CN206886765U - A kind of electric adsorption liquid processing module - Google Patents
A kind of electric adsorption liquid processing module Download PDFInfo
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- CN206886765U CN206886765U CN201720112098.9U CN201720112098U CN206886765U CN 206886765 U CN206886765 U CN 206886765U CN 201720112098 U CN201720112098 U CN 201720112098U CN 206886765 U CN206886765 U CN 206886765U
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- plate
- end plate
- insulation frame
- battery lead
- processing module
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- 239000007788 liquid Substances 0.000 title claims abstract description 57
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 25
- 238000009413 insulation Methods 0.000 claims abstract description 22
- 239000012530 fluid Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims description 15
- 229920005479 Lucite® Polymers 0.000 claims description 5
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 5
- 230000005611 electricity Effects 0.000 claims description 4
- 230000001680 brushing effect Effects 0.000 claims description 3
- 239000004568 cement Substances 0.000 claims description 3
- 239000003973 paint Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- 229910001868 water Inorganic materials 0.000 abstract description 14
- 239000002245 particle Substances 0.000 abstract description 13
- 239000000126 substance Substances 0.000 abstract description 2
- 239000002894 chemical waste Substances 0.000 abstract 1
- 235000013365 dairy product Nutrition 0.000 abstract 1
- 235000013399 edible fruits Nutrition 0.000 abstract 1
- 239000005416 organic matter Substances 0.000 abstract 1
- 150000002500 ions Chemical class 0.000 description 11
- 238000011033 desalting Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000003456 ion exchange resin Substances 0.000 description 4
- 229920003303 ion-exchange polymer Polymers 0.000 description 4
- 230000008439 repair process Effects 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 3
- 238000010612 desalination reaction Methods 0.000 description 3
- 230000005684 electric field Effects 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 238000005342 ion exchange Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000004917 carbon fiber Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 238000005115 demineralization Methods 0.000 description 1
- 230000002328 demineralizing effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 241000894007 species Species 0.000 description 1
Abstract
It is main to include insulation frame, insulating flange, end plate, binding post and multiple electrodes plate the utility model discloses a kind of electric adsorption liquid processing module；Insulation frame left and right ends are respectively arranged with insulating flange, and two insulating flanges are bolted with left and right sides end plate respectively, form dismountable modular structure；Both sides end plate is connected with left and right binding post respectively；Battery lead plate upper and lower surface uniform fold fibrofelt, battery lead plate, which is horizontally staggered, to be arranged side by side, successively with left and right sides end plate connection；Battery lead plate forms the fluid flow paths of series connection together with insulation frame and end plate, liquid flowing channel upper and lower ends respectively with being connected into and out of fluid apertures on insulation frame.Electric adsorption liquid processing module of the present utility model can effectively remove ion, organic matter, suspended substance and colloidal particle in liquid etc., and the water in various sources, wine, fruit dairy products and various chemical waste liquids can be handled.
Description
Technical field
A kind of electric adsorption liquid processing module is the utility model is related to, belongs to technical field of environment protection equipment.
Background technology
For liquid handling, especially water treatment procedure, conventional method has hyperfiltration, electroosmose process, ion exchange
Method etc..Hyperfiltration is largely used in terms of industrial pure water production at present, has desalination rate height, process combination relative ease etc.
Advantage.But hyperfiltration use macromolecule membrane easily by the materials such as Organic substance in water, calcium, chlorine pollution and poison, it is desirable to match somebody with somebody
There is strict pretreatment system and add various antioxidants and antisludging agent, thus energy consumption is higher, and need to regularly replace film,
Invest larger.Electroosmose process utilizes the effect of electric field, by force attracts ion at electrode, causes the ion of electrode middle part
Concentration substantially reduces, so as to which fresh water be made.But due to using amberplex, still there is the shortcomings that being poisoned.Ion-exchange is
Separated using the commutative group in ion-exchanger and various interionic ion-exchange capacity differences in solution
A kind of method.This method is handled liquid using ion exchange resin as main body, ion exchange resin not only price
Costliness, and need to use strong acid, highly basic to be regenerated, therefore plant maintenance is complicated and can cause secondary pollution problems.Electricity
Absorption desalination technology can also claim capacitive deionization technology, be the side using charged electrode surface adsorption water intermediate ion and charged particle
Method, the salt that is dissolved in water and other charge specieses can be made to realize purification/desalination of water in the surface enrichment concentration of electrode
A kind of new water technology.Its total technological process is divided into two parts：The course of work and regenerative process.The course of work is electricity
The adsorption process of adsorption module, the water outlet of module are the purified water after electro-adsorption demineralization；Regenerative process is by electrode both positive and negative polarity
Reversal connection, the charged particle that the course of work is adsorbed is re-released into interelectrode fluid flow paths, and backwashed by raw water
Take charged particle out of electric adsorption module, the now water outlet of module is backwashing water.
CN1169728C discloses a kind of electric adsorption liquid treatment device, including is arranged in shell more than a pair side by side
The conductive plate of configuration and the electrode plate groups that are connected on conductive plate into liquid-treatment unit, the conductive plate and power connecting column of two side ends
Connect, ion exchange resin is provided with the cavity between adjacent two battery lead plate.It is low using consuming energy in Liquid-treatment processes, have
Self-regeneration function, and liquid handling efficiency high.But because ion exchange resin is expensive, and need to use strong acid, highly basic
Regenerated, therefore plant maintenance is complicated, while secondary pollution problems can be caused.
Utility model content
The purpose of this utility model is on the premise of secondary pollution is avoided, there is provided one kind is simple in construction, uses process
Middle energy consumption is low, has the high electric adsorption liquid processing module of self-regeneration function, desalting efficiency.
Electric adsorption liquid processing module of the present utility model, it is main to include insulation frame, insulating flange, end plate, binding post
And multiple electrodes plate.The insulation frame left and right ends are respectively arranged with insulating flange, two insulating flanges respectively with the left and right sides
End plate is bolted, and forms dismountable modular structure, to facilitate the installation of battery lead plate and fibrofelt and dismounting.Described two
Side end panel is connected with left and right binding post respectively, two binding posts by wire with can the dc source of Variable Polarity be connected, Ke Yishi
Now to the positive and negative power supply of battery lead plate.The battery lead plate upper and lower surface uniform fold fibrofelt, battery lead plate, which is horizontally staggered, to be arranged side by side,
Successively with left and right sides end plate connection.Battery lead plate forms the fluid flow paths of series connection, liquid flow together with insulation frame and end plate
Passage upper and lower ends respectively with insulation frame on being connected into and out of fluid apertures.
In electric adsorption liquid processing module described in the utility model, described insulation frame uses lucite, so as to
See liquid flow process in module；Described insulating flange selects insulating materials, preferably lucite, to facilitate and insulate
Frame adhesion；Described end plate be good conductivity conductive plate, except with addition to the junction of battery lead plate and binding post, end plate remaining surface
Uniform brushing insulated paint；Described fibrofelt, by insulating cement adhesion, ensures tightly to be bonded at contact surface, fibrofelt with battery lead plate
It is preferred that active carbon fiber felt, graphite fibre felt or alumina silicate fiber felt；Described battery lead plate setting 8 ~ 500, preferably 20 ~
200.
Electric adsorption liquid processing module described in the utility model can two groups and more parallel use, to improve liquid
Treating capacity；Can also two groups and the above be used in series, further to improve desalting efficiency.
The operation principle of electric adsorption liquid processing module described in the utility model is：By dc source and the left and right sides
Binding post connects, and direct current is passed into positive and negative electrode plate by end plate, pending liquid enters module from liquid inlet
Afterwards, flow through positive and negative electrode plate and insulate the fluid flow paths formed between frame and end plate when, foreign ion in liquid and
Charged particle migrates in the presence of electric field to positive and negative electrode, and is stored in the fibrofelt of electrode plate surface covering so that treats
Foreign ion and charged particle in treatment liquid are removed, and liquid is purified, and the liquid after purification is from liquid outlet stream
Go out.When foreign ion and charged particle near positive and negative electrode are assembled to a certain extent, DC power polarity is changed, made
Positive-negative electrode plate is electrically on the contrary, the foreign ion and charged particle that are stored in originally in electrode surface fibrofelt are discharged into liquid and led to
In road, module is discharged with backwashing water, completes regenerative process.DC power polarity is changed again after regeneration ending, you can enter
Enter the purification process in next cycle.
The utility model has the advantage of：1st, it is simple in construction, the utility model by binding post and end plate by battery lead plate with
Dc source connects, and using the power supply mode of series connection, greatly reduces operating current, simplifies electric power system.2nd, liquid handling
Measure applied widely, the utility model can be in parallel by multiple liquid treatment modules, can be flexibly adapted to different liquids processing
The demand of amount.3rd, maintenance is easy, the utility model because end plate and insulation frame and insulation frame flange are connected by screw bolts, installation and
Convenient disassembly, and can neatly adjust quantity and spacing with the battery lead plate of end plate connection.4th, desalting efficiency is high, and this practicality is new
The fluid flow paths of series connection are formed between the multiple electrodes plate of type, battery lead plate number is more, battery lead plate is longer, and liquid flow is all
Road is longer, and desalting efficiency is higher.And electrode plate surface is covered with fibrofelt, fibrofelt can both play flow-disturbing effect, again can be with
Proper extension liquid flows about the time in battery lead plate, further promotes foreign ion and charged particle moving to positive and negative electrode
Move, so as to improve liquid handling capacity.5th, there is autosynthesis function, non-secondary pollution, battery lead plate of the present utility model has
Self-regeneration function, without chemical reagent, therefore secondary pollution problem is not present.
Brief description of the drawings
Fig. 1 is the front view of the utility model electric adsorption liquid processing module.
Fig. 2 is the top view of the utility model electric adsorption liquid processing module.
Wherein, 1- liquid outlets, 2- insulating flanges, 3- insulation frames, 4- end plates, 5- binding posts, 6- fibrofelts, 7- electrodes
Plate, 8- liquid-inlets.
Embodiment
Electric adsorption liquid processing module of the present utility model is described in further detail below in conjunction with the accompanying drawings.
Electric adsorption liquid processing module described in the utility model, it is main include insulation frame 3, insulating flange 2, end plate 4,
Binding post 5 and multiple electrodes plate 7.Insulation frame 3 left and right ends are respectively arranged with insulating flange 2, and two insulating flanges 2 are distinguished
It is bolted with left and right sides end plate 4, forms dismountable modular structure, facilitates the installation of battery lead plate 7 and fibrofelt 6
And dismounting.The both sides end plate 4 is connected with left and right binding post 5 respectively, two binding posts 5 by wire with can Variable Polarity direct current
Power supply connects, it is possible to achieve the positive and negative power supply to battery lead plate 7.The upper and lower surface uniform fold fibrofelt 6 of battery lead plate 7, electrode
Plate 7, which is horizontally staggered, to be arranged side by side, and is connected successively with left and right sides end plate 4.Battery lead plate 7 is formed together with insulation frame and end plate 4 and gone here and there
The fluid flow paths of connection, liquid flowing channel upper and lower ends respectively with insulation frame on being connected into and out of fluid apertures.
In electric adsorption liquid processing module described in the utility model, described insulation frame uses lucite, so as to
See liquid flow process in module；Described insulating flange 2 selects insulating materials, preferably lucite, with facilitate with absolutely
Edge frame adhesion；Described end plate 4 be good conductivity conductive plate, except with addition to the junction of battery lead plate 7 and binding post 5, end plate 4 its
The remaining uniform brushing insulated paint in surface；Described fibrofelt 6, by insulating cement adhesion, ensures tightly to paste at contact surface with battery lead plate 7
Close, 6 preferred active carbon fiber felt of fibrofelt, graphite fibre felt or alumina silicate fiber felt；Described battery lead plate 7 sets 8 ~ 500
It is individual, preferably 20 ~ 200.
Electric adsorption liquid processing module described in the utility model can two groups and more parallel use, to improve liquid
Treating capacity；Also two groups and the above are used in series, further to improve desalting efficiency.
The operation principle of electric adsorption liquid processing module described in the utility model is：By dc source and the left and right sides
Binding post 5 connects, and direct current is passed into positive and negative electrode plate 7 by end plate 4, pending liquid enters mould from liquid-inlet 8
After block, flow through positive and negative electrode plate 7 and insulate the fluid flow paths formed between frame and end plate 4 when, impurity in liquid from
Son and charged particle migrate in the presence of electric field to positive and negative electrode, and are stored in the fibrofelt 6 of the surface of battery lead plate 7 covering,
So that the foreign ion and charged particle in liquid to be treated are removed, liquid is purified, and the liquid after purification is from liquid
The outflow of outlet 1.When foreign ion and charged particle near positive and negative electrode are assembled to a certain extent, by DC power polarity
Change, make positive-negative electrode plate 7 electrically on the contrary, the foreign ion and charged particle that are stored in originally in electrode surface fibrofelt 6 are released
It is put into fluid passage, discharges module with backwashing water, complete regenerative process.DC power polarity is changed again after regeneration ending
Become, you can enter the purification process in next cycle.
Claims (7)
- A kind of 1. electric adsorption liquid processing module, it is characterised in that：It is main to include insulation frame, insulating flange, end plate, binding post And multiple electrodes plate；The insulation frame left and right ends are respectively arranged with insulating flange, two insulating flanges respectively with the left and right sides End plate is bolted, and forms dismountable modular structure；The both sides end plate is connected with left and right binding post respectively；The electricity Pole plate upper and lower surface uniform fold fibrofelt, battery lead plate, which is horizontally staggered, to be arranged side by side, successively with left and right sides end plate connection；Electrode Plate, insulation frame and end plate form series connection fluid flow paths, liquid flowing channel upper and lower ends respectively with insulation frame on into and out of Fluid apertures connects.
- 2. according to the module described in claim 1, it is characterised in that：Two binding posts by wire with can Variable Polarity direct current Source connects.
- 3. according to the module described in claim 1, it is characterised in that：Described insulation frame uses lucite, to see liquid Body flow process in module.
- 4. according to the module described in claim 1, it is characterised in that：Described end plate be good conductivity conductive plate, except with electricity Outside the junction of pole plate and binding post, the uniform brushing insulated paint of end plate remaining surface.
- 5. according to the module described in claim 1, it is characterised in that：Described fibrofelt passes through insulating cement adhesion with battery lead plate.
- 6. according to the module described in claim 1, it is characterised in that：Described battery lead plate sets 8 ~ 500.
- 7. according to the module described in claim 1, it is characterised in that：Two groups of described electric adsorption liquid processing module and more than It is used in parallel or in series.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720112098.9U CN206886765U (en) | 2017-02-07 | 2017-02-07 | A kind of electric adsorption liquid processing module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720112098.9U CN206886765U (en) | 2017-02-07 | 2017-02-07 | A kind of electric adsorption liquid processing module |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206886765U true CN206886765U (en) | 2018-01-16 |
Family
ID=61328249
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720112098.9U Active CN206886765U (en) | 2017-02-07 | 2017-02-07 | A kind of electric adsorption liquid processing module |
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| Country | Link |
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| CN (1) | CN206886765U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108373189A (en) * | 2018-03-13 | 2018-08-07 | 国网浙江省电力有限公司电力科学研究院 | Remove the device and method of valve cooling system toner |
| CN109133451A (en) * | 2018-08-21 | 2019-01-04 | 安徽安成工业设备有限公司 | A kind of industrial circulating cooling water technique of zero discharge |
| CN111825171A (en) * | 2020-06-12 | 2020-10-27 | 武汉尚源新能环境有限公司 | Preparation method of mesoporous carbon electrode and organic wastewater treatment equipment |
| CN112759042A (en) * | 2020-12-30 | 2021-05-07 | 安徽三江水务工程有限公司 | Industrial wastewater desalting equipment and desalting method using same |
-
2017
- 2017-02-07 CN CN201720112098.9U patent/CN206886765U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108373189A (en) * | 2018-03-13 | 2018-08-07 | 国网浙江省电力有限公司电力科学研究院 | Remove the device and method of valve cooling system toner |
| CN109133451A (en) * | 2018-08-21 | 2019-01-04 | 安徽安成工业设备有限公司 | A kind of industrial circulating cooling water technique of zero discharge |
| CN111825171A (en) * | 2020-06-12 | 2020-10-27 | 武汉尚源新能环境有限公司 | Preparation method of mesoporous carbon electrode and organic wastewater treatment equipment |
| CN112759042A (en) * | 2020-12-30 | 2021-05-07 | 安徽三江水务工程有限公司 | Industrial wastewater desalting equipment and desalting method using same |
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Legal Events
| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240401 Address after: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen Patentee after: CHINA PETROLEUM & CHEMICAL Corp. Country or region after: China Patentee after: Sinopec (Dalian) Petrochemical Research Institute Co.,Ltd. Address before: 100728 No. 22 North Main Street, Chaoyang District, Beijing, Chaoyangmen Patentee before: CHINA PETROLEUM & CHEMICAL Corp. Country or region before: China Patentee before: DALIAN RESEARCH INSTITUTE OF PETROLEUM AND PETROCHEMICALS, SINOPEC Corp. |