CN203715281U - Capacitor grade phosphoric acid yellow phosphorus purifying device - Google Patents
Capacitor grade phosphoric acid yellow phosphorus purifying device Download PDFInfo
- Publication number
- CN203715281U CN203715281U CN201420072092.XU CN201420072092U CN203715281U CN 203715281 U CN203715281 U CN 203715281U CN 201420072092 U CN201420072092 U CN 201420072092U CN 203715281 U CN203715281 U CN 203715281U
- Authority
- CN
- China
- Prior art keywords
- yellow phosphorus
- phosphoric acid
- tank
- phosphorus
- grade phosphoric
- 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 - Lifetime
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- OBSZRRSYVTXPNB-UHFFFAOYSA-N tetraphosphorus Chemical compound P12P3P1P32 OBSZRRSYVTXPNB-UHFFFAOYSA-N 0.000 title claims abstract description 82
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 229910000147 aluminium phosphate Inorganic materials 0.000 title claims abstract description 36
- 239000003990 capacitor Substances 0.000 title claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000005406 washing Methods 0.000 claims abstract description 29
- 238000005554 pickling Methods 0.000 claims abstract description 22
- 238000003860 storage Methods 0.000 claims abstract description 14
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 12
- 239000011574 phosphorus Substances 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 8
- 238000004140 cleaning Methods 0.000 claims description 26
- 235000021110 pickles Nutrition 0.000 claims description 17
- 238000000746 purification Methods 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 239000002994 raw material Substances 0.000 abstract description 8
- 238000002844 melting Methods 0.000 abstract description 3
- 230000008018 melting Effects 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Abstract
The utility model relates to the field of phosphoric acid production equipment and in particular relates to a capacitor grade phosphoric acid yellow phosphorus purifying device used for purifying yellow phosphorus raw material for producing capacitor grade phosphoric acid. The utility model aims at solving the technical problem of providing a capacitor grade phosphoric acid yellow phosphorus purifying device used for purifying an industrial yellow phosphorus raw material. The capacitor grade phosphoric acid yellow phosphorus purifying device comprises a rinsing tank provided with a stirring device inside, a yellow phosphorus storage tank, a pickling tank, a phosphorus melting tank and a washing purifying pot with an ionized water inlet, wherein the yellow phosphorus storage tank is communicated with the rinsing tank by virtue of a yellow phosphorus submerged pump arranged at the bottom in the yellow phosphorus storage tank, the pickling tank is communicated with the rinsing tank by virtue of a pickling submerged pump arranged at the bottom in the pickling tank, the rinsing tank is communicated with the washing purifying pot, and the washing purifying pot is communicated with the phosphorus melting tank by virtue of a yellow phosphorus output pipe. The capacitor grade phosphoric acid yellow phosphorus purifying device has the advantages that yellow phosphorus is washed with the ionized water, and the yellow phosphorus raw material used for producing capacitor grade phosphoric acid is obtained; The capacitor grade phosphoric acid yellow phosphorus purifying device is applicable to purifying of the yellow phosphorus used for producing the capacitor grade phosphoric acid.
Description
Technical field
The utility model relates to phosphoric acid production apparatus field, especially a kind of capacitor stage phosphoric acid yellow phosphorus purification device that the raw materials for production yellow phosphorus of capacitor stage phosphoric acid is purified.
Background technology
Existing phosphoric acid, especially in the production process of capacitor stage phosphoric acid, the primary industry yellow phosphorus adopting is all directly by pipeline, to be delivered in phosphoric acid production equipment combustion phosphorus hydration tower, by spray burning after described yellow phosphorus and air mixed, obtain Vanadium Pentoxide in FLAKES particle, and finally obtain phosphoric acid solution.But such technique is because yellow phosphorus raw material is without any purifying treatment, in industrial yellow phosphorus, containing the impurity such as heavy metal, impurity, organism also can be along with entering into final phosphoric acid product.Therefore such mode of production can affect the purity of final phosphoric acid product.Especially for capacitor stage phosphoric acid product, such production technique is difficult to the qualified product of producing of efficient stable.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of capacitor stage phosphoric acid yellow phosphorus purification device that industrial yellow phosphorus raw material is purified.
The utility model solves the technical scheme that its technical problem adopts: capacitor stage phosphoric acid yellow phosphorus purification device, comprise that inside is provided with the rinse tank of whipping appts, yellow phosphorus storage tank, pickling tank, melts phosphorus groove and is provided with the water washing cleaning pot of ionized water entrance, described yellow phosphorus storage tank communicates with rinse tank by being arranged at the yellow phosphorus submerged pump of yellow phosphorus storage tank inner bottom part, described pickling tank communicates with rinse tank by being arranged at the pickling submerged pump of pickling tank inner bottom part, rinse tank communicates with water washing cleaning pot, described water washing cleaning pot by yellow phosphorus output tube with melt phosphorus groove and communicate.
Further, the whipping appts in described rinse tank is the stirring rake that is arranged at rinse tank bottom.
Further, described yellow phosphorus output tube is arranged at the stage casing of water washing cleaning pot.
Further, the bottom of water washing cleaning pot is provided with pickle solution relief outlet.
Further, in rinse tank, be provided with temperature-detecting device.
Further, described ionized water entrance is arranged at the top of water washing cleaning pot.
The beneficial effects of the utility model are: first the utility model is transported to liquid industrial yellow phosphorus in rinse tank, to stir rinsing by yellow phosphorus submerged pump, when temperature reaches 70 to 80 degrees Celsius, start pickling submerged pump, the pickle solution in pickling tank is pumped in rinse tank and carries out mix and blend with yellow phosphorus raw material.After stirring, the liquid in rinse tank is passed in water washing cleaning pot and is heated, and the ion film water that simultaneously passes into 70 to 80 degrees Celsius of temperature by ionized water entrance rinses, until remove completely in yellow phosphorus after residual acid solution, can obtain the pure yellow phosphorus raw material for the production of capacitor stage phosphoric acid.The utility model practicality that is skillfully constructed, is specially adapted to purify the yellow phosphorus for the production of capacitor stage phosphoric acid, thereby guarantees the quality of the capacitor stage phosphoric acid product that finally obtains.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, be labeled as: yellow phosphorus storage tank 1, yellow phosphorus submerged pump 11, rinse tank 2, whipping appts 21, water washing cleaning pot 3, yellow phosphorus 31, yellow phosphorus output tube 311, ionized water 32, pickle solution 33, pickle solution relief outlet 331, ionized water entrance 34, pickling tank 4, pickling submerged pump 41, melt phosphorus groove 5.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further illustrated.
Capacitor stage phosphoric acid yellow phosphorus purification device as shown in Figure 1, comprise that inside is provided with the rinse tank 2 of whipping appts 21, yellow phosphorus storage tank 1, pickling tank 4, melts phosphorus groove 5 and is provided with the water washing cleaning pot 3 of ionized water entrance 34, described yellow phosphorus storage tank 1 communicates with rinse tank 2 by being arranged at the yellow phosphorus submerged pump 11 of yellow phosphorus storage tank 1 inner bottom part, described pickling tank 4 communicates with rinse tank 2 by being arranged at the pickling submerged pump 41 of pickling tank 4 inner bottom parts, rinse tank 2 communicates with water washing cleaning pot 3, described water washing cleaning pot 3 by yellow phosphorus output tube 311 with melt phosphorus groove 5 and communicate.
When reality is used the utility model, the industrial yellow phosphorus first needs being cleaned is poured in yellow phosphorus storage tank 1, and first described liquid industrial yellow phosphorus is transported in rinse tank 2 through yellow phosphorus submerged pump 11, and heats up through the stirring of whipping appts 21.General, when temperature reaches to 70 to 80 degrees Celsius, the pickling submerged pump 41 that starts pickling tank 4 is input to pickle solution in rinse tank 2, mixes, and removed and be take the impurity that sulfide is representative by pickle solution with yellow phosphorus.Next, the yellow phosphorus that contains pickle solution is passed in water washing cleaning pot 3, and yellow phosphorus solution is heated.Meanwhile, by ionized water entrance 34, pass into ionized water the yellow phosphorus that contains pickle solution is carried out to rinsing.Finally, at the interior material that can form three aspects of water washing cleaning pot 3: be positioned at undermost pickle solution 33, be positioned at middle layer yellow phosphorus 31, be positioned at the ionized water 32 of the superiors.Now, only need yellow phosphorus 31 is input to and melt phosphorus groove 5 by yellow phosphorus output tube 311, the yellow phosphorus starting material after finally can being purified in melting phosphorus groove 5 be for the production of capacitor stage phosphoric acid.
In order to simplify the structure of whipping appts 21, the whipping appts 21 in described rinse tank 2 can be chosen as to the stirring rake that is arranged at rinse tank 2 bottoms.As shown in Figure 1, the stirring rake after simplification can guarantee mixing of industrial yellow phosphorus and ionized water, and is convenient to the dismounting maintenance in later stage.
Because the yellow phosphorus 31 obtaining in water washing cleaning pot 3 is generally the stage casing that is positioned at water washing cleaning pot 3, described yellow phosphorus output tube 311 can be arranged to the stage casing of water washing cleaning pot 3, can easylier more fully yellow phosphorus 31 be discharged again like this.
In order timely the pickle solution of water washing cleaning pot 3 bottoms to be discharged, pickle solution relief outlet 331 can be set in the bottom of water washing cleaning pot 3.As shown in Figure 1, yellow phosphorus after ionized water rinses, its pickle solution containing becomes branch to be deposited in water washing cleaning pot 3 bottoms, sets up after pickle solution relief outlet 331, can timely described pickle solution be discharged, finally for repetitious ionized water rinses, provide technical guarantee.
Due to the requirement having when starting input pickle solution aspect temperature, so can be at the interior set temperature proofing unit of rinse tank 2.The temperature-detecting device of setting up can go out the interior Temperature Feedback of rinse tank 2 comparatively accurately, can realize like this automatization control that pickle solution adds, and improves level of automation of the present utility model.
In order to make ionized water better to the developing result of yellow phosphorus, described ionized water entrance 34 can be arranged to the top of water washing cleaning pot 3.Such improvement can allow ionized water rinse more fully yellow phosphorus 31, also allows the purity of the yellow phosphorus product that finally obtains higher.
The resulting pure yellow phosphorus product of the utility model is the starting material of production capacitor stage phosphoric acid.Through processing of the present utility model, purification, yellow phosphorus can directly be passed among next step operation, and the quality of the capacitor stage phosphoric acid product finally obtaining also can be greatly increased.
Claims (6)
1. capacitor stage phosphoric acid yellow phosphorus purification device, it is characterized in that: comprise that inside is provided with the rinse tank of whipping appts (21) (2), yellow phosphorus storage tank (1), pickling tank (4), melt phosphorus groove (5) and be provided with the water washing cleaning pot (3) of ionized water entrance (34), described yellow phosphorus storage tank (1) communicates with rinse tank (2) by being arranged at the yellow phosphorus submerged pump (11) of yellow phosphorus storage tank (1) inner bottom part, described pickling tank (4) communicates with rinse tank (2) by being arranged at the pickling submerged pump (41) of pickling tank (4) inner bottom part, rinse tank (2) communicates with water washing cleaning pot (3), described water washing cleaning pot (3) by yellow phosphorus output tube (311) with melt phosphorus groove (5) and communicate.
2. capacitor stage phosphoric acid yellow phosphorus purification device as claimed in claim 1, is characterized in that: the whipping appts (21) in described rinse tank (2) is for being arranged at the stirring rake bottom rinse tank (2).
3. capacitor stage phosphoric acid yellow phosphorus purification device as claimed in claim 1 or 2, is characterized in that: described yellow phosphorus output tube (311) is arranged at the stage casing of water washing cleaning pot (3).
4. capacitor stage phosphoric acid yellow phosphorus purification device as claimed in claim 3, is characterized in that: the bottom of water washing cleaning pot (3) is provided with pickle solution relief outlet (331).
5. capacitor stage phosphoric acid yellow phosphorus purification device as claimed in claim 1 or 2, is characterized in that: rinse tank is provided with temperature-detecting device in (2).
6. capacitor stage phosphoric acid yellow phosphorus purification device as claimed in claim 1 or 2, is characterized in that: described ionized water entrance (34) is arranged at the top of water washing cleaning pot (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420072092.XU CN203715281U (en) | 2014-02-19 | 2014-02-19 | Capacitor grade phosphoric acid yellow phosphorus purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420072092.XU CN203715281U (en) | 2014-02-19 | 2014-02-19 | Capacitor grade phosphoric acid yellow phosphorus purifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203715281U true CN203715281U (en) | 2014-07-16 |
Family
ID=51154449
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420072092.XU Expired - Lifetime CN203715281U (en) | 2014-02-19 | 2014-02-19 | Capacitor grade phosphoric acid yellow phosphorus purifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203715281U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103754841A (en) * | 2014-02-19 | 2014-04-30 | 四川蓝海化工（集团）有限公司 | Purifying device for capacitor-grade phosphoric acid yellow phosphorus |
| CN110330001A (en) * | 2019-08-19 | 2019-10-15 | 贵州新东浩化工材料科技有限公司 | A kind of method and device recycling yellow phosphorus in phosphorus mud using piston flow reactor |
-
2014
- 2014-02-19 CN CN201420072092.XU patent/CN203715281U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103754841A (en) * | 2014-02-19 | 2014-04-30 | 四川蓝海化工（集团）有限公司 | Purifying device for capacitor-grade phosphoric acid yellow phosphorus |
| CN110330001A (en) * | 2019-08-19 | 2019-10-15 | 贵州新东浩化工材料科技有限公司 | A kind of method and device recycling yellow phosphorus in phosphorus mud using piston flow reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140716 |