film Component.
  3. 3. membrane module filter according to claim 2, it is characterised in that:The membrane aperture of the flat board filtering type membrane module For 0.25 ~ 0.50um.
  4. 4. membrane module filter according to claim 1, it is characterised in that:Between the Membrane filtering machine and the filtrate receiver Provided with regulating valve.
  5. 5. membrane module filter according to claim 1, it is characterised in that:Constant pump both ends pipeline is provided with control Valve, the pipeline between the filtrate receiver and circulating pump are provided with control valve.
CN201720697981.9U 2017-06-15 2017-06-15 A kind of membrane module filter Expired - Fee Related CN207072829U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720697981.9U CN207072829U (en) 2017-06-15 2017-06-15 A kind of membrane module filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720697981.9U CN207072829U (en) 2017-06-15 2017-06-15 A kind of membrane module filter

Publications (1)

Publication Number Publication Date
CN207072829U true CN207072829U (en) 2018-03-06

Family

ID=61513923

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720697981.9U Expired - Fee Related CN207072829U (en) 2017-06-15 2017-06-15 A kind of membrane module filter

Country Status (1)

Country Link
CN (1) CN207072829U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110681269A (en) * 2019-11-20 2020-01-14 宁波建嵘科技有限公司 Two-stage coating heterogeneous synchronous composite membrane preparation technology and device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110681269A (en) * 2019-11-20 2020-01-14 宁波建嵘科技有限公司 Two-stage coating heterogeneous synchronous composite membrane preparation technology and device

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GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180306

Termination date: 20200615

CF01 Termination of patent right due to non-payment of annual fee