CN201680152U - Double pipelines for conveying resin - Google Patents
Double pipelines for conveying resin Download PDFInfo
- Publication number
- CN201680152U CN201680152U CN2010201480304U CN201020148030U CN201680152U CN 201680152 U CN201680152 U CN 201680152U CN 2010201480304 U CN2010201480304 U CN 2010201480304U CN 201020148030 U CN201020148030 U CN 201020148030U CN 201680152 U CN201680152 U CN 201680152U
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- Prior art keywords
- resin
- pipe
- tower
- bottom tube
- valve
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- Expired - Fee Related
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Abstract
The utility model relates to double pipelines for conveying resin, in particular to a pipeline pipe for a conventional island condensing water refining system of a nuclear power plant. The double pipelines for conveying resin comprise a resin outlet pipe, a resin inlet pipe, a resin return pipe, a separating tower inlet pipe, a lower manifold, a separating tower bottom pipe, an anion resin bottom pipe, a cation resin bottom pipe, a cation resin side pipe, a communicating pipe, a storing tower bottom pipe and a storing tower side pipe. The utility model has the advantages of reasonable structural design, no resin residues, high running efficiency, and simple and easy installation.
Description
Technical field
The utility model relates to a kind of twin flue that is used for resin transfer, specifically is the piping installation of a kind of nuclear power plant conventional island condensed water precision processing system.
Background technique
The effect of nuclear power plant's condensed water precision processing system operation depends primarily on the technology and the effect of ion exchange resin regeneration.Because nuclear power plant is very high to the quality requirement of water, general reclaiming process does not reach regeneration effect.The piping installation operational effect of present domestic nuclear power plant condensed water precision processing system is undesirable, often causes the separation of positive resin anion (R.A.) not thorough, also can cull in the pipeline, greatly reduce overall system efficiency
Summary of the invention
The twin flue that is used for resin transfer that technical problem to be solved in the utility model provides a kind of reasonable in design, no resin residue, operational efficiency height, is simple and easy to install.
It is this twin flue that is used for resin transfer that the utility model solves the problems of the technologies described above the technological scheme that is adopted, its structural feature is: comprise the fat pipe, advance the fat pipe, return the fat pipe, the separator inlet pipe, following house steward, the separator bottom tube, the negative resin bottom tube, sun resin bottom tube, sun resin side pipe, connecting tube, store the tower bottom tube, store the tower side pipe, wherein, a described end that advances the fat pipe links to each other with the grease outlet that mixes the bed exchanger, the other end links to each other with the separator inlet pipe with time fat pipe respectively, the separator inlet pipe links to each other with the resin isolation tower, the other end that returns the fat pipe respectively with go out the fat pipe and link to each other with following house steward, following house steward is provided with the separator bottom tube, the negative resin bottom tube, sun resin bottom tube, sun resin side pipe, store the tower bottom tube, store the tower side pipe, the separator bottom tube links to each other with the bottom of resin isolation tower, the negative resin bottom tube links to each other with the bottom of negative resin regenering tower, sun resin bottom tube links to each other with the side with the bottom of Yang Shuzhizaishengta respectively with positive resin side pipe, store the tower bottom tube, storing the tower side pipe links to each other with the side with the bottom of storing tower respectively, be arranged on described connecting tube between resin isolation tower and the negative resin regenering tower, describedly go out the fat pipe and link to each other with the grease inlet that mixes the bed exchanger.
Described in the utility modelly go out the fat pipe and be provided with out fat valve and following visor.
Described in the utility modelly advance the fat pipe and be provided with ester inlet valve and last visor.
Separator inlet pipe described in the utility model is provided with the separator valve.
Described in the utility model time the fat pipe is provided with back the fat pipe valve.
Be respectively arranged with separator bottom tube valve, negative resin bottom tube valve, positive resin bottom tube valve, positive resin side pipe valve on separator bottom tube described in the utility model, negative resin bottom tube, positive resin bottom tube, positive resin side pipe, storage tower bottom tube, the storage tower side pipe, store tower bottom tube valve, store tower side pipe valve.
Connecting tube described in the utility model is provided with the connection pipe valve.
The utility model is compared with prior art and is had the following advantages and effect:
Inverted "L" shaped structure pipeline is set, and the excessive and close regenering tower of the large radius arc valve that the storage tank position installs of holding concurrently all makes resin pipeline of the present utility model reduce flow resistance, makes the resin transfer smoothness, prevents that resin from stopping up in pipeline.Reasonable in design simple in structure.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
Below in conjunction with embodiment the utility model is described in further detail, following examples are to explanation of the present utility model and the utility model is not limited to following examples.
Embodiment 1: as shown in Figure 1, the twin flue that is used for resin transfer of present embodiment mainly comprise fat pipe 2, advance fat pipe 5, return fat pipe 7, separator inlet pipe 8, down house steward 15, separator bottom tube 16, negative resin bottom tube 17, positive resin bottom tube 18, positive resin side pipe 19, connecting tube 20, store tower bottom tube 21, store tower side pipe 22, go out fat pipe 2, advance fat pipe 5 and link to each other with grease outlet with the grease inlet that mixes the bed exchanger respectively.The other end that advances fat pipe 5 links to each other with separator inlet pipe 8 with time fat pipe 7 respectively, is advancing to be equipped with on the fat pipe 5 ester inlet valve 6 and last visor 11.Separator inlet pipe 8 links to each other with resin isolation tower 1, separator inlet pipe 8 is provided with separator valve 10, return fat pipe 7 and be provided with back fat pipe valve 9, the other end that returns fat pipe 7 respectively with go out fat pipe 2 and link to each other with following house steward 15, go out fat pipe 2 and be provided with out fat valve 3 and following visor 4, following house steward 15 is provided with separator bottom tube 16, negative resin bottom tube 17, sun resin bottom tube 18, sun resin side pipe 19, store tower bottom tube 21, store tower side pipe 22, separator bottom tube 16, negative resin bottom tube 17, sun resin bottom tube 18, sun resin side pipe 19, store tower bottom tube 21, store on the tower side pipe 22 and be provided with separator bottom tube valve 26 respectively, negative resin bottom tube valve 27, sun resin bottom tube valve 28, sun resin side pipe valve 24, store tower bottom tube valve 29, store tower side pipe valve 25, separator bottom tube 19 links to each other with the bottom of resin isolation tower 1, negative resin bottom tube 17 links to each other with the bottom of negative resin regenering tower 12, sun resin bottom tube 18 links to each other with the side with the bottom of positive resin regeneration tower 13 respectively with positive resin side pipe 19, store tower bottom tube 21, storing tower side pipe 22 links to each other with the side with the bottom of storing tower 14 respectively, be arranged on described connecting tube 20 between resin isolation tower 1 and the negative resin regenering tower 12, be provided with connection pipe valve 23 connecting tube 20.
In addition, need to prove, the specific embodiment described in this specification, its zero, the shape of parts, institute's title of being named etc. can be different.Allly conceive equivalence or the simple change that described structure, feature and principle are done, be included in the protection domain of the utility model patent according to the utility model patent.The utility model person of ordinary skill in the field can make various modifications or replenishes or adopt similar mode to substitute described specific embodiment; only otherwise depart from structure of the present utility model or surmount the defined scope of these claims, all should belong to protection domain of the present utility model.
Claims (7)
1. twin flue that is used for resin transfer, it is characterized in that: comprise the fat pipe, advance the fat pipe, return the fat pipe, the separator inlet pipe, following house steward, the separator bottom tube, the negative resin bottom tube, sun resin bottom tube, sun resin side pipe, connecting tube, store the tower bottom tube, store the tower side pipe, wherein, a described end that advances the fat pipe links to each other with the grease outlet that mixes the bed exchanger, the other end links to each other with the separator inlet pipe with time fat pipe respectively, the separator inlet pipe links to each other with the resin isolation tower, the other end that returns the fat pipe respectively with go out the fat pipe and link to each other with following house steward, following house steward is provided with the separator bottom tube, the negative resin bottom tube, sun resin bottom tube, sun resin side pipe, store the tower bottom tube, store the tower side pipe, the separator bottom tube links to each other with the bottom of resin isolation tower, the negative resin bottom tube links to each other with the bottom of negative resin regenering tower, sun resin bottom tube links to each other with the side with the bottom of Yang Shuzhizaishengta respectively with positive resin side pipe, store the tower bottom tube, storing the tower side pipe links to each other with the side with the bottom of storing tower respectively, be arranged on described connecting tube between resin isolation tower and the negative resin regenering tower, describedly go out the fat pipe and link to each other with the grease inlet that mixes the bed exchanger.
2. the twin flue that is used for resin transfer according to claim 1 is characterized in that: describedly go out the fat pipe and be provided with out fat valve and following visor.
3. the twin flue that is used for resin transfer according to claim 1 is characterized in that: describedly advance the fat pipe and be provided with ester inlet valve and last visor.
4. the twin flue that is used for resin transfer according to claim 1 is characterized in that: described separator inlet pipe is provided with the separator valve.
5. the twin flue that is used for resin transfer according to claim 1 is characterized in that: described time the fat pipe is provided with back the fat pipe valve.
6. the twin flue that is used for resin transfer according to claim 1 is characterized in that: be respectively arranged with separator bottom tube valve, negative resin bottom tube valve, positive resin bottom tube valve, positive resin side pipe valve on described separator bottom tube, negative resin bottom tube, positive resin bottom tube, positive resin side pipe, storage tower bottom tube, the storage tower side pipe, store tower bottom tube valve, store tower side pipe valve.
7. the twin flue that is used for resin transfer according to claim 1 is characterized in that: described connecting tube is provided with the connection pipe valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201480304U CN201680152U (en) | 2010-04-01 | 2010-04-01 | Double pipelines for conveying resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201480304U CN201680152U (en) | 2010-04-01 | 2010-04-01 | Double pipelines for conveying resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201680152U true CN201680152U (en) | 2010-12-22 |
Family
ID=43345196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201480304U Expired - Fee Related CN201680152U (en) | 2010-04-01 | 2010-04-01 | Double pipelines for conveying resin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201680152U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115259280A (en) * | 2022-07-11 | 2022-11-01 | 中国核电工程有限公司 | Mixed ion exchange resin separation and transportation method |
-
2010
- 2010-04-01 CN CN2010201480304U patent/CN201680152U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115259280A (en) * | 2022-07-11 | 2022-11-01 | 中国核电工程有限公司 | Mixed ion exchange resin separation and transportation 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: 20101222 Termination date: 20160401 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |