CN204251668U - High effective sealing formula wet method vanadium extraction ion-exchanger - Google Patents
High effective sealing formula wet method vanadium extraction ion-exchanger Download PDFInfo
- Publication number
- CN204251668U CN204251668U CN201420727909.2U CN201420727909U CN204251668U CN 204251668 U CN204251668 U CN 204251668U CN 201420727909 U CN201420727909 U CN 201420727909U CN 204251668 U CN204251668 U CN 204251668U
- Authority
- CN
- China
- Prior art keywords
- filter
- ion
- filter plate
- housing
- ring
- 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
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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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- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a kind of high effective sealing formula wet method vanadium extraction ion-exchanger, described ion-exchanger comprises lower cover (3), filter plate (4), ion exchange resin (5) and housing (6), the below order of housing (6) installs filter plate (4) and lower cover (3), the inner chamber of the housing (6) of filter plate (4) top installs ion exchange resin (5), and (4) install filter with filter plate; The top order of housing (6) installs filter plate (4) and upper cover (7).Filter plate (4) is upper installs ring type filter: center filter (9), first ring filter (10) and the second ring filter (11); The drainage amount of single filter (4) is 0.25 ~ 1 ton/hour.The utility model is simple and reasonable, and water distribution is even, exchange is comprehensive, has stopped the problem of leaked liquid.Be conducive to environment protection, improve the work-ing life of ion exchange resin, saved equipment self-weight and cost of manufacture, improve vanadium extraction efficiency, vanadium good product quality.
Description
Technical field
The utility model relates to a kind of high effective sealing formula wet method vanadium extraction ion-exchanger.
Background technology
Ion-exchange is ion in liquid phase and carries out a kind of reversible chemical permutoid reaction between specific solid phase intermediate ion, that is: when some ion in liquid phase is liked by certain solid intermediate ion, ion in liquid phase can adsorb by solid, for maintaining the electrobalance of liquid, solid must discharge other ions of equal value and return in liquid during above-mentioned ion when adsorbing, thus form ion-exchange.The solid with absorption vanadium ability claims " ion exchange resin ", and people is called for short " resin " in the industry.Present stage is for the ion-exchanger of process for extracting vanadium, form primarily of lower cover, housing, filter plate and ion exchange resin, filter plate and end socket are installed in the below of housing, and ion exchange resin is arranged in the housing on filter plate, and namely the upper end of ion-exchanger is open type structure.In addition, no matter its diameter of the filter plate in the ion-exchanger of above-mentioned open type structure, be all close and numerously be covered with filter, filter usage quantity is very large.Its weak point: easily leak above the ion-exchanger of open type structure liquid, to environment and vanadium loss, filter plate is installed more filter, one is thickness and the deadweight that will increase filter plate, two is waste a large amount of filters, because the top of ion exchange resin does not arrange filter, be easily directed at the molten punching direct current of exchange, obtain by cylinder limit resin and do not exchange reduction adsorptive power.Three is that column diameter and matched are unreasonable, and height of column only has straight 3 ~ 3 times, penetrates and reduce exchange capacity too early when leading exchange.Impurity in liquid easily causes the adsorptive power of ion exchange resin reduce very soon or completely lose adsorptive power.
Utility model content
The purpose of this utility model is to overcome deficiency of the prior art, provides a kind of and effectively can solve the low and easy outer high effective sealing formula wet method vanadium extraction ion-exchanger emitting solution problem of exchange efficiency.
The purpose of this utility model is achieved by following technical proposals:
Described ion-exchanger comprises lower cover, filter plate, ion exchange resin and housing, and the below order of housing installs filter plate and lower cover, and the inner chamber of the housing above filter plate installs ion exchange resin, and filter installed by filter plate; The top order of described housing installs filter plate and upper cover.
The inner chamber described filter plate being positioned at housing installs ring type filter: center filter, first ring filter and the second ring filter; The drainage amount of single filter is 0.25 ~ 1 ton/hour.
Described center filter is one, and first ring filter is 10-22, and the second ring filter is 4-12; Described first ring and the second Ring current distribution line position are according to decile on ion exchange resin effective cross section.
The height of described ion exchange resin is 5 ~ 8 times of its diameter.
Filtering material is filled in described upper cover.
Compared with prior art, the utility model has the following advantages: simple and reasonable, has stopped the problem of leaked liquid; be conducive to environment protection, improve the work-ing life of ion exchange resin simultaneously, save equipment self-weight and cost of manufacture; improve vanadium extraction efficiency, vanadium good product quality.
Accompanying drawing explanation
Fig. 1 is the structural representation of the ion-exchanger of prior art;
Fig. 2 is the utility model one example structure schematic diagram;
Fig. 3 is the structural representation of the utility model Novel filter plate;
In figure: 1-water outlet, 2-supports, 3-lower cover, 4-filter plate, 5-ion exchange resin, 6-housing, 7-upper cover, 8-prosopyle, 9-center filter, 10-first ring filter, 11-second ring filter, 12-ring flange.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail:
Described ion-exchanger comprises lower cover 3, filter plate 4, ion exchange resin 5 and housing 6, and the below order of housing 6 installs filter plate 4 and lower cover 3, and the inner chamber of the housing 6 above filter plate 4 installs ion exchange resin 5, and filter installed by filter plate 4; The top order of described housing 6 installs filter plate 4 and upper cover 7.
The inner chamber described filter plate 4 being positioned at housing 6 installs ring type filter: center filter 9, first ring filter 10 and the second ring filter 11; The drainage amount of single filter 4 is 0.25 ~ 1 ton/hour.Ring type filter adopts prior art to design and produce, or adopts the product of prior art.
Described center filter 9 is one, and first ring filter 10 is 10-22, and the second ring filter 11 is 4-12; Described first ring and the second Ring current distribution line position are according to decile on ion exchange resin 5 effective cross section.
The height of described ion exchange resin 5 is 5 ~ 8 times of its diameter.
Filtering material is filled in described upper cover 7.
Embodiment 1:
Ion-exchanger of the present utility model is sequentially installed under upper: upper cover 7, filter plate 4, the housing 6 being provided with ion exchange resin 5, filter plate 4 and lower cover 3.Upper cover 7 is arranged prosopyle 8, lower cover 3 set out the mouth of a river 1 and support 2.Upper cover 7, filter plate 4, ring flange 12 between housing 6 and lower cover 3, is adopted to connect.
Embodiment 2:
Substantially the same manner as Example 1, unlike: inner chamber filter plate 4 being positioned at housing 6 installs ring type filter: center filter 9, first ring filter 10 and the second ring filter 11; The drainage amount of single filter 4 is 0.25 ~ 1 ton/hour.
Embodiment 3:
Substantially the same manner as Example 2, unlike: center filter 9 is one, and first ring filter 10 is 10-22, and the second ring filter 11 is 4-12; Described first ring and the second Ring current distribution line position are according to decile on ion exchange resin 5 effective cross section.
Embodiment 4,5,6:
Respectively on the basis of embodiment 1,2,3, the height of ion exchange resin 5 is 6 times of its diameter.The size that rescales can improve the working efficiency of ion exchange resin 5 to greatest extent.
Embodiment 7-12:
Respectively on the basis of embodiment 1-6, in upper cover 7, fill filtering material.
Feature of the present utility model:
1, the top order of housing 6 installs filter plate 4 and upper cover 7.The open type structure of prior art is become sealed construction, solves leaked liquid problem.On the other hand, above ion exchange resin 5, increase filter plate 4, be conducive to protection ion exchange resin 5 and be not easily polluted by the external foreign matters, in other words, the working life of ion exchange resin 5 can be improved.
2, employing center and two is periphery and puts filter, saves filter, reduces filter plate deadweight.
3, interchanger height of column is increased to 5 ~ 8 times, resin filling high growth by 2 ~ 3 times of original diameter, and the exchanged process of solution increases thereupon, and exchange capacity efficiency significantly improves.
4, filtering material is filled in end socket 7.The protection to ion exchange resin 5 can be increased, the working life of ion exchange resin 5 can be improved further.
Claims (6)
1. a high effective sealing formula wet method vanadium extraction ion-exchanger, described ion-exchanger comprises lower cover (3), filter plate (4), ion exchange resin (5) and housing (6), the below order of housing (6) installs filter plate (4) and lower cover (3), the inner chamber of the housing (6) of filter plate (4) top installs ion exchange resin (5), and (4) install filter with filter plate; It is characterized in that: the top order of described housing (6) installs filter plate (4) and upper cover (7).
2. ion-exchanger according to claim 1, is characterized in that: the inner chamber described filter plate (4) being positioned at housing (6) installs ring type filter: center filter (9), first ring filter (10) and the second ring filter (11); The drainage amount of single filter (4) is 0.25 ~ 1 ton/hour.
3. ion-exchanger according to claim 2, is characterized in that: described center filter (9) is one, and first ring filter (10) is 10-22, and the second ring filter (11) is 4-12; Described first ring and the second Ring current distribution line position are according to decile on ion exchange resin (5) effective cross section.
4. the ion-exchanger according to claim 1 or 2 or 3, is characterized in that: the height of described ion exchange resin (5) is 5 ~ 8 times of its diameter.
5. the ion-exchanger according to claim 1 or 2 or 3, is characterized in that: fill filtering material in upper cover (7).
6. ion-exchanger according to claim 4, is characterized in that: fill filtering material in upper cover (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420727909.2U CN204251668U (en) | 2014-11-28 | 2014-11-28 | High effective sealing formula wet method vanadium extraction ion-exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420727909.2U CN204251668U (en) | 2014-11-28 | 2014-11-28 | High effective sealing formula wet method vanadium extraction ion-exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204251668U true CN204251668U (en) | 2015-04-08 |
Family
ID=52955993
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420727909.2U Expired - Fee Related CN204251668U (en) | 2014-11-28 | 2014-11-28 | High effective sealing formula wet method vanadium extraction ion-exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204251668U (en) |
-
2014
- 2014-11-28 CN CN201420727909.2U patent/CN204251668U/en not_active Expired - Fee Related
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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: 20150408 Termination date: 20171128 |