CN204981274U - Little electrolytic reaction jar - Google Patents
Little electrolytic reaction jar Download PDFInfo
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- CN204981274U CN204981274U CN201520662451.1U CN201520662451U CN204981274U CN 204981274 U CN204981274 U CN 204981274U CN 201520662451 U CN201520662451 U CN 201520662451U CN 204981274 U CN204981274 U CN 204981274U
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- tank body
- sewer line
- micro
- electrolysis reaction
- aerated conduit
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Abstract
The utility model provides a little electrolytic reaction jar, including a jar body (2), inlet tube (7), intake pipe (8) and outlet pipe (3), the jar body (2) is the cavity cavity, set up bottom the jar body (2) inner chamber aerated conduit (11) and sewer line (10), in aerated conduit (11), set up the through -hole on sewer line (10) respectively, aerated conduit (11) and intake pipe (8) intercommunication, sewer line (10) and inlet tube (7) intercommunication, outlet pipe (3) are located sewer line (10) top and communicate with the jar body (2) inner chamber, outlet pipe (3) exit end, inlet tube (7) entrance point and intake pipe (8) exit end all expose in the jar body (2). The utility model discloses an aerated conduit and sewer line serve as indisputable carbon filler's supporting layer simultaneously, and the structure is compacter, and area is few, and implementation cost is low, are suitable for very much the useless treatment of water of water -based ink of low discharge, have the use, move outstanding advantages such as convenient, that sewage treatment is effectual.
Description
Technical field
The utility model relates to technical field of sewage treatment equipment, especially relates to a kind of micro-electrolysis reaction tank of process water color ink waste water.
Background technology
A kind of waste water produced in water color ink waste water mainly packed in cases industry printing workshop section cleaning equipment process, sewage quantity is little, and water quality is unstable, and colourity, turbidity are large, and biodegradability is poor.The main component of water color ink waste water is water soluble resin, and it can unstability remove in acid condition, therefore, often adopts acid out-this type of sewage of weak electrolysis mechanism process, removes Colority of Sewage Water, turbidity, improve the object of Biodegradability of Wastewater simultaneously to reach.
Because acid out-weak electrolysis mechanism adopts the micro-electrolysis reaction pond of traditional civil engineering structure to process this type of sewage, and the micro-electrolysis reaction pond of traditional civil engineering structure needs to do waterproof, acid-alkali-corrosive-resisting process, cost of investment is larger, and floor space is also larger, use dumb, be unsuitable for the sewage disposal of low discharge.
Utility model content
The technical problems to be solved in the utility model is: for prior art Problems existing, a kind of micro-electrolysis reaction tank is provided, sewage disposal can be carried out for the water color ink waste water of low discharge, not only use, operate and conveniently moving, and floor space is little, implementation cost is low.
The technical problems to be solved in the utility model realizes by the following technical solutions: a kind of micro-electrolysis reaction tank, comprise tank body, water inlet pipe and inlet pipe and rising pipe, described tank body is hollow cavity, aerated conduit and sewer line are set bottom tank inner chamber, at aerated conduit, some through holes offered respectively by sewer line, described aerated conduit is communicated with inlet pipe, described sewer line is communicated with water inlet pipe, described rising pipe to be positioned at above sewer line and to be communicated with tank inner chamber, described rising pipe exit end, water inlet pipe entrance end and inlet pipe exit end all expose to tank body.
Preferably, arrange support rim bottom described tank inner chamber, described aerated conduit, sewer line are installed on support rim.
Preferably, described support rim is stepped boss, and described sewer line is positioned at above aerated conduit.
Preferably, the opening direction of the through hole on described aerated conduit points to bottom tank inner chamber.
Preferably, described sewer line and/or aerated conduit are circulating lines.
Preferably, also comprise annular V-notch weir, described V-notch weir is fixedly connected on tank inner chamber, and jointly forms annular collecting vat with tank inner chamber wall, and described rising pipe is communicated with water leg.
Preferably, also comprise blow-off pipe, described blow-off pipe is near tank body bottom and be communicated with tank inner chamber.
Preferably, also comprise upflow tube, described upflow tube position higher than rising pipe position, and is communicated with tank inner chamber.
Preferably, described tank body is the tank body that PP material is made.
Preferably, loose joint is adopted to be interconnected between described water inlet pipe and sewer line.
Compared with prior art, the beneficial effects of the utility model are: the aerated conduit arranged bottom tank inner chamber and sewer line can serve as the supporting layer of iron carbon filler simultaneously, after needing sewage to be processed constantly to enter sewer line from water inlet pipe, sewage in sewer line constantly flows out in tank inner chamber by the through hole on it, directly contact with iron carbon filler after sewage flows out sewer line and carry out micro-electrolysis reaction, simultaneously, ventilated to send into oxygen in the sewage in tank inner chamber to aerated conduit by inlet pipe, according to practical situation, aeration time is set, to ensure light electrolysis effect, sewage after microelectrolysis processing from the bottom up after stopping fully, flows out tank body to subsequent processing finally by rising pipe in tank inner chamber.The sewage disposal part of this micro-electrolysis reaction tank is all arranged in tank inner chamber, compact construction, and volume is little, floor space is few, and implementation cost is also low, and the water color ink waste water be suitable for for low discharge carries out sewage disposal, use, operation, mobile all convenient, and good sewage processing effect.
Accompanying drawing explanation
Fig. 1 is the constructing stereo figure of a kind of micro-electrolysis reaction tank of the utility model.
Fig. 2 is the front view (part sectioned view) of a kind of micro-electrolysis reaction tank of the utility model.
Fig. 3 is the vertical view of a kind of micro-electrolysis reaction tank of the utility model.
Fig. 4 be in Fig. 2 A-A to sectional view.
Fig. 5 be in Fig. 4 B-B to sectional view.
Fig. 6 is the partial enlarged drawing (the perforate mode schematic diagram of aerated conduit) at C place in Fig. 5.
Figure middle part product token name claims: 1-blow-off pipe, 2-tank body, 3-rising pipe, 4-V-notch weir, 5-motor mounting plate, 6-upflow tube, 7-water inlet pipe, 8-inlet pipe, 9-water leg, 10-sewer line, 11-aerated conduit, 12-loose joint, 13-threeway, 14-support rim, 15-elbow.
Embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with the drawings and specific embodiments, the utility model is described in detail.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
A kind of micro-electrolysis reaction tank as shown in Figure 1, Figure 2, Figure 3 shows, mainly comprise cylindrical tank body 2, water inlet pipe 7, inlet pipe 8, rising pipe 3 and aerated conduit 11 and sewer line 10, described tank body 2 is hollow cavity, its one end is closed, the other end opening, be fixedly connected with motor mounting plate 5 at the opening end of tank body 2, to facilitate, agitator motor be directly installed on micro-electrolysis reaction tank by motor mounting plate 5.Described sewer line 10 is the circulating lines be formed by connecting by elbow 15 and straight pipeline, described aerated conduit 11 is also the circulating line be formed by connecting by elbow 15 and straight pipeline, tank body 2 intracavity bottom is provided with stair-stepping support rim 14, described aerated conduit 11, sewer line 10 are installed on support rim 14, and sewer line 10 is positioned at above aerated conduit 11, described rising pipe 3 to be positioned at above sewer line 10 and with tank body 2 inner space.Described inlet pipe 8 is interconnected by threeway 13 and aerated conduit 11, loose joint 12 can also be adopted to be interconnected, as shown in Figure 2, Figure 4 shows between described threeway 13 and inlet pipe 8.Similarly, described water inlet pipe 7 also can be interconnected by threeway and sewer line 10, and loose joint 12 also can be adopted between described threeway and water inlet pipe 7 to be interconnected, as shown in Fig. 2, Fig. 5.Described rising pipe 3 exit end, water inlet pipe 7 entrance end and inlet pipe 8 exit end all expose to tank body 2, as shown in Fig. 1, Fig. 3, Fig. 5, wherein, described loose joint 12 is a kind of pipe jointer parts facilitating dismounting between pipeline, adopt loose joint 12 can facilitate the dismounting of aerated conduit 11, sewer line 10, to clean micro-electrolysis reaction tank and aerated conduit 11, sewer line 10, ensure the wastewater treatment efficiency of micro-electrolysis reaction tank.
As shown in Fig. 3, Fig. 4, Fig. 5, Fig. 6, some through holes offered by sewer line 10, these through hole environmental pollution waterpipe 10 even circumferentials distribute; Similarly, some through holes also offered by aerated conduit 11, these through holes are also equidistantly be evenly distributed on aerated conduit 11.It is pointed out that as shown in Figure 6, when hole opened by aerated conduit 11, preferably reverse side boring is carried out to aerated conduit 11, namely preferably ensure that the opening direction of the through hole that aerated conduit 11 is offered points to tank body 2 intracavity bottom.After adopting above-mentioned pipeline configuration, the sewage in sewer line 10 not only can be made evenly to flow out sewer line 10, and be evenly distributed on each position of tank body 2 inner chamber, and the uniform aeration of tank body 2 inner chamber can be guaranteed, described aerated conduit 11 and these two circulating lines of sewer line 10 can be used as the supporting layer of iron carbon filler simultaneously, also increase the contact area between the sewage in iron carbon filler and tank body 2 inner chamber simultaneously, therefore, can make to enter the sewage in tank body 2 inner chamber, air (oxygen) and iron carbon filler can be carried out fully directly contacting to carry out micro-electrolysis reaction, aeration time can be set according to practical situation simultaneously, thus significantly enhance the light electrolysis effect of sewage.
As shown in Figure 1, Figure 2, Figure 4 shows, annular V-notch weir 4 is fixedly connected with on tank body 2 inner chamber top, its top indention, described V-notch weir 4 forms annular collecting vat 9 jointly with tank body 2 internal chamber wall, described rising pipe 3 is communicated with water leg 9, adopt this structure can avoid the directly overflow because of excessive rolling of sewage in aeration, ensure sewage in tank body 2 inner chamber from bottom to top after fully stopping again overflow to subsequent processing.As shown in Figure 1, tank body 2 is also fixedly connected with blow-off pipe 1 and upflow tube 6, described blow-off pipe 1 is mutually through with tank body 2 inner chamber near tank body 2 bottom, and described upflow tube 6 position is higher than rising pipe 3 position, and mutually through with tank body 2 inner chamber.Micro-electrolysis reaction tank can be facilitated can to clear up sewage in tank body 2 inner chamber when overhauling by arranging blow-off pipe 1; When can prevent system malfunctions by arranging upflow tube 6, sewage diffuses out micro-electrolysis reaction tank.
Consider that the sewage carrying out light electrolysis in micro-electrolysis reaction tank is generally acidity, there is corrodibility.Therefore, described tank body 2 adopts the PP material of acid-alkali-corrosive-resisting to make, and meanwhile, tubular tank body 2 is not yielding yet, thus can extend the work-ing life of micro-electrolysis reaction tank, and is conducive to the weight alleviating micro-electrolysis reaction tank, convenient mobile.The amount of the water color ink waste water produced due to most of package plant is 10-15 cubic meter every day, if the useful volume design of micro-electrolysis reaction tank of the present utility model is into about 1.37 cubic metres, with equipment to work every day 20 hours, the residence time of sewage in tank body 2 calculate for 0.5-1 hour, this micro-electrolysis reaction tank maximum process sewage quantity every day can reach 27.4 cubic metres.Therefore, the utility model is highly suitable for small sewage treatment plant (containing most of package plant) and carries out sewage disposal for the water color ink waste water of low discharge, and implementation cost is also low.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; it should be pointed out that all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. a micro-electrolysis reaction tank, it is characterized in that: comprise tank body (2), water inlet pipe (7) and inlet pipe (8) and rising pipe (3), described tank body (2) is hollow cavity, at tank body (2) intracavity bottom, aerated conduit (11) and sewer line (10) are set, in aerated conduit (11), (10) offer some through holes respectively with sewer line, described aerated conduit (11) is communicated with inlet pipe (8), described sewer line (10) is communicated with water inlet pipe (7), described rising pipe (3) be positioned at sewer line (10) top and with tank body (2) inner space, described rising pipe (3) exit end, water inlet pipe (7) entrance end and inlet pipe (8) exit end all expose to tank body (2).
2. a kind of micro-electrolysis reaction tank according to claim 1, it is characterized in that: described tank body (2) intracavity bottom arranges support rim (14), described aerated conduit (11), sewer line (10) are installed on support rim (14).
3. a kind of micro-electrolysis reaction tank according to claim 2, is characterized in that: described support rim (14) is stepped boss, and described sewer line (10) is positioned at aerated conduit (11) top.
4. a kind of micro-electrolysis reaction tank according to any one of claim 1-3, is characterized in that: the opening direction of the through hole on described aerated conduit (11) points to tank body (2) intracavity bottom.
5. a kind of micro-electrolysis reaction tank according to any one of claim 1-3, is characterized in that: described sewer line (10) and/or aerated conduit (11) are circulating lines.
6. a kind of micro-electrolysis reaction tank according to any one of claim 1-3, it is characterized in that: also comprise annular V-notch weir (4), described V-notch weir (4) is fixedly connected on tank body (2) inner chamber, and jointly forming annular collecting vat (9) with tank body (2) internal chamber wall, described rising pipe (3) is communicated with water leg (9).
7. a kind of micro-electrolysis reaction tank according to any one of claim 1-3, is characterized in that: also comprise blow-off pipe (1), described blow-off pipe (1) near tank body (2) bottom and with tank body (2) inner space.
8. a kind of micro-electrolysis reaction tank according to any one of claim 1-3, it is characterized in that: also comprise upflow tube (6), described upflow tube (6) position higher than rising pipe (3) position, and with tank body (2) inner space.
9. a kind of micro-electrolysis reaction tank according to claim 8, is characterized in that: described tank body (2) is the tank body that PP material is made.
10. a kind of micro-electrolysis reaction tank according to any one of claim 1-3, is characterized in that: adopt loose joint (12) to be interconnected between described water inlet pipe (7) and sewer line (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520662451.1U CN204981274U (en) | 2015-08-28 | 2015-08-28 | Little electrolytic reaction jar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520662451.1U CN204981274U (en) | 2015-08-28 | 2015-08-28 | Little electrolytic reaction jar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204981274U true CN204981274U (en) | 2016-01-20 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520662451.1U Active CN204981274U (en) | 2015-08-28 | 2015-08-28 | Little electrolytic reaction jar |
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| CN (1) | CN204981274U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110204111A (en) * | 2019-05-31 | 2019-09-06 | 优德太湖水务（苏州）有限公司 | A kind of dephosphorization system for sewage treatment |
| CN111717963A (en) * | 2020-06-29 | 2020-09-29 | 巢湖市科凌沃特水处理技术有限公司 | Iron-carbon micro-electrolysis device |
-
2015
- 2015-08-28 CN CN201520662451.1U patent/CN204981274U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110204111A (en) * | 2019-05-31 | 2019-09-06 | 优德太湖水务（苏州）有限公司 | A kind of dephosphorization system for sewage treatment |
| CN111717963A (en) * | 2020-06-29 | 2020-09-29 | 巢湖市科凌沃特水处理技术有限公司 | Iron-carbon micro-electrolysis device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170327 Address after: 610200 Chengdu, Sichuan, Hong Kong Industrial Park, Hong Kong double Park Plaza building, room 3, room 1303 Patentee after: Chengdu core Packaging Technology Co., Ltd. Address before: 610200 Fuling, Sichuan, Chengdu, Hong Kong Industrial Park, Hong Kong double Park Road, No. 8, No. 222, No. Patentee before: Chengdu Innovation Corrugated Paper Products Technology Co., Ltd. |
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| TR01 | Transfer of patent right |