CN203715697U - Reaction chute of nickel electrolyte purification system - Google Patents
Reaction chute of nickel electrolyte purification system Download PDFInfo
- Publication number
- CN203715697U CN203715697U CN201420089352.4U CN201420089352U CN203715697U CN 203715697 U CN203715697 U CN 203715697U CN 201420089352 U CN201420089352 U CN 201420089352U CN 203715697 U CN203715697 U CN 203715697U
- Authority
- CN
- China
- Prior art keywords
- chute
- purification system
- nickel electrolyte
- instrument
- reaction
- 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
Classifications
-
- 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
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
The utility model provides a reaction chute of a nickel electrolyte purification system. The reaction chute comprises a chute main pipe and a supporting column, wherein the chute main pipe is connected with a plurality of pairs of liquid inlet branch pipes and liquid outlet branch pipes; an instrument opening is formed in each liquid inlet branch pipe, and is connected with a flange plate; a detecting instrument is fixed at the center hole part of the flange plate, and the gap between the detecting instrument and the flange plate forms seal by virtue of a sealing material. The reaction chute disclosed by the utility model has better sealing performance than a conventional square chute by adopting the tubular structure; the flange plate is arranged on the instrument opening, so that the gap between the detecting instrument and the instrument opening is reduced, the sealing performance of the reaction chute of the nickel electrolyte purification system is further improved, the phenomenon of running, popping, dripping and leaking of solutions is eliminated, the phenomenon of environment pollution caused by acid mist and chlorine is solved, the chlorine utilization rate is improved, and the production cost is reduced.
Description
Technical field
The utility model belongs to technical field of non-ferrous metallurgy, relates to a kind of nickel electrolyte purification system response chute.
Background technology
Reaction chute is the visual plant that nickel electrolyte purification operation (mainly refer to deironing, remove cobalt operation) is used, its Main Function is to make nickel electrolyte to flow to outflow at deironing reactive tank with except in cobalt reactive tank, is transport and connecting pipe in nickel electrolyte purification process.In nickel electrolyte purification operation, need in system, pass into chlorine and air, make Fe
2+, Co
2+oxidation, forms Fe (OH)
3and Co (OH)
3precipitation, reaches the object of deironing except cobalt with this.And existing nickel electrolyte purification system chute is square structure, adopt glass reinforced plastic to make, upper cap fibreglass reinforced plastic cover, poor sealing, the measuring instruments such as thermometer, pH meter are directly put into chute by instrument mouth, cannot realize the sealing completely of chute.Due to deironing, except cobalt temperature of reaction high, it is acid that solution is, deironing region high-temperature acidic gas and easily flow out contaminate environment except cobalt region chlorine-containing gas, and it is lower to cause removing cobalt operation chlorine utilization, remove cobalt chlorine consumption large, cause chlorine residue absorption liquid quantity of alkali consumption to increase, the corresponding production cost that increased.
Utility model content
The purpose of this utility model is the problem existing for prior art, and a kind of nickel electrolyte purification system response chute with good seal performance is provided.
For this reason, the utility model adopts following technical scheme:
A kind of nickel electrolyte purification system response chute, comprise chute supervisor and pillar, on described chute supervisor, be connected with some to feed liquor arm and fluid arm, described feed liquor arm is provided with instrument mouth, on described instrument mouth, be connected with ring flange, described ring flange central hole is fixed with measuring instrument, and the gap between described measuring instrument and ring flange forms sealing by sealing material.Described pillar mainly works to support chute supervisor.
Further, described chute supervisor top is provided with porthole, and described porthole is provided with sealing cover.
Further, described measuring instrument comprises thermometer, pH meter and potentiometer.
Further, on described feed liquor arm and fluid arm, be all connected with valve.The setting of valve is convenient to react chute and is occurred stopping groove maintenance after seepage, is also convenient to solution compolision and makes circular treatment after defective, ensure every step reaction after solution compolision qualified.
The beneficial effects of the utility model are: the utility model reaction chute adopts tubular structure, have saved the upper cover that square groove uses, and better tightness; Reduce the gap between measuring instrument and instrument mouth by ring flange being set at instrument mouth place, and eliminate as far as possible above-mentioned gap by sealing material, thereby further improve the stopping property of nickel electrolyte purification system response chute, stop solution evaporating, emitting, dripping or leaking of liquid or gas phenomenon in chute, solve the phenomenon of acid mist and chlorine pollution environment, and improved chlorine utilization, reduce production cost.
Brief description of the drawings
Fig. 1 is structural front view of the present utility model;
Fig. 2 is structure vertical view of the present utility model.
In figure, 1-chute supervisor, 2-pillar, 3-feed liquor arm, 4-fluid arm, 5-valve, 6-instrument mouth, 7-ring flange, 8-measuring instrument, 9-porthole, 10-sealing cover.
Embodiment
As illustrated in fig. 1 and 2, a kind of nickel electrolyte purification system response chute, comprise chute supervisor 1 and pillar 2, on chute supervisor 1, be connected with some to feed liquor arm 3 and fluid arm 4, and on feed liquor arm 3 and fluid arm 4, be all connected with valve 5, on feed liquor arm 3, be also provided with instrument mouth 6, on instrument mouth 6, be connected with ring flange 7, ring flange 7 central hole are fixed with measuring instrument 8, and gap between measuring instrument 8 and ring flange 7 forms sealing by sealing material; Chute is responsible for 1 top and is provided with porthole 9, and porthole 9 is provided with sealing cover 10.Measuring instrument 8 comprises thermometer, pH meter and potentiometer.
When the utility model work, chute supervisor 1 two ends are connected respectively to question response solution line and scavenging solution storage tank, feed liquor arm 3 and fluid arm 4 are connect respectively to deironing reactive tank or fluid inlet and liquid outlet except cobalt reactive tank, make nickel electrolyte successively at deironing reactive tank with except carrying out deironing in cobalt reactive tank and removing cobalt reaction; By measuring instrument 8, the technical qualification of cleansing soln are carried out to Real-Time Monitoring.Under normal circumstances, porthole 9 is in by sealing cover 10 sealed states, need to be to solution sampling or personal monitoring's pH, temperature value time, opens sealing cover 10, after end-of-job, sealing cover 10 built, sealed.Feed liquor arm 3 and the valve 5 being connected on fluid arm 4 are convenient to react chute and are occurred stopping groove maintenance after seepage, are also convenient to solution composition and do circular treatment when defective.
Utilize after the utility model, improve the reaction efficiency of nickel electrolyte purification system, deironing, reach more than 99% except solution compolision qualification rate after cobalt, except cobalt chlorine utilization improves 8-10%, chlorine consumption reduces 20kg/t.Ni, and approximately 450,000 yuan of annual direct economic benefits have been stopped solution evaporating, emitting, dripping or leaking of liquid or gas phenomenon in chute simultaneously, the phenomenon that has solved acid mist and chlorine pollution environment, social benefit is remarkable.
Claims (4)
1. a nickel electrolyte purification system response chute, it is characterized in that, comprise chute supervisor and pillar, on described chute supervisor, be connected with some to feed liquor arm and fluid arm, described feed liquor arm is provided with instrument mouth, on described instrument mouth, be connected with ring flange, described ring flange central hole is fixed with measuring instrument, and the gap between described measuring instrument and ring flange forms sealing by sealing material.
2. a kind of nickel electrolyte purification system response chute according to claim 1, is characterized in that, described chute supervisor top is provided with porthole, and described porthole is provided with sealing cover.
3. a kind of nickel electrolyte purification system response chute according to claim 1, is characterized in that, described measuring instrument comprises thermometer, pH meter and potentiometer.
4. a kind of nickel electrolyte purification system response chute according to claim 1, is characterized in that, on described feed liquor arm and fluid arm, is all connected with valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420089352.4U CN203715697U (en) | 2014-02-28 | 2014-02-28 | Reaction chute of nickel electrolyte purification system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420089352.4U CN203715697U (en) | 2014-02-28 | 2014-02-28 | Reaction chute of nickel electrolyte purification system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203715697U true CN203715697U (en) | 2014-07-16 |
Family
ID=51154866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420089352.4U Expired - Fee Related CN203715697U (en) | 2014-02-28 | 2014-02-28 | Reaction chute of nickel electrolyte purification system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203715697U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113957490A (en) * | 2021-11-05 | 2022-01-21 | 金川集团股份有限公司 | Electrolytic nickel purification and impurity removal reaction tank and method thereof |
-
2014
- 2014-02-28 CN CN201420089352.4U patent/CN203715697U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113957490A (en) * | 2021-11-05 | 2022-01-21 | 金川集团股份有限公司 | Electrolytic nickel purification and impurity removal reaction tank and method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206955727U (en) | A kind of preparation facilities of hydrogen rich water | |
| CN206384830U (en) | A kind of hydrogen production units by carbinol | |
| CN207899247U (en) | A kind of integrated device based on triazine solution desulfurization | |
| CN203641589U (en) | Combined-type energy-saving water-sealed valve | |
| CN203715697U (en) | Reaction chute of nickel electrolyte purification system | |
| CN202785681U (en) | Device for continuously producing ultra-clean and high-purity ammonia water | |
| CN206688457U (en) | A kind of chemical emission processing unit | |
| CN209451578U (en) | A kind of production food-grade carbon-dioxide gas absorption tower | |
| CN202803069U (en) | Device capable of reducing content of acid and iron oxide powder in acid regeneration tail gas | |
| CN209143703U (en) | A kind of activated carbon of phosphoric acid method workshop high efficiente callback phosphoric acid plant | |
| CN202880863U (en) | Synthesizer for producing hydrochloric acid from chlor-alkali | |
| CN205774374U (en) | A kind of single column formula washing Methane decarbonization tower | |
| CN204778859U (en) | System for including retrieving ammonia in ammonia mother liquor | |
| CN205973789U (en) | Hydrogen peroxide solution production oxidation process gas -liquid separation | |
| CN205031904U (en) | Acetic acid recovery tower | |
| CN203572683U (en) | Circulation type pH meter sampling device | |
| CN202786059U (en) | Device for purifying ultra-pure absolute ethyl alcohol | |
| CN205061569U (en) | Full -automatic carbon -dioxide generator | |
| CN202390543U (en) | Gas generator | |
| CN203954995U (en) | Sintering flue gas desulfurization system and desulfurizing agent adding set thereof | |
| CN208238870U (en) | A kind of high energy-saving environment protection type water flow indicator | |
| CN216630261U (en) | Ammonia exhaust gas absorption device | |
| CN202666866U (en) | Water seal structure for discharge port of reaction kettle | |
| CN215585945U (en) | Ammonia gas leakage emergency system in nitrogen preparation | |
| CN203462063U (en) | Online acid liquor treatment device for main blast-furnace gas pipeline |
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 |
Granted publication date: 20140716 Termination date: 20200228 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |