CN205874103U - Electrochemistry sewage treatment plant - Google Patents

Electrochemistry sewage treatment plant Download PDF

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Publication number
CN205874103U
CN205874103U CN201620853212.9U CN201620853212U CN205874103U CN 205874103 U CN205874103 U CN 205874103U CN 201620853212 U CN201620853212 U CN 201620853212U CN 205874103 U CN205874103 U CN 205874103U
Authority
CN
China
Prior art keywords
case
sedimentation tank
treatment plant
booster pump
battery lead
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
CN201620853212.9U
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Chinese (zh)
Inventor
秦山
叶记飞
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.)
Anhui University of Science and Technology
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Anhui University of Science and Technology
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 Anhui University of Science and Technology filed Critical Anhui University of Science and Technology
Priority to CN201620853212.9U priority Critical patent/CN205874103U/en
Application granted granted Critical
Publication of CN205874103U publication Critical patent/CN205874103U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses an electrochemistry sewage treatment plant, including water intaking valve, booster pump, integration case, plate electrode, rotating fan blade, fe3+ solution tank, fe3+ measuring pump, sedimentation tank, many filter medium filtration net, outlet valve, it is the cuboid form to fuse the case, the plate electrode is four to be fixed respectively on fusing case rectangle side, the booster pump is established on the square side of fusing the case, the water intaking valve is established on the side of fusing the case is kept away from to the booster pump, the fe3+ measuring pump is established on the side of booster pump is kept away from to the integration case, fe3+ solution tank is connected with the fe3+ measuring pump, rotating fan blade is the three lower extreme of establishing respectively at the plate electrode, the sedimentation tank is established and is kept away from the one end that fuses the case at the plate electrode. The utility model discloses utilize among the chemical reaction principle that 3 flocculence complex compounds of fe (OH) can adsorbed particle, use electric chemical reaction to make heavy metal cations reaction be adsorption precipitation separation again behind the not tolerant granule to play sewage treatment's effect.

Description

Electrochemistry sewage-treatment plant
Technical field
This utility model relates to environmental protection and energy saving technical field, particularly relates to a kind of electrochemistry sewage-treatment plant.
Background technology
Along with improving constantly and industrial expansion of people's living standard, resident living sewage and trade effluent are also Increasing, present sewage also has substantial amounts of Organic substance and heavy metal ion, present electrochemistry sewage-treatment plant is also More and more, Organic substance is mainly processed by microbial decomposition, and the heavy metal contained in the sewage of required process with Not being single kind, often various heavy depositing, these heavy metal ion are the biggest to the threat of environment structure;Existing electricity When chemical sewage treatment device processes the sewage containing heavy metal, the metal ion that positive plate discharges is diffused into the most timely In water body, easily there is passivation phenomenon in positive electricity pole plate, thus causes the sewage disposal time long, and energy consumption is high, active substance is released into inequality The problem such as moisture content even, dregs are higher and continuity of operation is poor.
Utility model content
The purpose of this utility model is to solve shortcoming present in prior art, and a kind of electrochemistry sewage proposed Processing means.
To achieve these goals, this utility model adopts the technical scheme that
A kind of electrochemistry sewage-treatment plant, including water intaking valve, booster pump, fusion case, battery lead plate, rotary fan, Fe3+Molten Liquid case, Fe3+Dosing pump, sedimentation tank, multi-medium filtering net, outlet valve, described fusion case is rectangular-shaped, and described battery lead plate is four Individual being separately fixed at is merged in case rectangle sides, and described booster pump is located in the square sides merging case, and described water intaking valve sets On the booster pump side away from fusion case, described Fe3+Dosing pump is located at fusion case away from the side of booster pump, described Fe3+ Liquor box and Fe3+Dosing pump is connected, and described rotary fan is three lower ends being respectively provided at battery lead plate, and described sedimentation tank is located at Battery lead plate is away from one end of fusion case, and described multi-medium filtering net is fixed on the side of sedimentation tank, described outlet valve and sedimentation tank It is connected.
Preferably, described connecting plate is connected with the external high pressure pulse power.
Preferably, described battery lead plate uses metal platinum to make.
Preferably, pipe flange is used to be connected between described fusion case, battery lead plate and sedimentation tank.
Preferably, it is respectively provided with sewage draining valve bottom described fusion pond and sedimentation tank.
Preferably, described rotary fan utilizes motor braking, described motor model to be Y90S-2.
The beneficial effects of the utility model are: be provided with booster pump at water intaking valve, accelerate water velocity, and sewage is merging case Time interior, Fe3+Dosing pump can discharge Fe3+Entering and merge inside case, flow velocity is the fastest, with Fe3+Fusion speed faster, now can produce Raw Fe (OH)3Flocculence complex, suspends in merging pond sewage, in current enter battery lead plate afterwards, the negative electrode of battery lead plate Anion heavy metal ion in sewage is combined generation precipitation granule, and floccule then can will condense granule, lower disconnected rotation Rotary fan accelerates the circulation of gig, prevents concretion from condensing upon on motor plate thus produces passivation phenomenon, and current accelerate stream such as To becoming precipitate and separate in battery, separate through multi-medium filtering net;This utility model utilizes Fe in chemical reaction (OH)3Flocculence network Compound can the principle of adsorption particle, use electrochemical reaction to make heavy metal cation reaction heavy in not allowing after composition granule absorption again Form sediment and separate, thus play the effect of sewage disposal.
Accompanying drawing explanation
Fig. 1 is the top view of a kind of electrochemistry sewage-treatment plant that the utility model proposes.
Fig. 2 is the position signal of a kind of electrochemistry sewage-treatment plant battery lead plate and the rotary fan that the utility model proposes Figure.
In figure: 1 water intaking valve, 2 booster pumps, 3 fusion case, 4 battery lead plates, 5 rotary fans, 6Fe3+Liquor box, Fe3+Meter Amount pump 7,8 sedimentation tank, 9 multi-medium filtering nets, 10 outlet valves.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole Embodiment.
With reference to Fig. 1-2, a kind of electrochemistry sewage-treatment plant, including water intaking valve 1, booster pump 2, merge case 3, battery lead plate 4, Rotary fan 5, Fe3+Liquor box 6, Fe3+Dosing pump 7, sedimentation tank 8, multi-medium filtering net 9, outlet valve 10, the model of booster pump 2 For PW-175EA, Fe3+The model of dosing pump 7 is GB-S, merges case 3 in rectangular-shaped, and battery lead plate 4 is four and is separately fixed at and melts In mould assembling 3 rectangle sides, booster pump 2 is located in the square sides merging case 3, and water intaking valve 1 is located at booster pump 2 away from merging case On the side of 3, Fe3+Dosing pump 7 is located on the fusion case 3 side away from booster pump 2, Fe3+Liquor box 6 and Fe3+Dosing pump 7 phase Connecting, rotary fan 5 is three lower ends being respectively provided at battery lead plate 4, and sedimentation tank 8 is located at battery lead plate 4 away from merging the one of case 3 End, multi-medium filtering net 9 is fixed on the side of sedimentation tank 8, and outlet valve 10 is connected with sedimentation tank 8;Connecting plate 4 and external high pressure The pulse power is connected;Battery lead plate 4 uses metal platinum to make;Merge case 3, between battery lead plate 4 and sedimentation tank 8, use pipe flange Connect;Merge pond 3 and be respectively provided with sewage draining valve bottom sedimentation tank 4;Rotary fan 5 utilizes motor braking, motor model to be Y90S- 2。
It is provided with booster pump 2 at water intaking valve 1, accelerates water velocity, when sewage is in fusion case 3, Fe3+Dosing pump 7 can be released Put Fe3+Entering and merge case 3 inside, flow velocity is the fastest, with Fe3+Fusion speed faster, now can produce a small amount of Fe (OH)3Flocculence Complex, suspends in merging pond 3 sewage, in current enter battery lead plate 4 afterwards, and the anion of the negative electrode of battery lead plate 4 and sewage In heavy metal ion combine and produce precipitation granule, floccule then can will condense granule, and lower disconnected rotary fan 5 accelerates rotation Turning the circulation of thing, prevent concretion from condensing upon on motor plate 5 thus produce passivation phenomenon, it is heavy that current accelerate in stream such as arrives into battery Form sediment and separate, separate 9 through multi-medium filtering net;This utility model utilizes Fe in chemical reaction (OH)3Flocculence complex can be inhaled The principle of attached granule, use electrochemical reaction make heavy metal cation reaction in not allowing after composition granule adsorption precipitation again to separate, from And play the effect of sewage disposal.
Sewage flows in device through water intaking valve 1, adds people Fe in merging case 33+, flow into afterwards in battery lead plate 4, battery lead plate 4 it Between be electrolysed water produce anion OH-With Fe3+Producing flocculate, other metal ions also can produce precipitation granule, flocculate meeting Condensing granule on its surface, flow velocity accelerated by rotated fan 5, prevents precipitate from assembling, enters sedimentation tank afterwards and precipitates, after warp Multi-medium filtering net 9 filters floccule and granule foreign, for removing the metal ion in water, thus plays cleaning water quality and makees With.
The above, only this utility model preferably detailed description of the invention, but protection domain of the present utility model is not Being confined to this, any those familiar with the art is in the technical scope that this utility model discloses, according to this practicality Novel technical scheme and utility model thereof conceive equivalent or change in addition, all should contain at protection model of the present utility model Within enclosing.

Claims (6)

1. an electrochemistry sewage-treatment plant, it is characterised in that: include water intaking valve, booster pump, fusion case, battery lead plate, rotation Flabellum, Fe3+Liquor box, Fe3+Dosing pump, sedimentation tank, multi-medium filtering net, outlet valve, described fusion case is rectangular-shaped, institute State battery lead plate be four be separately fixed at fusion case rectangle sides on, described booster pump be located at merge case square sides on, Described water intaking valve is located on the booster pump side away from fusion case, described Fe3+Dosing pump is located at the side merging case away from booster pump On face, described Fe3+Liquor box and Fe3+Dosing pump is connected, and described rotary fan is three lower ends being respectively provided at battery lead plate, Described sedimentation tank is located at battery lead plate one end away from fusion case, and described multi-medium filtering net is fixed on the side of sedimentation tank, described Outlet valve is connected with sedimentation tank.
A kind of electrochemistry sewage-treatment plant the most according to claim 1, it is characterised in that: described connecting plate is high with outside The pressure pulse power is connected.
A kind of electrochemistry sewage-treatment plant the most according to claim 1, it is characterised in that: described battery lead plate uses metal Platinum is made.
A kind of electrochemistry sewage-treatment plant the most according to claim 1, it is characterised in that: described fusion case, battery lead plate It is connected with using pipe flange between sedimentation tank.
A kind of electrochemistry sewage-treatment plant the most according to claim 1, it is characterised in that: described fusion pond and sedimentation tank Bottom is respectively provided with sewage draining valve.
A kind of electrochemistry sewage-treatment plant the most according to claim 1, it is characterised in that: described rotary fan utilizes electricity Mechanism is dynamic, and described motor model is Y90S-2.
CN201620853212.9U 2016-08-08 2016-08-08 Electrochemistry sewage treatment plant Expired - Fee Related CN205874103U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620853212.9U CN205874103U (en) 2016-08-08 2016-08-08 Electrochemistry sewage treatment plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620853212.9U CN205874103U (en) 2016-08-08 2016-08-08 Electrochemistry sewage treatment plant

Publications (1)

Publication Number Publication Date
CN205874103U true CN205874103U (en) 2017-01-11

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620853212.9U Expired - Fee Related CN205874103U (en) 2016-08-08 2016-08-08 Electrochemistry sewage treatment plant

Country Status (1)

Country Link
CN (1) CN205874103U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108238702A (en) * 2018-01-25 2018-07-03 詹胜超 A kind of urban wastewater treatment device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108238702A (en) * 2018-01-25 2018-07-03 詹胜超 A kind of urban wastewater treatment device

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

Granted publication date: 20170111

Termination date: 20170808

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