CN207986764U - A kind of tubular type microfiltration systems handle the device of wet electric waste water - Google Patents
A kind of tubular type microfiltration systems handle the device of wet electric waste water Download PDFInfo
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- CN207986764U CN207986764U CN201820120207.6U CN201820120207U CN207986764U CN 207986764 U CN207986764 U CN 207986764U CN 201820120207 U CN201820120207 U CN 201820120207U CN 207986764 U CN207986764 U CN 207986764U
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- 238000001471 micro-filtration Methods 0.000 title claims abstract description 40
- 239000002351 wastewater Substances 0.000 title claims abstract description 24
- 239000012528 membrane Substances 0.000 claims abstract description 63
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 238000004140 cleaning Methods 0.000 claims abstract description 24
- 239000002562 thickening agent Substances 0.000 claims abstract description 23
- 239000004593 Epoxy Substances 0.000 claims abstract description 9
- 239000010802 sludge Substances 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 6
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 230000007423 decrease Effects 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 17
- 230000000694 effects Effects 0.000 abstract description 10
- 239000002699 waste material Substances 0.000 description 13
- 230000005611 electricity Effects 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000000108 ultra-filtration Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009295 crossflow filtration Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- -1 dirt Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
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- 238000012986 modification Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
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- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses the devices that a kind of tubular type microfiltration systems handle wet electric waste water, including thickener, the top and left side of the thickener are communicated with membrane tube, bottom on the left of the thickener is communicated with cleaning water tank, it is communicated with cleaning pump at the top of the cleaning water tank, the top of the thickener is communicated with intake pump by membrane tube, and the top of the cleaning water tank is communicated with backwash water bumper post by membrane tube, and the right side of the backwash water bumper post is communicated with backwash air inlet by membrane tube.The utility model by membrane tube, cleaning pump, backwash water bumper post, backwash air inlet, tube microfiltration membrane, epoxy layer steelframe, through water out, flush box, clean water tank and intake pump cooperation, solid-liquid in wet electric waste water can be effectively separated, it is poor to solve the problems, such as that the processing unit of simple structure handles wet electric waste water effect, enhance processing unit to the treatment effect of wet electric waste water, reduces the labor intensity of user.
Description
Technical field
The utility model is related to tubular type microfiltration systems technical field, specially a kind of wet electric waste water of tubular type microfiltration systems processing
Device.
Background technology
Wet electrical dust precipitator be it is a kind of be used for handling the high-pressure static cleaner containing humid gas, be mainly used to remove containing wet
The harmful substances such as dirt, acid mist, water droplet, aerosol, stink, PM2.5 in gas are that the ideal of improvement atmospheric dust pollution is set
Standby, wet cottrell needs the dust adsorbed on continuous shower water removal anode plate, shower water to be needed after recycling
It discharges, the wet electric waste water of discharge goes mist separator of desulfurization to use after filtration treatment, and wet electric precipitation waste water contains a large amount of ash
Dirt, gypsum, colloidal substance and heavy metal, generally first pass through addition flocculant and flocculation aid flocculates, and then utilize flat flow
Sedimentation basin or vertical sedimentation basin carry out flocculation sediment, remove most solid suspended particle, but conventional processing skill
Art technological process is long, and depositing technology hydraulic detention time is long, takes up a large area, and system investments are high, simple coagulation, clarification process
It is unable to reach satisfactory outlet effect, and common ultrafiltration cannot receive very high turbidity, due to effectively precipitating needs
The grain size of precipitate particles is sufficiently large and proportion is sufficiently large, generally requires excessively to add flocculant and macromolecule flocculation aid, this is just
Abundant residues medicament in production water is caused, the consequence thus brought is that producing water water quality is poor, and water quality is unstable, influences subsequent processing
Effect and have an impact to discharge index.
When user carries out micro-filtration processing to wet electric waste water, need to use the wet electric waste plant of processing, existing processing
Device is mostly the processing unit of simple structure, and the wet electric waste water effect of processing unit processing of simple structure is poor, can not be to wet electricity
Solid-liquid in waste liquid is detached, and can not carry out retention removal to the particle in waste liquid, and user is needed to carry out reworked processing, is increased
Force the labor intensity of user.
Utility model content
The purpose of this utility model is to provide the devices that a kind of tubular type microfiltration systems handle wet electric waste water, and it is wet to have processing
It is poor to solve the problems, such as that the processing unit of simple structure handles wet electric waste water effect for the good advantage of electric waste liquid effect.
To achieve the above object, the utility model provides the following technical solutions：A kind of wet electricity of tubular type microfiltration systems processing is useless
The device of water, including thickener, the top and left side of the thickener are communicated with membrane tube, the bottom connection on the left of the thickener
There is cleaning water tank, cleaning pump is communicated at the top of the cleaning water tank, the top of the thickener is communicated with by membrane tube into water
The top of pump, the cleaning water tank is communicated with backwash water bumper post by membrane tube, passes through film on the right side of the backwash water bumper post
Pipe is communicated with backwash air inlet, and the right side of the backwash air inlet is communicated with tube microfiltration membrane, the tubular type micro-filtration by membrane tube
Epoxy layer steelframe is fixedly connected on the right side of film, the bottom of the epoxy layer steelframe is communicated with by membrane tube through water out, institute
The bottom stated through water out is communicated with flush box by membrane tube, and the bottom of the flush box is communicated with recoil by membrane tube
The top of tank, the recoil tank is provided with separation pressure reducing valve by membrane tube.
Preferably, the bottom on the left of the thickener is communicated with sludge pump by membrane tube, and the sludge pump is located at flushing water
The bottom of case.
Preferably, the quantity of the tube microfiltration membrane is no less than four, and the tube microfiltration membrane is arranged in horizontal structure.
Compared with prior art, the beneficial effects of the utility model are as follows：
1, the utility model passes through membrane tube, cleaning pump, backwash water bumper post, backwash air inlet, tube microfiltration membrane, epoxy layer
Steelframe, through water out, flush box, the cooperation for cleaning water tank and intake pump, the solid-liquid in wet electric waste water can be carried out effective
Separation solves the problems, such as that the processing unit of simple structure handles that wet electric waste water effect is poor, and enhancing processing unit is to wet electricity waste water
Treatment effect, reduce the labor intensity of user, be worth of widely use.
2, the utility model is discharged the mud in thickener by sludge pump, enhances the stream of waste liquid in thickener
Dynamic property, further concentrates mud convenient for compression set, is no less than four by the quantity of tube microfiltration membrane, enhances the stream of waste liquid
Dynamic property is arranged in horizontal structure by tube microfiltration membrane, is flowed in tube microfiltration membrane convenient for waste liquid, enhance microfiltration systems
Waste liquid is handled.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model.
In figure：1 thickener, 2 membrane tubes, 3 cleaning pumps, 4 backwash water bumper posts, 5 backwash air inlets, 6 tube microfiltration membranes, 7 rings
Oxygen layer steelframe, 8 are through water out, 9 flush boxs, 10 cleaning water tanks, 11 intake pumps, 12 recoil tanks, 13 separation pressure reducing valves, 14 rows
Dredge pump.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
Referring to Fig. 1, a kind of tubular type microfiltration systems handle the device of wet electric waste water, including thickener 1,1 left side of thickener
Bottom sludge pump 14 is communicated with by membrane tube 2, sludge pump 14 is located at the bottom of flush box 9, by sludge pump 14, to concentration
Mud in slot 1 is discharged, and is enhanced the mobility of waste liquid in thickener 1, is further concentrated to mud convenient for compression set, dense
The top and left side of contracting slot 1 are communicated with membrane tube 2, and the bottom in 1 left side of thickener is communicated with cleaning water tank 10, cleans the top of water tank 10
Portion is communicated with cleaning pump 3, and the top of thickener 1 is communicated with intake pump 11 by membrane tube 2, and the top of cleaning water tank 10 passes through membrane tube
2 are communicated with backwash water bumper post 4, and the right side of backwash water bumper post 4 is communicated with backwash air inlet 5, backwash air inlet by membrane tube 2
5 right side is communicated with tube microfiltration membrane 6 by membrane tube 2, and the quantity of tube microfiltration membrane 6 is no less than four, passes through tube microfiltration membrane 6
Quantity be no less than four, enhance the mobility of waste liquid, tube microfiltration membrane 6 is arranged in horizontal structure, is in by tube microfiltration membrane 6
Horizontal structure is arranged, and is flowed in tube microfiltration membrane 6 convenient for waste liquid, and enhancing microfiltration systems handle waste liquid, tubular type
The right side of microfiltration membranes 6 is fixedly connected with epoxy layer steelframe 7, and the bottom of epoxy layer steelframe 7 is communicated with by membrane tube 2 through water out
8, flush box 9 is communicated with by membrane tube 2 through the bottom of water out 8, the bottom of flush box 9 is communicated with instead by membrane tube 2
Tank 12 is rushed, the top for the tank 12 that recoils is provided with separation pressure reducing valve 13 by membrane tube 2.
In use, opening cleaning pump 3 and intake pump 11 by peripheral control unit, the dope water in thickener 1 passes through water inlet
Pump 11 is lifted into 6 inner cavity of tube microfiltration membrane, and dope water under the driving of pressure and speed, is made through filmed passing tube 2 by perforated membrane
Suspended solid material is detached with liquid, the process of cross-flow filtration, and in each tube microfiltration membrane 6, wet electricity waste water is cleaned to pump 3
It is very high to pump the flow velocity through filmed passing tube 2, turbulent flow parallel with film surface generates a shear action, the solid that will be deposited on film
Amount minimizes, and the clear water after filtering is admitted in cleaning water tank 10, remaining to be known as concentrate, is admitted in flush box 9,
It is cleaned again by cleaning pump 3, so that the suspended solid material in waste liquid is flow back into thickener 1, thus constantly followed
Ring, tube microfiltration membrane system mainly detach the particulate matter of inorganic states with water, and the general water turbidity that produces is less than 1NTU even
Less than 0.5NTU, this film uses the PVDF materials for most having resistance to epistasis and chemical resistance to be made, since it is close
In ultra-filtration filters aperture, the pollutant in waste water can be efficiently removed using such microfiltration membranes, simultaneously because it is solely
Special construction can make the wet electric waste water containing mud granule enter membranous system and is directly separated by solid-liquid separation, and it is heavy to save
Shallow lake pond, multi-medium filtering, the links such as sand filtration, carbon filter and ultrafiltration.
In summary：The tubular type microfiltration systems handle the device of wet electric waste water, slow by membrane tube 2, cleaning pump 3, backwash water
Rush column 4, backwash air inlet 5, tube microfiltration membrane 6, epoxy layer steelframe 7, through water out 8, flush box 9, cleaning water tank 10 and
It is poor to solve the problems, such as that the processing unit of simple structure handles wet electric waste water effect for the cooperation of intake pump 11.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is appreciated that can these embodiments be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (3)
1. a kind of tubular type microfiltration systems handle the device of wet electric waste water, including thickener（1）, it is characterised in that：The thickener
（1）Top and left side be communicated with membrane tube（2）, the thickener（1）The bottom in left side is communicated with cleaning water tank（10）, described clear
Water tank（10）Top be communicated with cleaning pump（3）, the thickener（1）Top pass through membrane tube（2）It is communicated with intake pump
（11）, the cleaning water tank（10）Top pass through membrane tube（2）It is communicated with backwash water bumper post（4）, the backwash water bumper post
（4）Right side pass through membrane tube（2）It is communicated with backwash air inlet（5）, the backwash air inlet（5）Right side pass through membrane tube（2）Even
It is connected with tube microfiltration membrane（6）, the tube microfiltration membrane（6）Right side be fixedly connected with epoxy layer steelframe（7）, the epoxy layer steel
Frame（7）Bottom pass through membrane tube（2）It is communicated with and penetrates water out（8）, described to penetrate water out（8）Bottom pass through membrane tube（2）
It is communicated with flush box（9）, the flush box（9）Bottom pass through membrane tube（2）It is communicated with recoil tank（12）, the recoil tank
（12）Top pass through membrane tube（2）It is provided with separation pressure reducing valve（13）.
2. a kind of tubular type microfiltration systems according to claim 1 handle the device of wet electric waste water, it is characterised in that：It is described dense
Contracting slot（1）The bottom in left side passes through membrane tube（2）It is communicated with sludge pump（14）, the sludge pump（14）Positioned at flush box（9）'s
Bottom.
3. a kind of tubular type microfiltration systems according to claim 1 handle the device of wet electric waste water, it is characterised in that：The pipe
Decline filter membrane（6）Quantity be no less than four, the tube microfiltration membrane（6）It is arranged in horizontal structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820120207.6U CN207986764U (en) | 2018-01-24 | 2018-01-24 | A kind of tubular type microfiltration systems handle the device of wet electric waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820120207.6U CN207986764U (en) | 2018-01-24 | 2018-01-24 | A kind of tubular type microfiltration systems handle the device of wet electric waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207986764U true CN207986764U (en) | 2018-10-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820120207.6U Expired - Fee Related CN207986764U (en) | 2018-01-24 | 2018-01-24 | A kind of tubular type microfiltration systems handle the device of wet electric waste water |
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| CN (1) | CN207986764U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108217842A (en) * | 2018-01-24 | 2018-06-29 | 浙江南源环境工程技术有限公司 | A kind of device of the wet electric waste water of tubular type microfiltration systems processing |
-
2018
- 2018-01-24 CN CN201820120207.6U patent/CN207986764U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108217842A (en) * | 2018-01-24 | 2018-06-29 | 浙江南源环境工程技术有限公司 | A kind of device of the wet electric waste water of tubular type microfiltration systems processing |
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| GR01 | Patent grant | ||
| 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: 20181019 Termination date: 20200124 |