CN204752277U - Hydrogen is led duolite and is concentrated regenerating unit - Google Patents
Hydrogen is led duolite and is concentrated regenerating unit Download PDFInfo
- Publication number
- CN204752277U CN204752277U CN201520390191.7U CN201520390191U CN204752277U CN 204752277 U CN204752277 U CN 204752277U CN 201520390191 U CN201520390191 U CN 201520390191U CN 204752277 U CN204752277 U CN 204752277U
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- China
- Prior art keywords
- water
- pipeline
- batchmeter
- valve
- exchange resin
- 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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- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 26
- 239000001257 hydrogen Substances 0.000 title claims abstract description 26
- 230000001172 regenerating effect Effects 0.000 title claims abstract description 17
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title abstract description 9
- 229920002125 Sokalan® Polymers 0.000 title abstract 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 102
- 239000007788 liquid Substances 0.000 claims abstract description 52
- 239000011347 resin Substances 0.000 claims abstract description 35
- 229920005989 resin Polymers 0.000 claims abstract description 35
- 239000012141 concentrate Substances 0.000 claims abstract description 16
- 238000005406 washing Methods 0.000 claims abstract description 12
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 24
- 239000003456 ion exchange resin Substances 0.000 claims description 24
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 24
- 238000007599 discharging Methods 0.000 claims description 17
- 238000001514 detection method Methods 0.000 claims description 6
- 230000000630 rising effect Effects 0.000 claims description 5
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 6
- 230000008929 regeneration Effects 0.000 abstract description 17
- 238000011069 regeneration method Methods 0.000 abstract description 17
- 238000000034 method Methods 0.000 abstract description 6
- 238000012372 quality testing Methods 0.000 abstract 1
- 150000002431 hydrogen Chemical class 0.000 description 11
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 5
- 238000005342 ion exchange Methods 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- POIUWJQBRNEFGX-XAMSXPGMSA-N cathelicidin Chemical compound C([C@@H](C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CO)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H]([C@@H](C)CC)C(=O)NCC(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CC=1C=CC=CC=1)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)CC)C(=O)N[C@@H](C(C)C)C(=O)N[C@@H](CCC(N)=O)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)CC)C(=O)N[C@@H](CCCCN)C(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CC=1C=CC=CC=1)C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H](CC(N)=O)C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](C(C)C)C(=O)N1[C@@H](CCC1)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)O)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CO)C(O)=O)NC(=O)[C@H](CC=1C=CC=CC=1)NC(=O)[C@H](CC(O)=O)NC(=O)CNC(=O)[C@H](CC(C)C)NC(=O)[C@@H](N)CC(C)C)C1=CC=CC=C1 POIUWJQBRNEFGX-XAMSXPGMSA-N 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- RVPVRDXYQKGNMQ-UHFFFAOYSA-N lead(2+) Chemical group [Pb+2] RVPVRDXYQKGNMQ-UHFFFAOYSA-N 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a hydrogen is led duolite and is concentrated regenerating unit, including the duolite centralized processing post that is equipped with water inlet and delivery port, regeneration liquid pipeline, just wash pipeline and backwash pipeline, the water inlet is equipped with inlet valve, regeneration liquid pipeline with is just washing the parallelly connected back of pipeline and is passing through the water inlet of inlet valve access duolite centralized processing post, the backwash pipeline is including connecting at regeneration liquid pipeline and backwash inlet tube after just washing the pipeline and the backwash outlet pipe of connection at the water inlet, the delivery port is equipped with the drainage valve, connects in parallel and have the water quality testing pipeline in the both ends of drainage valve, and the lower extreme of duolite centralized processing post still feeds through has the resin to derive the pipeline. Hydrogen is led duolite and is concentrated regenerating unit easy operation, dynamic regeneration treatment is effectual, realizes that hydrogen ionic conductivity detector duolite concentrates regeneration treatment, once can accomplish all hydrogen of 1-2 unit and lead the duolite regeneration treatment overall process, and the resin regeneration degree is high, work efficiency is high.
Description
Technical field
The utility model relates to a kind of exchange resin and concentrates regenerating unit, and specifically a kind of hydrogen diversion sub-exchange resin concentrates regenerating unit.
Background technology
Power plant's hydrogen ion (leading hereinafter referred to as hydrogen) is the important indicator of water quality such as supervision boiler water, oiler feed etc., and online hydrogen ion detector is widely used in each position of Power Plant Water Vapor system.Hydrogen is led ion exchange column and is arranged at the import of online hydrogen ion detector, and the quantities of electric charge such as the positively charged ion in water sample are converted into hydrogen ion, and the resin that hydrogen is led in ion exchange column needs regular regeneration.
The renovation process of the resin that current hydrogen is led in ion exchange column generally adopts manual handling: take exchange column apart, pour out resin, stir, topple over change water remove impurity, salt acid soak, de-mineralized water displacement, cleaning, detect cleaning water quality, backfill ion exchange column, waterproof pressure test.This process is generally carried out in beaker, and existing problems comprise: primary treatment amount is little, and resin easily changes water operation loss with toppling over, static immersing regeneration effect is poor.
Summary of the invention
For the defect of prior art, the utility model discloses a kind of hydrogen diversion sub-exchange resin and concentrate regenerating unit, simple to operate, dynamic manipulation of regeneration is effective, and working efficiency is high.
In order to solve the technical problem, the technical solution adopted in the utility model is: a kind of hydrogen diversion sub-exchange resin concentrates regenerating unit, comprise the ion exchange resin being provided with water-in and water outlet to focus on post, regenerated liquid pipeline, just wash pipeline and backwash pipeline, water-in is provided with inlet valve, regenerated liquid pipeline and focus on the water-in of post by inlet valve access ion exchange resin after just washing pipeline parallel connection; Backwash pipeline comprises the backwash water inlet pipe after being connected to regenerated liquid pipeline and just washing pipeline and is connected to the backwash rising pipe of water-in, and backwash water inlet pipe is provided with backwash inlet valve, and backwash rising pipe is provided with backwash water discharging valve; Water outlet is provided with water discharging valve, and the two ends of water discharging valve are parallel with water quality detection pipeline, and the lower end that ion exchange resin focuses on post is also communicated with resin outgoing line, and resin outgoing line is provided with resin and derives valve.
Further, described regenerated liquid pipeline comprises high-order regenerated liquid case and regenerated liquid batchmeter, the high-order water outlet of regenerated liquid case and the water-in of regenerated liquid batchmeter communicate and are provided with high-order regenerated liquid case valve, and the water-in that water outlet and the ion exchange resin of regenerated liquid batchmeter focus on post communicates and is provided with regenerated liquid batchmeter valve.
Further, described pipeline of just washing comprises high-order flush box and wash-down water batchmeter, the water outlet of high-order flush box communicates with the water-in of wash-down water batchmeter and is provided with high-order flush box valve, and the water-in that water outlet and the ion exchange resin of wash-down water batchmeter focus on post communicates and is provided with wash-down water batchmeter valve.
Further, described water quality detection pipeline comprises electric conductivity detector and electric conductivity detector inlet valve, before electric conductivity detector inlet valve is arranged on electric conductivity detector.
Further, in order to make detected result more accurate, wash-down water batchmeter is provided with wash-down water batchmeter scale marks.
Further, described ion exchange resin focuses on column bottom and is provided with water cap, and water discharging valve is connected to bottom water cap, and resin outgoing line is located at above water cap.
The beneficial effects of the utility model: hydrogen diversion sub-exchange resin described in the utility model concentrates regenerating unit simple to operate, dynamic manipulation of regeneration is effective, realize hydrogen ion detector ion exchange resin and concentrate manipulation of regeneration, once can complete all hydrogen diversion sub-exchange resin manipulation of regeneration whole processes of 2 units, working efficiency is high; Lead ion exchange column Capacity design regenerated liquid batchmeter and wash-down water batchmeter according to hydrogen, in batchmeter, liquid stream is complete reaches holomorphosis effect just, do not waste, do not need human metering, save time, laborsaving, do not waste, economical, efficient.Be provided with effluent quality test set, effluent quality after on-line checkingi process, confirm developing result, convenient and swift.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure: 1, high-order regenerated liquid case, 2, high-order flush box, 3, regenerated liquid batchmeter, 4, wash-down water batchmeter, 5, ion exchange resin focuses on post, 6, electric conductivity detector, 7, high-order regenerated liquid case valve, 8, high-order flush box valve, 9, regenerated liquid batchmeter valve, 10, wash-down water batchmeter valve, 11, inlet valve, 12, backwash inlet valve, 13, backwash water discharging valve, 14, electric conductivity detector inlet valve, 15, water discharging valve, 16, wash-down water batchmeter scale marks, 17, valve derived by resin, 18, water cap, 19, water-in, 20, water outlet.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model be described further and limit.
As shown in Figure 1, a kind of hydrogen diversion sub-exchange resin concentrates regenerating unit, comprise the ion exchange resin being provided with water-in 19 and water outlet 20 to focus on post 5, regenerated liquid pipeline, just wash pipeline and backwash pipeline, water-in 19 is provided with inlet valve 11, regenerated liquid pipeline and access by inlet valve 11 water-in 19 that ion exchange resin focuses on post 5 after just washing pipeline parallel connection; Backwash pipeline comprises the backwash water inlet pipe after being connected to regenerated liquid pipeline and just washing pipeline and is connected to the backwash rising pipe of water-in 19, and backwash water inlet pipe is provided with backwash inlet valve 12, and backwash rising pipe is provided with backwash water discharging valve 13; Water outlet 20 is provided with water discharging valve 15, and the two ends of water discharging valve 15 are parallel with water quality detection pipeline, and the lower end that ion exchange resin focuses on post 5 is also communicated with resin outgoing line, and resin outgoing line is provided with resin and derives valve 17.
Described regenerated liquid pipeline comprises high-order regenerated liquid case 1 and regenerated liquid batchmeter 3, the high-order water outlet of regenerated liquid case 1 and the water-in of regenerated liquid batchmeter 3 communicate and are provided with high-order regenerated liquid case valve 7, and the water-in 19 that water outlet and the ion exchange resin of regenerated liquid batchmeter 3 focus on post 5 communicates and is provided with regenerated liquid batchmeter valve 9.
Described pipeline of just washing comprises high-order flush box 2 and wash-down water batchmeter 4, the water outlet of high-order flush box 2 communicates with the water-in of wash-down water batchmeter 4 and is provided with high-order flush box valve 8, and the water-in 19 that water outlet and the ion exchange resin of wash-down water batchmeter 4 focus on post 5 communicates and is provided with wash-down water batchmeter valve 10.
Described water quality detection pipeline comprises electric conductivity detector 6 and electric conductivity detector inlet valve 14, before electric conductivity detector inlet valve 14 is arranged on electric conductivity detector 6.
In order to make detected result more accurate, wash-down water batchmeter 4 is provided with wash-down water batchmeter scale marks 16.
Further, described ion exchange resin focuses on bottom post 5 and is provided with water cap 18, and water discharging valve 15 is connected to bottom water cap 18, and resin outgoing line is located at above water cap 18.
Hydrogen diversion sub-exchange resin described in the utility model concentrates the working process of regenerating unit to be:
(1) all hydrogen diversion sub-exchange resins are concentrated pour ion exchange resin into and focus on post 5, connect regenerated liquid pipeline and just washing pipeline;
(2) the regeneration of hydrochloric acid liquid of 5% is prepared in high-order regenerated liquid case 1;
(3) de-mineralized water is added in high-order flush box 2;
(4) open high-order flush box valve 8, fill wash-down water batchmeter 4, close high-order flush box valve 8;
(5) close inlet valve 11, open wash-down water batchmeter valve 10, backwash inlet valve 12, backwash water discharging valve 13, back flushing ion exchange resin focuses on post 5 to without visible foreign, the transparent clarification of water outlet, closes all valves;
(6) open high-order regenerated liquid case valve 7, regeneration of hydrochloric acid liquid is filled regenerated liquid batchmeter 3, close high-order regenerated liquid case valve 7;
(7) open valve regenerated liquid batchmeter valve 9, backwash inlet valve 12, backwash water discharging valve 13, counter-current regeneration ion exchange resin focuses on post 5, and to regenerated liquid batchmeter 3, regenerated liquid stream is empty, closes all valves;
(8) open high-order flush box valve 8, fill wash-down water batchmeter 4, close high-order flush box valve 8;
(9) open wash-down water batchmeter valve 10, inlet valve 11, water discharging valve 15, following current is rinsed ion exchange resin and is focused on post 5, to wash-down water batchmeter scale marks 16.
(10) open electric conductivity detector inlet valve 14, close water discharging valve 15, detect effluent quality.If effluent quality is defective, repeats (8), (9) step is qualified to water quality.Close all valves.
(11) de-mineralized water is added high-order flush box 2, open high-order flush box valve 8, wash-down water batchmeter valve 10, backwash inlet valve 12, valve 17 aperture derived by adjustment resin, the resin regenerated is derived, loading hydrogen leads in exchange column, namely complete regeneration, proceed to stand-by state, can use at any time.
Claims (6)
1. a hydrogen diversion sub-exchange resin concentrates regenerating unit, it is characterized in that: comprise the ion exchange resin being provided with water-in and water outlet and focus on post, regenerated liquid pipeline, just wash pipeline and backwash pipeline, water-in is provided with inlet valve, regenerated liquid pipeline and focus on the water-in of post by inlet valve access ion exchange resin after just washing pipeline parallel connection; Backwash pipeline comprises the backwash water inlet pipe after being connected to regenerated liquid pipeline and just washing pipeline and is connected to the backwash rising pipe of water-in; Water outlet is provided with water discharging valve, and the two ends of water discharging valve are parallel with water quality detection pipeline, and the lower end that ion exchange resin focuses on post is also communicated with resin outgoing line.
2. hydrogen diversion sub-exchange resin according to claim 1 concentrates regenerating unit, it is characterized in that: described regenerated liquid pipeline comprises high-order regenerated liquid case and regenerated liquid batchmeter, the water outlet of high-order regenerated liquid case is connected with the water-in of regenerated liquid batchmeter and is provided with high-order regenerated liquid case valve, and the water-in that water outlet and the ion exchange resin of regenerated liquid batchmeter focus on post is connected and is provided with regenerated liquid batchmeter valve.
3. hydrogen diversion sub-exchange resin according to claim 1 and 2 concentrates regenerating unit, it is characterized in that: described pipeline of just washing comprises high-order flush box and wash-down water batchmeter, the water outlet of high-order flush box is connected with the water-in of wash-down water batchmeter and is provided with high-order flush box valve, and the water-in that water outlet and the ion exchange resin of wash-down water batchmeter focus on post is connected and is provided with wash-down water batchmeter valve.
4. hydrogen diversion sub-exchange resin according to claim 3 concentrates regenerating unit, it is characterized in that: described water quality detection pipeline comprises electric conductivity detector and electric conductivity detector inlet valve, before electric conductivity detector inlet valve is arranged on electric conductivity detector.
5. hydrogen diversion sub-exchange resin according to claim 4 concentrates regenerating unit, it is characterized in that: described wash-down water batchmeter is provided with wash-down water batchmeter scale marks.
6. hydrogen diversion sub-exchange resin according to claim 5 concentrates regenerating unit, it is characterized in that: described ion exchange resin focuses on column bottom and is provided with water cap, and water discharging valve is connected to bottom water cap, and resin outgoing line is located at above water cap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520390191.7U CN204752277U (en) | 2015-06-09 | 2015-06-09 | Hydrogen is led duolite and is concentrated regenerating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520390191.7U CN204752277U (en) | 2015-06-09 | 2015-06-09 | Hydrogen is led duolite and is concentrated regenerating unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204752277U true CN204752277U (en) | 2015-11-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520390191.7U Expired - Fee Related CN204752277U (en) | 2015-06-09 | 2015-06-09 | Hydrogen is led duolite and is concentrated regenerating unit |
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| Country | Link |
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| CN (1) | CN204752277U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106940335A (en) * | 2017-02-28 | 2017-07-11 | 浙江浙能嘉华发电有限公司 | A kind of resin-column on-line rinsing device |
| CN107199055A (en) * | 2017-05-19 | 2017-09-26 | 江苏常熟发电有限公司 | Hydrogen leads resin and dynamically cleans regenerating unit and its operating method |
| CN110560183A (en) * | 2019-10-09 | 2019-12-13 | 深圳市加美富实业有限公司 | Automatic resin column regeneration device and automatic regeneration method |
| CN112299525A (en) * | 2019-08-01 | 2021-02-02 | 造梦者科技有限公司 | Method for increasing purified water quantity of exchanger and water quality purification device thereof |
-
2015
- 2015-06-09 CN CN201520390191.7U patent/CN204752277U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106940335A (en) * | 2017-02-28 | 2017-07-11 | 浙江浙能嘉华发电有限公司 | A kind of resin-column on-line rinsing device |
| CN107199055A (en) * | 2017-05-19 | 2017-09-26 | 江苏常熟发电有限公司 | Hydrogen leads resin and dynamically cleans regenerating unit and its operating method |
| CN112299525A (en) * | 2019-08-01 | 2021-02-02 | 造梦者科技有限公司 | Method for increasing purified water quantity of exchanger and water quality purification device thereof |
| CN110560183A (en) * | 2019-10-09 | 2019-12-13 | 深圳市加美富实业有限公司 | Automatic resin column regeneration device and automatic regeneration method |
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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 |
Granted publication date: 20151111 Termination date: 20170609 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |