CN203878229U - Electrolytic tank organic phase recovery device - Google Patents
Electrolytic tank organic phase recovery device Download PDFInfo
- Publication number
- CN203878229U CN203878229U CN201420283267.1U CN201420283267U CN203878229U CN 203878229 U CN203878229 U CN 203878229U CN 201420283267 U CN201420283267 U CN 201420283267U CN 203878229 U CN203878229 U CN 203878229U
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- China
- Prior art keywords
- organic phase
- phase recovery
- accumulator tank
- mortar pump
- electrolytic tank
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model discloses an electrolytic tank organic phase recovery device. The electrolytic tank organic phase recovery device is characterized by comprising an organic phase suction pipe, a mortar pump and an organic phase recovery groove, wherein the outlet end of the mortar pump is connected to the top of the organic phase recovery groove by virtue of a pipeline; an air release valve is arranged on the side wall of the bottom of the organic phase recovery groove; a circulating pipeline is also arranged on the side wall of the bottom of the organic phase recovery groove; the circulating pipeline is connected to the suction end of the mortar pump; the organic phase suction pipe is connected to the circulating pipeline; a valve and a flow plug are arranged on the circulating pipeline. By adopting the electrolytic tank organic phase recovery device, the difficult problems that organic matter of a wet-process electric copper electrolytic tank is difficult to clean and extract can be solved.
Description
Technical field
The utility model belongs to mechanical means, relates in particular to a kind of electrolyzer organic phase retrieving arrangement.
Background technology
Many organism 13(, after long-play, can be piled up referring to Fig. 1 in electrodeposition workshop on electrolyzer 11 liquid levels 12).Because any solvent extraction system is after long time running, the volatilization of extraction agent and thinner, degraded, degradation reason under surfactivity and surface tension, cause phase-splitting slack-off, the generation of emulsion is entrained with a large amount of organic phase small dropletss after causing the back extraction of poor copper electric effusion, through oil eliminator oil removing, thoroughly do not enter electrodeposition system, because electrolytic deposition process temperature is high, electrolytic process anode produces oxygen, organic phase small droplets in electrolytic solution is taken out of, cause the floating a large amount of organic phase of electrolyzer cathode-anode plate liquid level periphery, badly influence the apparent mass of cathode copper, and can cause machine burning plate, shorten the stainless steel cathode plate life-span, thereby greatly increase production cost.
It is a difficult problem of hydrometallurgy industry that organism reclaims problem always.In prior art, electrodeposition system electrolyzer can only pass through the manually organism to Winning cell two ends liquid-inlet pipe and overflow port place with screen cloth, organism in middle cathode-anode plate gap is because narrow space, never having good way removes, with the screen cloth of making, fishing for organism causes input duct, flase floor platform to drip organic phase everywhere, badly influence the attractive in appearance of workshop, generally, the organic rate of recovery can only reach 50%.
Utility model content
The problem that the purpose of this utility model exists for prior art, provides a kind of electrolyzer organic phase retrieving arrangement.
Above-mentioned purpose realizes by following proposal:
An electrolyzer organic phase retrieving arrangement, is characterized in that, described retrieving arrangement comprises organic phase suction pipe, mortar pump, organic phase accumulator tank; The exit end of described mortar pump is connected to the top of described organic phase accumulator tank by pipeline; In the bottom of described organic phase accumulator tank, sidewall is provided with blow-off valve, in the bottom of described organic phase accumulator tank, sidewall also arranges circulation line, this circulation line is connected to the suction side of described mortar pump, described organic phase suction pipe is connected on described circulation line, and is provided with valve and flow plug on described circulation line; The outlet end of described mortar pump connects circulatory mediator pipeline, and described circulatory mediator pipeline accesses the top of described organic phase accumulator tank.
Retrieving arrangement according to above-mentioned, is characterized in that, described organic phase suction pipe comprises 2 pipelines.
The beneficial effects of the utility model: the utility model has solved the difficult problems such as electricity of wet process copper electrolysis cells organism difficulty is cleared up, hard-pumped is got, overcome in the past that cathode-anode plate gap is little causes the problems such as operation inconvenience, bad absorption is organic, the feature such as have that operation of equipment is simple, simple structure, accessory are easily purchased, draft is large.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Referring to Fig. 1, electrolyzer organic phase retrieving arrangement of the present utility model comprises organic phase suction pipe 1, mortar pump 2, organic phase accumulator tank 3.Mortar pump 2 belongs to cantilevered single stage single suction volute pump, and its exit end is connected to the top of organic phase accumulator tank 3 by pipeline.In the bottom of organic phase accumulator tank 3, sidewall is provided with blow-off valve 4, for the organic liquid that is deposited on bottom after separated with solution left standstill of emptying groove.In the bottom of organic phase accumulator tank 3, sidewall also arranges circulation line 5, and circulation line 5 is connected to the suction side of mortar pump 2, and organic phase suction pipe 1 is connected on circulation line 5, and on circulation line 5, is provided with valve 6 and flow plug 7.The outlet end of mortar pump 2 connects circulatory mediator pipeline 10, the top of circulatory mediator pipeline 10 access organic phase accumulator tanks 3.For the ease of operated by two people, organic phase suction pipe can comprise 2 pipelines.
Electrolyzer organic phase retrieving arrangement workflow and principle are as follows:
1. before retrieving arrangement operation, first by suction culvert 9, in organic phase accumulator tank 3, fill with water, as circulatory mediator.In follow-up operation process, utilize electrolytic solution 14 that organic phase accumulator tank 3 bottoms separate as circulatory mediator.
2. start mortar pump 2, when impeller rotates clockwise, circulatory mediator is thrown to surrounding by impeller, and due to the effect of centrifugal force, circulatory mediator has formed a closed circle that is similar to equal thickness that is decided by pump chamber shape.
3. in conjunction with vacuum pump principle, the upper part internal surface of water ring is lucky and impeller hub is tangent, and the lower inner surface of water ring just contacts with blade tip.Now between impeller hub and water ring, form a crescent-shaped space, and this space is divided into by impeller several loculuses that lobe numbers equates.If take the top of impeller is 0 degree starting point, the volume of impeller 180 loculuses while spending before rotation changes from small to big so, and communicates with the liquid sucting port on end face, and this circulatory mediator is inhaled into, when air-breathing at the end loculus isolated with liquid sucting port; When impeller continues rotation, loculus from large to small, makes circulatory mediator compressed; When loculus communicates with leakage fluid dram, circulatory mediator is just discharged from outside pump.Impeller often rotates a circle, and blade suction, discharge opeing once, if work without cessation, are reequiped and so forth pump and just continuously aspirated or delivery cycle medium, produce super large negative pressure of vacuum suction.In addition, at circulating line 5, install flow plug 7 additional, make 2 suction pressure in organic phase suction pipe 1 increase 1 times, and draw organic stability of flow.
4. workman grips has the portable special withdrawer (being organic phase suction pipe 1) of negative pressure of vacuum to draw Winning cell liquid level top organism, by control valve 8, operate the organic phase of drawing on liquid level of electrolyzer, organic phase and part electrolytic solution enter into repacking buffering twin flue again through repacking pump through connecting hose, organic phase and circulatory mediator enter into organic phase accumulator tank through pump outlet, organic phase standing for some time in accumulator tank can go out top organic phase 15 by clarified separation, thereby completes the organic phase recovery of Winning cell liquid level.
5. circulatory mediator per tour is changed once, and the electrolytic solution of bottom is entered after trench and returned in electrolyzer after collection and purification by blow-off valve 4, then fills into new water as circulatory mediator, each circulation fluid volume of changing just 0.5m3, there is not water expansion issues.And reaching certain volume, organism carries out next activation treatment being drained into recycling bin.
Claims (2)
1. an electrolyzer organic phase retrieving arrangement, is characterized in that, described retrieving arrangement comprises organic phase suction pipe, mortar pump, organic phase accumulator tank; The exit end of described mortar pump is connected to the top of described organic phase accumulator tank by pipeline; In the bottom of described organic phase accumulator tank, sidewall is provided with blow-off valve, in the bottom of described organic phase accumulator tank, sidewall also arranges circulation line, this circulation line is connected to the suction side of described mortar pump, described organic phase suction pipe is connected on described circulation line, and is provided with valve and flow plug on described circulation line; The outlet end of described mortar pump connects circulatory mediator pipeline, and described circulatory mediator pipeline accesses the top of described organic phase accumulator tank.
2. retrieving arrangement according to claim 1, is characterized in that, described organic phase suction pipe comprises 2 pipelines.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420283267.1U CN203878229U (en) | 2014-05-30 | 2014-05-30 | Electrolytic tank organic phase recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420283267.1U CN203878229U (en) | 2014-05-30 | 2014-05-30 | Electrolytic tank organic phase recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203878229U true CN203878229U (en) | 2014-10-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420283267.1U Active CN203878229U (en) | 2014-05-30 | 2014-05-30 | Electrolytic tank organic phase recovery device |
Country Status (1)
| Country | Link |
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| CN (1) | CN203878229U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108744616A (en) * | 2018-07-03 | 2018-11-06 | 中铁资源集团有限公司 | A kind of fishing device of flocculate for being generated in extraction process |
-
2014
- 2014-05-30 CN CN201420283267.1U patent/CN203878229U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108744616A (en) * | 2018-07-03 | 2018-11-06 | 中铁资源集团有限公司 | A kind of fishing device of flocculate for being generated in extraction process |
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| C14 | Grant of patent or utility model | ||
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