CN205413054U - Cationic resin separation recovery system - Google Patents
Cationic resin separation recovery system Download PDFInfo
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- CN205413054U CN205413054U CN201521084365.3U CN201521084365U CN205413054U CN 205413054 U CN205413054 U CN 205413054U CN 201521084365 U CN201521084365 U CN 201521084365U CN 205413054 U CN205413054 U CN 205413054U
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- resin
- pipeline
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- water scrubber
- recovery system
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Abstract
The utility model relates to a chemical industry equipment field, concretely relates to cationic resin separation recovery system. Including be used for with good resin and damaged resin wash the water wash column separated, be used for with good resin carry the resin reactor the transport pressurized canister, carry out the resin of damage solid -liquid separation's useless resin filter and connect the pipeline and the valve of each container, the overflow mouth has been seted up on the water wash column, the overflow mouth pass through the pipeline with useless resin filter is connected, the pan feeding mouth of carrying the pressurized canister pass through the pipeline with the bin outlet of water wash column bottom is connected. The utility model discloses simple structure separates the resin of damage and complete resin through the mode of washing, puts into resin reactor again with good resin, the waste of the resin of avoiding, and the resin reactor is sent into after through the pressurization to resin after the washing, and whole process need not be suspend, has improved reaction efficiency, has practiced thrift the energy, has reduced the manual operation degree of difficulty, has reduced workman's working strength.
Description
Technical field
This utility model relates to a kind of cationic resin separation and recovery system.
Background technology
At present, fixed bed cation resin reaction device the most generally exists, and mainly is used for reclaiming the valuable ion in industry tailing (liquid) or poisonous and harmful ion (abbreviation object ion) by ion exchange form.Resin, by the high concentration object ion in absorption material, carries out being desorbed and resin regeneration with regenerated liquid after replacing with unclassified stores, reaches the purpose recycled.Relative to other resin reaction devices, fixed bed has simple to operate, investment and the low advantage of maintenance cost, and this is also the reason that the most a lot of industry and producer select fixed bed.In fixed bed, resin is after long-play, and part resin occurs that abrasion is pulverized, and have impact on the overall serviceability of resin, and usual processing method is all to be discharged by the resin in reactor, again puts into new resin.Because the resin after Shi Yonging cannot realize isolating quality, causing the resin waste that part is intact, need stopping at fixed time locking apparatus to carry out batch replacement simultaneously, manual labor amount is big.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of resin of can saving can reduce again the cationic resin separation and recovery system of hand labor intensity.
This utility model adopts the following technical scheme that
A kind of cationic resin separation and recovery system, including for good resin and damaged resin are cleaned separate water scrubber, be used for the resin by the conveying pressurized canister of good resin transfer to resin reaction device, by breakage and carry out the spent resin filter of solid-liquid separation and connect pipeline and the valve of each container, overfall is offered on described water scrubber, described overfall is connected with described spent resin filter by pipeline, the feeding mouth of described conveying pressurized canister is connected with the discharge gate bottom described water scrubber by pipeline, and described spent resin filter bottom offers discharge outlet.
Improve further as this utility model, it also includes for adding head tank to the resin of resin reaction device feeding, described resin is added the entrance of head tank and is connected by the outlet of pipeline with described conveying pressurized canister, described resin is added the outlet of head tank and is connected by the charge door of pipeline with resin reaction device, and described resin adds the head tank installation site charge door higher than resin reaction device.
Improve further as this utility model, resin settling tank it is also equipped with between described water scrubber and spent resin filter, the entrance of described resin settling tank is connected by the overfall of pipeline with water scrubber, the outlet of described resin settling tank is connected with the entrance of spent resin filter, and described resin settling tank top offers overfall.
Good effect of the present utility model is as follows:
This utility model simple in construction, by the way of washing, damaged resin and complete resin are separated, good resin are reentered in resin reaction device, it is to avoid the waste of resin, new resin is added in water scrubber simultaneously, can be removed by the magazine on its surface, the resin after washing is by sending into resin reaction device after pressurization, whole process need not be interrupted, improve reaction efficiency, save the energy, decreased manual operation difficulty, reduce the working strength of workman.
Accompanying drawing explanation
Accompanying drawing 1 is this utility model structural representation.
In the accompanying drawings: 1 water scrubber, 2 conveying pressurized canister, 3 resins add head tank, 4 resin settling tanks, 5 spent resin filters, 6 collecting pits.
Detailed description of the invention
With detailed description of the invention, this utility model is described in further detail below in conjunction with the accompanying drawings.
nullA kind of cationic resin separation and recovery system as shown in Figure 1，Including for good resin and damaged resin are cleaned the water scrubber 1 separated，For the conveying pressurized canister 2 by good resin transfer to resin reaction device，For adding head tank 3 to the resin of resin reaction device feeding，Damaged resin is carried out the spent resin filter 5 of solid-liquid separation，It is arranged on the resin settling tank 4 between described water scrubber 1 and spent resin filter 5 and connects pipeline and the valve of each container，After resin reacts a period of time in resin reaction device，By in a resin discharge part to water scrubber 1，Resin is after water scrubber，Broken resin swims in the surface of water in water scrubber under the effect of water，Then the overfall by offering on described water scrubber 1 flows out，Good resin sinks to the bottom of water scrubber 1 under gravity，The feeding mouth of described conveying pressurized canister 2 is connected with the discharge gate bottom described water scrubber 1 by pipeline，Good resin arrives resin after pressurizeing in being just exhausted directly to carry pressurized canister 2 and adds head tank 3.
Described resin is added the entrance of head tank 3 and is connected by the outlet of pipeline with described conveying pressurized canister 2, described resin is added the outlet of head tank 3 and is connected by the charge door of pipeline with resin reaction device, and described resin adds head tank 3 installation site charge door higher than resin reaction device, the when that amount of resin in resin reaction device being few, resin is added to participation reaction in resin reaction device by the valve opening resin interpolation head tank 3 downstream.
The entrance of described resin settling tank 4 is connected by the overfall of pipeline with water scrubber 1, broken resin floating in water scrubber 1 enters in resin settling tank 4 along with water, after resin elapsed time here precipitation, broken resin precipitated is to bottom, water after precipitation flows out resin settling tank 4 by the overfall at its top, then it is passed in water scrubber 1 by pipeline, the outlet of described resin settling tank 4 is connected with the entrance of spent resin filter 5, the valve of the outlet of described resin settling tank 4 is opened after precipitation a period of time, resin after precipitation reaches spent resin filter 5 by pipeline.
Resin and water are completely separated out in described spent resin filter 5 by the resin after precipitation through filtration, discharge outlet is offered bottom described spent resin filter 5, water is discharged in collecting pit by discharge outlet, is then sent for processing, and the resin trap filtered out is to being uniformly processed the most afterwards.
Claims (3)
1. a cationic resin separation and recovery system, it is characterized in that: include for good resin and damaged resin are cleaned the water scrubber (1) separated, for by the conveying pressurized canister (2) of good resin transfer to resin reaction device, damaged resin is carried out the spent resin filter (5) of solid-liquid separation and connects pipeline and the valve of each container, described water scrubber offers overfall on (1), described overfall is connected with described spent resin filter (5) by pipeline, the feeding mouth of described conveying pressurized canister (2) is connected by the discharge gate of pipeline with described water scrubber (1) bottom, described spent resin filter (5) bottom offers discharge outlet.
A kind of cationic resin separation and recovery system the most according to claim 1, it is characterized in that: it also includes for adding head tank (3) to the resin of resin reaction device feeding, described resin is added the entrance of head tank (3) and is connected by the outlet of pipeline with described conveying pressurized canister (2), described resin is added the outlet of head tank (3) and is connected by the charge door of pipeline with resin reaction device, and described resin adds head tank (3) installation site charge door higher than resin reaction device.
A kind of cationic resin separation and recovery system the most according to claim 1 and 2, it is characterized in that: between described water scrubber (1) and spent resin filter (5), be also equipped with resin settling tank (4), the entrance of described resin settling tank (4) is connected by the overfall of pipeline with water scrubber (1), the outlet of described resin settling tank (4) is connected with the entrance of spent resin filter (5), and described resin settling tank (4) top offers overfall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521084365.3U CN205413054U (en) | 2015-12-23 | 2015-12-23 | Cationic resin separation recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521084365.3U CN205413054U (en) | 2015-12-23 | 2015-12-23 | Cationic resin separation recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205413054U true CN205413054U (en) | 2016-08-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521084365.3U Active CN205413054U (en) | 2015-12-23 | 2015-12-23 | Cationic resin separation recovery system |
Country Status (1)
| Country | Link |
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| CN (1) | CN205413054U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107694613A (en) * | 2017-11-29 | 2018-02-16 | 洛阳市天誉环保工程有限公司 | The technique and device of phenol impurity in a kind of removal doctor solution |
| CN111841666A (en) * | 2020-07-14 | 2020-10-30 | 江苏核电有限公司 | Movable resin bed external flushing device and flushing method thereof |
-
2015
- 2015-12-23 CN CN201521084365.3U patent/CN205413054U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107694613A (en) * | 2017-11-29 | 2018-02-16 | 洛阳市天誉环保工程有限公司 | The technique and device of phenol impurity in a kind of removal doctor solution |
| CN111841666A (en) * | 2020-07-14 | 2020-10-30 | 江苏核电有限公司 | Movable resin bed external flushing device and flushing method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A cation resin separation and recovery system Effective date of registration: 20201026 Granted publication date: 20160803 Pledgee: Bank of Cangzhou Limited by Share Ltd. Tangshan branch Pledgor: TANGSHAN ZHONGHAO CHEMICAL Co.,Ltd. Registration number: Y2020980007150 |