CN205361292U - Nickel sulfate solution purifying and removing impurity reaction unit - Google Patents
Nickel sulfate solution purifying and removing impurity reaction unit Download PDFInfo
- Publication number
- CN205361292U CN205361292U CN201520927417.2U CN201520927417U CN205361292U CN 205361292 U CN205361292 U CN 205361292U CN 201520927417 U CN201520927417 U CN 201520927417U CN 205361292 U CN205361292 U CN 205361292U
- Authority
- CN
- China
- Prior art keywords
- reation kettle
- reactor
- chemical pump
- drain pipe
- sodium fluoride
- 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.)
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- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 title claims abstract description 14
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 title claims abstract description 14
- 239000012535 impurity Substances 0.000 title claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 11
- 239000000843 powder Substances 0.000 claims abstract description 23
- 239000000126 substance Substances 0.000 claims abstract description 18
- 238000000746 purification Methods 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 3
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 abstract description 40
- 235000013024 sodium fluoride Nutrition 0.000 abstract description 20
- 239000011775 sodium fluoride Substances 0.000 abstract description 20
- 239000000463 material Substances 0.000 abstract description 6
- 239000007787 solid Substances 0.000 abstract description 4
- 229910001425 magnesium ion Inorganic materials 0.000 abstract description 3
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 abstract 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 5
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 5
- 239000011575 calcium Substances 0.000 description 5
- 229910052791 calcium Inorganic materials 0.000 description 5
- 239000011777 magnesium Substances 0.000 description 5
- 229910052749 magnesium Inorganic materials 0.000 description 5
- 230000008021 deposition Effects 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 2
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- -1 hopper Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
The utility model relates to a nickel sulfate solution purifying and removing impurity reaction unit, its structure includes: reation kettle, reation kettle drain pipe and feed liquor pipe, the chemical pump, lower connecting tube between reation kettle drain pipe and the chemical pump, last connecting tube between reation kettle feed liquor pipe and the chemical pump, reation kettle operation platform, its structure of its characterized in that still includes: fix the powder hopper on reation kettle operation platform, upper end and the hookup of powder hopper discharge gate, the lower connecting tube between lower extreme and reation kettle drain pipe and the chemical pump links powder unloading pipe. The utility model discloses a device, powdery material can evenly flow into pipeline and solution intensive mixing together the pump reation kettle goes into, increased ionic kinetic energy for the combination of interionic, the sodium fluoride of make adding in time, fully dissolves and fully reacts with the calcium magnesium ion, the effectual deposit of having solved the sodium fluoride and by the problem of solid residue parcel among the reation kettle has reduced the consumption of sodium fluoride.
Description
Technical field
A kind of nickel sulfate solution purification and impurity removal reaction unit, relates to the improvement of a kind of nickel sulfate solution purification and impurity removal reaction unit structure.
Background technology
In nickel sulfate solution purification and impurity removal technique, removing calcium and magnesium adopts sodium fluoride powder body as the chemical precipitation agent removing calcium and magnesium impurity.Sodium fluoride outward appearance is white powder, has good mobility, is slightly soluble in water, 25kg/ bag independent packaging.By required sodium fluoride by being manually directly added into by the manhole of reactor during removing calcium and magnesium operation, it is impossible to effectively control sodium fluoride is slow, be uniformly added into reactor.Adition process exists sodium fluoride and adds too fast, cause the sodium fluoride of addition to be wrapped up by solid slag in reactor, it is impossible in time, fully dissolve and fully react with calcium ions and magnesium ions, cause the deposition of sodium fluoride and addition to increase, add material consumption.
Utility model content
The purpose of this utility model be aiming at above-mentioned prior art exist deficiency, it is provided that a kind of can effectively solve in nickel sulfate solution removing calcium and magnesium process control sodium fluoride powder body can not slowly, be uniformly added into the deposition with sodium fluoride and by reactor solid slag wrap up problem nickel sulfate solution purification and impurity removal reaction unit.
In order to solve the problems referred to above, this utility model adopts the following technical scheme that.
A kind of nickel sulfate solution purification and impurity removal reaction unit, its structure includes: reactor；Reactor drain pipe；Reactor drain pipe feed tube；Chemical pump；Second line of a couplet adapter between reactor drain pipe and chemical pump；The valve being provided with on the second line of a couplet is taken over；Upper connecting tube between reactor feed tube and chemical pump；The valve being provided with in upper connecting tube；Reactor operating platform；It is characterized in that its structure also includes:
Powder body hopper, this powder body hopper is fixed on reactor operating platform；
Powder body tremie pipe, this tremie pipe upper end couples with powder body hopper discharging opening, and the second line of a couplet adapter between lower end with reactor drain pipe and chemical pump couples；Powder body tremie pipe is provided with control valve.
A kind of nickel sulfate solution purification and impurity removal reaction unit of the present utility model, hangs on the operational platform and installs powder body hopper additional, and the upper port of hopper is along being easy to manually sodium fluoride be added material bin in same level with operating platform；By hopper lower part outlet valve switch, the discharge quantity adjusting sodium fluoride, effectively control sodium fluoride slowly, be uniformly added into；In pump high-speed circulating conveying reactor, solution forms micro-vacuum, granular material is under the effect of micro-vacuum state and gravity, uniform flow ipe and solution are sufficiently mixed and together pump into reactor, add the kinetic energy of ion, accelerate interionic combination, the sodium fluoride making addition in time, fully dissolves and fully reacts with calcium ions and magnesium ions, effectively solves the deposition of sodium fluoride and by the problem of solid slag parcel in reactor, reduces the consumption of sodium fluoride.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
A kind of nickel sulfate solution purification and impurity removal reaction unit, its structure includes: reactor 1；Reactor drain pipe 2；Reactor drain pipe feed tube 3；Chemical pump 4；Second line of a couplet adapter 5 between reactor drain pipe and chemical pump；The valve 6 being provided with on the second line of a couplet is taken over；Upper connecting tube 7 between reactor feed tube and chemical pump；The valve 8 being provided with in upper connecting tube；Reactor operating platform 9；Its structure also includes: powder body hopper 10, and this powder body hopper is fixed on reactor operating platform；Powder body tremie pipe 11, this tremie pipe upper end couples with powder body hopper discharging opening, and the second line of a couplet adapter between lower end with reactor drain pipe and chemical pump couples；Powder body tremie pipe is provided with control valve 12.
A kind of nickel sulfate solution purification and impurity removal reaction unit of the present utility model, hopper, valve, chemical pump and corresponding pipeline, pipe fitting composition, hopper, ball valve, chemical pump and pipeline all can adopt anticorrosion material.During the operation of nickel sulfate solution removing calcium and magnesium, after the required artificial broken bag of packed sodium fluoride, add material bin；Open reactor outlet valve, start solution transfer pump, open delivery pump outlet valve, then turn on hopper outlet valve and by adjusting Valve controlling blanking velocity, make sodium fluoride flow ipe slow, uniform and solution be sufficiently mixed and together pump into reactor, until the powder material of required addition reactor has been carried.
Claims (1)
1. a nickel sulfate solution purification and impurity removal reaction unit, its structure includes: reactor；Reactor drain pipe；Reactor drain pipe feed tube；Chemical pump；Second line of a couplet adapter between reactor drain pipe and chemical pump；The valve being provided with on the second line of a couplet is taken over；Upper connecting tube between reactor feed tube and chemical pump；The valve being provided with in upper connecting tube；Reactor operating platform；It is characterized in that its structure also includes:
Powder body hopper, this powder body hopper is fixed on reactor operating platform；
Powder body tremie pipe, this tremie pipe upper end couples with powder body hopper discharging opening, and the second line of a couplet adapter between lower end with reactor drain pipe and chemical pump couples；Powder body tremie pipe is provided with control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520927417.2U CN205361292U (en) | 2015-11-20 | 2015-11-20 | Nickel sulfate solution purifying and removing impurity reaction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520927417.2U CN205361292U (en) | 2015-11-20 | 2015-11-20 | Nickel sulfate solution purifying and removing impurity reaction unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205361292U true CN205361292U (en) | 2016-07-06 |
Family
ID=56260677
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520927417.2U Active CN205361292U (en) | 2015-11-20 | 2015-11-20 | Nickel sulfate solution purifying and removing impurity reaction unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205361292U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111646524A (en) * | 2020-05-12 | 2020-09-11 | 荆门市格林美新材料有限公司 | Quality improving system for nickel sulfate solutions with different technological sources |
-
2015
- 2015-11-20 CN CN201520927417.2U patent/CN205361292U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111646524A (en) * | 2020-05-12 | 2020-09-11 | 荆门市格林美新材料有限公司 | Quality improving system for nickel sulfate solutions with different technological sources |
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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: 20240325 Address after: 737100 No.1 Lanzhou Road, Jinchuan District, Jinchang City, Gansu Province Patentee after: Jinchuan Group Nickel Salt Co.,Ltd. Country or region after: China Address before: 737103 No. 98, Jinchuan Road, Jinchang, Gansu Patentee before: JINCHUAN GROUP Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right |