CN204111890U - Electrolytic solution is automatically except scum silica frost device - Google Patents
Electrolytic solution is automatically except scum silica frost device Download PDFInfo
- Publication number
- CN204111890U CN204111890U CN201420666265.0U CN201420666265U CN204111890U CN 204111890 U CN204111890 U CN 204111890U CN 201420666265 U CN201420666265 U CN 201420666265U CN 204111890 U CN204111890 U CN 204111890U
- Authority
- CN
- China
- Prior art keywords
- silica frost
- scum silica
- collecting slot
- dreg collecting
- electrolytic solution
- 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
Links
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
A kind of electrolytic solution is automatically except scum silica frost device comprises clean solution tank (2), scum silica frost pond (4), helix wheel (5), dreg collecting slot (6), chain transmission system (7), impeller (8) etc.Utilize the flowing kinetic energy of lead channel (9) electrolytic solution to promote impeller (8) to rotate, helix wheel (5) is driven to rotate by chain transmission system (7), the spiral vane of helix wheel (5) promotes scum silica frost pond (4) surface and oil contaminant, scum and electrolytic solution and enters dreg collecting slot (6), make greasy dirt and scum be enriched in dreg collecting slot (6) liquid level, and electrolytic solution is refluxed into scum silica frost pond (4) by the through hole of dreg collecting slot (6) with scum silica frost pond (4).The utility model decreases electric energy loss, solves long-pending manganese, long-pending zinc returns molten problem, improve electrolytic production quality.
Description
Technical field
The utility model relates to hydrometallurgy electrolyte purification and removes slag technical field, particularly a kind of electrolytic solution automatically except scum silica frost device.
Background technology
At electrolytic manganese, during electrolytic zinc is produced, breeze is after sulfuric acid liquid leaching, obtain electrolytic solution, at this moment subparticle is had to suspend in electrolytic solution, electrolytic solution becomes muddy state, some greasy dirts and foamy slag is also had to produce, although removed slag by settling bowl sedimentation, but also have the foam materials such as some greasy dirts to exist, through the stirring of pump and Cemented filling to electrolyzer, the generation of greasy dirt and scum can be increased the weight of again, electrolytic solution with greasy dirt and scum enters electrolyzer, greasy dirt and scum can be bonded at the moon, on positive plate, affect the conductivity of pole plate and the electrochemical reaction rates of electrolysis and current efficiency, increase electric energy loss, the long-pending manganese caused, long-pending zinc returns molten problem, the impurity of greasy dirt and scum, electrolytic production quality and quality can be had a strong impact on, at high purity electrolytic manganese, electrolytic zinc is especially outstanding in producing, therefore last link wipe oil of electrolyzer is entered and foamy slag is even more important at electrolytic solution, what generally adopt now is nature press over system, but this method is degreasing and is also overflowing a large amount of electrolytic solution while scum, spillway discharge accounts for the 10-15% of input, the electrolytic solution inputting electrolyzer can be made like this to reduce a lot, although the electrolytic solution of overflow can reflux defeated again, spillway discharge can be regulated by overflow port, due to fluctuation and the turbulent phenomenon of fluid, how to accomplish the minimum and greasy dirt of spillway discharge and scum except cleanliness the highest, reach this trim point to be difficult to, now employing is also had manually to scrape method, need in high humidity and the continuous long-time operation of sour environment, labour intensity is large, affect healthy.
Summary of the invention
The purpose of this utility model is to provide a kind of quick, large discharge, and the electrolytic solution of automatic operation removes scum silica frost device automatically continuously.
Electrolytic solution of the present utility model is automatically except scum silica frost device comprises output tube, clean solution tank, upper lower clapboard, scum silica frost pond, helix wheel, dreg collecting slot, chain transmission system, impeller, lead channel.In lead channel built with impeller, on on scum silica frost pond and dreg collecting slot, helix wheel is housed, dreg collecting slot has the semicircle orifice of helix wheel diameter to communicate with scum silica frost pond in liquid level helix wheel position, through hole is had to communicate with scum silica frost pond below dreg collecting slot, lower clapboard is provided with in clean solution tank and bottom, scum silica frost pond, the passage that clean solution tank and scum silica frost pond are formed by upper lower clapboard communicates, helix wheel to be connected by chain transmission system by impeller and drives, output tube is arranged on clean solution tank upper position and lower than clean solution tank liquid level, clean solution tank, scum silica frost pond, dreg collecting slot and lead channel are the rectangular box of upper shed, the overflow port of dreg collecting slot is approximately higher than metal line.
When electrolytic solution enters lead channel, promote wheel rotation, helix wheel is driven to rotate by chain transmission system, the spiral vane of helix wheel promotes helix wheel place, scum silica frost pond surface and oil contaminant, scum and electrolytic solution enter dreg collecting slot, continuously advance, greasy dirt and scum are enriched in dreg collecting slot liquid level, and electrolytic solution refluxes into scum silica frost pond by the through hole in dreg collecting slot and scum silica frost pond, greasy dirt in dreg collecting slot and foam float and collect thicker and thicker, in the buoyancy of dreg collecting slot liquid level, higher than greasy dirt and the scum outflow dreg collecting slot of dreg collecting slot overflow port, because the overflow port of dreg collecting slot is approximately higher than metal line, so there is no the spilling of electrolytic solution, except the clean electrolytic solution of degreasing and scum enters clean solution tank from the separator channels up and down of bottom, scum silica frost pond, electrolyzer is input into by output tube.
A kind of electrolytic solution of the present utility model degreases and the device of scum automatically, and the spilling of electrolytic solution can not be caused, solve the technical problems such as hydrometallurgy electrolyte purification, greasy dirt and scum can not be bonded at yin, yang pole plate affects the conductivity of pole plate and the electrochemical reaction rates of electrolysis and current efficiency, reduce electric energy loss, solve long-pending manganese, long-pending zinc returns molten problem, improve electrolytic production quality and quality.
Accompanying drawing explanation
Accompanying drawing 1 is the utility model structural representation.
1, output tube 2, clean solution tank 3, upper lower clapboard 4, scum silica frost pond 5, helix wheel 6, dreg collecting slot 7, chain transmission system 8, impeller 9, lead channel.
Embodiment
As shown in drawings, electrolytic solution of the present utility model is automatically except scum silica frost device comprises output tube (1), clean solution tank (2), upper lower clapboard (3), scum silica frost pond (4), helix wheel (5), dreg collecting slot (6), chain transmission system (7), impeller (8), lead channel (9).In lead channel (9) built with impeller (8), on on scum silica frost pond (4) and dreg collecting slot (6), helix wheel (5) is housed, dreg collecting slot (6) has the semicircle orifice of helix wheel (5) diameter to communicate with scum silica frost pond (4) in liquid level helix wheel (5) position, dreg collecting slot (6) has through hole to communicate with scum silica frost pond (4) below, upper lower clapboard (3) is provided with in clean solution tank (2) and scum silica frost pond (4) bottom, the passage that clean solution tank (2) and scum silica frost pond (4) are formed by upper lower clapboard (3) communicates, helix wheel (5) is connected by impeller (8) by chain transmission system (7) and is driven, output tube (1) is arranged on clean solution tank (2) upper position and lower than clean solution tank (2) liquid level, clean solution tank (2), scum silica frost pond (4), dreg collecting slot (6) and lead channel (9) are the rectangular box of upper shed, the overflow port of dreg collecting slot (6) is approximately higher than metal line.
When electrolytic solution enters lead channel (9), promote impeller (8) to rotate, helix wheel (5) is driven to rotate by chain transmission system (7), the spiral vane of helix wheel (5) promotes scum silica frost pond (4) helix wheel (5) place surface and oil contaminant, scum and electrolytic solution enter dreg collecting slot (6), continuously advance, greasy dirt and scum are enriched in dreg collecting slot (6) liquid level, and electrolytic solution refluxes into scum silica frost pond (4) by dreg collecting slot (6) and the through hole in scum silica frost pond (4), greasy dirt in dreg collecting slot (6) and foam float and collect thicker and thicker, in the buoyancy of dreg collecting slot (6) liquid level, higher than greasy dirt and scum outflow dreg collecting slot (6) of dreg collecting slot (6) overflow port, because the overflow port of dreg collecting slot (6) is approximately higher than metal line, so there is no the spilling of electrolytic solution, except the clean electrolytic solution of degreasing and scum enters clean solution tank (2) from upper lower clapboard (3) passage of scum silica frost pond (4) bottom, electrolyzer is input into by output tube (1).
The utility model provide a kind of fast, large discharge, the continuously electrolytic solution of automatic operation degrease and the device of scum automatically, and the spilling of electrolytic solution can not be caused, solve the technical problems such as hydrometallurgy electrolyte purification, greasy dirt and scum can not be bonded at yin, yang pole plate affects the conductivity of pole plate and the electrochemical reaction rates of electrolysis and current efficiency, reduce electric energy loss, solve long-pending manganese, long-pending zinc returns molten problem, improve electrolytic production quality and quality.
Claims (1)
1. an electrolytic solution is automatically except scum silica frost device, comprise output tube (1), clean solution tank (2), upper lower clapboard (3), scum silica frost pond (4), helix wheel (5), dreg collecting slot (6), chain transmission system (7), impeller (8), lead channel (9), it is characterized in that in lead channel (9) built with impeller (8), on on scum silica frost pond (4) and dreg collecting slot (6), helix wheel (5) is housed, dreg collecting slot (6) has the semicircle orifice of helix wheel (5) diameter to communicate with scum silica frost pond (4) in liquid level helix wheel (5) position, dreg collecting slot (6) has through hole to communicate with scum silica frost pond (4) below, upper lower clapboard (3) is provided with in clean solution tank (2) and scum silica frost pond (4) bottom, the passage that clean solution tank (2) and scum silica frost pond (4) are formed by upper lower clapboard (3) communicates, helix wheel (5) is connected by impeller (8) by chain transmission system (7) and is driven, output tube (1) is arranged on clean solution tank (2) upper position and lower than clean solution tank (2) liquid level, clean solution tank (2), scum silica frost pond (4), dreg collecting slot (6) and lead channel (9) are the rectangular box of upper shed, the overflow port of dreg collecting slot (6) is approximately higher than metal line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420666265.0U CN204111890U (en) | 2014-11-11 | 2014-11-11 | Electrolytic solution is automatically except scum silica frost device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420666265.0U CN204111890U (en) | 2014-11-11 | 2014-11-11 | Electrolytic solution is automatically except scum silica frost device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204111890U true CN204111890U (en) | 2015-01-21 |
Family
ID=52329223
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420666265.0U Expired - Fee Related CN204111890U (en) | 2014-11-11 | 2014-11-11 | Electrolytic solution is automatically except scum silica frost device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204111890U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112190978A (en) * | 2020-09-29 | 2021-01-08 | 中冶焦耐(大连)工程技术有限公司 | Device and method for separating acid tar from ammonium sulfate mother liquor |
| CN113617075A (en) * | 2021-08-23 | 2021-11-09 | 铜陵有色金属集团股份有限公司 | Solid-liquid foam three-phase separator for electrolytic copper liquid purification process |
-
2014
- 2014-11-11 CN CN201420666265.0U patent/CN204111890U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112190978A (en) * | 2020-09-29 | 2021-01-08 | 中冶焦耐(大连)工程技术有限公司 | Device and method for separating acid tar from ammonium sulfate mother liquor |
| CN112190978B (en) * | 2020-09-29 | 2024-03-19 | 中冶焦耐(大连)工程技术有限公司 | Device and method for separating acid tar in ammonium sulfate mother liquor |
| CN113617075A (en) * | 2021-08-23 | 2021-11-09 | 铜陵有色金属集团股份有限公司 | Solid-liquid foam three-phase separator for electrolytic copper liquid purification process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204111890U (en) | Electrolytic solution is automatically except scum silica frost device | |
| CN108002570A (en) | A kind of environmental protection food and drink waste water processing oil-water separation tank | |
| JP5085474B2 (en) | Method for electrolytic purification of copper | |
| CN201722171U (en) | Air flotation sewage treatment unit | |
| CN102266859A (en) | Method and device for cleaning cauliflower-shaped polycrystalline silicon raw material with oxides on surface thereof | |
| CN207567008U (en) | A kind of environmental protection food and drink waste water processing oil-water separation tank | |
| CN204918256U (en) | Acid effluent disposal system of mine copper -containing | |
| CN204107891U (en) | A kind of Degreasing Area Stage 1 structure | |
| CN203999514U (en) | Crude oil water-oil interface electric field dehydration slagging-off compensating groove | |
| CN202973059U (en) | Novel periodic blowdown flash tank | |
| CN201756463U (en) | Oil remover | |
| CN203612993U (en) | Oil-water separation device for treating oily sewage | |
| CN101891276A (en) | Oil removing device | |
| CN104818500A (en) | Anode mud cleaning system | |
| CN210030130U (en) | Automatic change liquid level tracking formula oily sewage purification preprocessing device | |
| CN205419893U (en) | Single push rod rotary type water decanter | |
| CN105753086A (en) | Jet air flotation apparatus | |
| CN202880951U (en) | Novel jet air floating device | |
| CN204261391U (en) | A kind of Wastewater from Yellow Phosphorus Production settling tank | |
| CN104532301A (en) | Dry discharging type ore pulp electrolytic lead device | |
| CN219470223U (en) | Floating object filtering collector in electrolytic tank | |
| CN211734487U (en) | Novel horizontal electrolytic tank | |
| CN211813546U (en) | Progressive efficient air floating device | |
| CN203754460U (en) | Power-free deslagging floatation device | |
| CN216426970U (en) | Special electric flocculation equipment for oil and gas field wastewater treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20150121 Termination date: 20201111 |