CN207472100U - A kind of recycle device of steam condensation water - Google Patents
A kind of recycle device of steam condensation water Download PDFInfo
- Publication number
- CN207472100U CN207472100U CN201721531679.2U CN201721531679U CN207472100U CN 207472100 U CN207472100 U CN 207472100U CN 201721531679 U CN201721531679 U CN 201721531679U CN 207472100 U CN207472100 U CN 207472100U
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- CN
- China
- Prior art keywords
- valve
- pipeline
- water
- condensate
- steam
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Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 86
- 238000009833 condensation Methods 0.000 title claims abstract description 15
- 230000005494 condensation Effects 0.000 title claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000010992 reflux Methods 0.000 claims abstract description 16
- 238000000034 method Methods 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims description 7
- 238000006356 dehydrogenation reaction Methods 0.000 claims description 4
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000012946 outsourcing Methods 0.000 abstract description 2
- 238000010792 warming Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a kind of recycle devices of steam condensation water, including condensate water pot, condensate pump, indirect steam is connected separately on condensate water pot to concentration tower heating pipeline, cut light tower feed preheater steam return pipeline, cut light tower feed preheater steam lead line, water stripping water return tank pipeline, condensate pump reflux pipeline, main steam header road return piping, condensate pump outlet line, the indirect steam are connected to condensate water pot to concentration tower heating pipeline by valve；The condensate pump outlet line is connected to condensate pump by valve, and the condensate pump is connected to condensate pump reflux pipeline by valve, and the condensate pump reflux pipeline is connected with main steam header road return piping.The utility model solves the problems, such as process water in device（Original device passes through outsourcing demineralized water）, energy consumption is saved in this way, and reduces cost；It solves the problems, such as warming, goes to heat with the existing energy of device；It is simple and practical in structure, small investment.
Description
Technical field
The utility model belongs to chemical production technical field, particularly relates to a kind of recycling dress of steam condensation water
It puts.
Background technology
At present, well known steam condensation water is generally directly discharged to circulating water pool and recirculated water is used as after wind turbine cools down to heat exchange
Device exchanges heat, it is impossible to give full play to the effect of steam.
Invention content
The utility model is exactly to overcome the problems, such as that existing steam energy cannot play one's part to the full, and provides a kind of steaming
The recycle device of vapor condensed water.
To achieve the above object, the utility model adopts the following technical solution.
A kind of recycle device of steam condensation water of the utility model, including condensate water pot, condensate pump, feature exists
In：Indirect steam is connected separately on the condensate water pot to steam to concentration tower heating pipeline, cut light tower feed preheater
Vapour return piping, cut light tower feed preheater steam lead line, water stripping water return tank pipeline, condensate pump reflux pipeline,
Main steam header road return piping, condensate pump outlet line, the indirect steam are connected to concentration tower heating pipeline by valve
To condensate water pot, the cut light tower feed preheater steam return pipeline is connected to condensate water pot by valve, described de-
Lights column feed preheater steam lead line is connected to condensate water pot by valve, and the water stripping water return tank pipeline passes through valve
Door is connected to condensate water pot, and the condensate pump reflux pipeline is connected to condensate water pot by valve, and the main steam header road returns
Water pipeline is connected to condensate water pot by valve, and the condensate pump outlet line is connected to condensate water pot by valve；It is described
Condensate pump outlet line is connected to condensate pump by valve, and the condensate pump is connected to condensate pump by valve and flows back
Pipeline, the condensate pump reflux pipeline are connected with main steam header road return piping.
As a kind of preferred embodiment of the utility model, also connected on the condensate pump reflux pipeline by valve branch
There is device area technique water pipeline.
As another preferred embodiment of the utility model, described device area technique water pipeline is connected with by valve to be adopted
Heating coil line.
It is described that heating line is gone to be connect by valve with heat-exchange unit A as another preferred embodiment of the utility model,
Heat-exchange unit A is connect by valve with heat-exchange unit B；Heat-exchange unit B is connect by valve with heat-exchange unit B discharging pipelines, is changed
Hot B of Unit discharging pipeline is pumped out expects pipe line with heat exchange by valve and is connect by valve and heat exchange pump connection, heat exchange pump.
As another preferred embodiment of the utility model, the cut light tower feed preheater steam lead line takes off
Lights column feed preheater steam return pipeline is connected to dehydrogenation component tower feed exchanger by valve respectively.
The beneficial effects of the utility model.
1st, the utility model solves the problems, such as process water in device（Original device passes through outsourcing demineralized water）, save in this way
Energy consumption, and reduce cost.
2nd, the utility model solves the problems, such as warming, goes to heat with the existing energy of device.
3rd, the utility model is simple and practical in structure, small investment, can give full play to the energy of steam, and reduces and be produced into
This.
Description of the drawings
The technical issues of in order to solve the utility model, technical solution and advantageous effect are more clearly understood, below
With reference to the drawings and the specific embodiments, the present invention is further described in detail.It should be appreciated that tool described herein
Body embodiment is only used to explain the utility model, is not used to limit the utility model.
Fig. 1 is a kind of overall structure diagram of the recycle device of steam condensation water of the utility model.
It is marked in figure：1 be cut light tower feed preheater steam lead line, 2 be cut light tower feed preheater steam
Vapour return piping, 3 be indirect steam to concentration tower heating pipeline, 4 are water stripping water return tank pipeline, and 5 be condensate pump return duct
Line, 6 be main steam header road return piping, 7 be condensate pump outlet line, 8 be device area technique water pipeline, 9 to go heating pipe
Line, 10 be condensate water pot, 11 be condensate pump, 12 be heat-exchange unit A, 13 be heat-exchange unit B, 14 be heat-exchange unit B discharge nozzles
Line, 15 be heat exchange pump, 16 be that heat exchange pumps out expects pipe line, 17 is dehydrogenation component tower feed exchanger.
Specific embodiment
With reference to shown in attached drawing, a kind of recycle device of steam condensation water of the utility model, it is characterised in that：Including condensation
Water pot 10, condensate pump 11, it is characterised in that：Indirect steam is connected separately on the condensate water pot 10 to heat to concentration tower
Pipeline 3, cut light tower feed preheater steam return pipeline 2, cut light tower feed preheater steam lead line 1, stripping
Water water return tank pipeline 4, condensate pump reflux pipeline 5, main steam header road return piping 6, condensate pump outlet line 7, described two
Secondary steam is connected to condensate water pot 10, the cut light tower feed preheater steam to concentration tower heating pipeline 3 by valve
Return piping 2 is connected to condensate water pot 10 by valve, and the cut light tower feed preheater steam lead line 1 passes through valve
Condensate water pot 10 is connected to, the water stripping water return tank pipeline 4 is connected to condensate water pot 10, the condensed water blowback by valve
Flow tube line 5 is connected to condensate water pot 10 by valve, and main steam header road return piping 6 is connected to condensate water pot by valve
10, the condensate pump outlet line 7 is connected to condensate water pot 10 by valve；The condensate pump outlet line 7 passes through valve
Door is connected to condensate pump 11, and the condensate pump 11 is connected to condensate pump reflux pipeline 5, the condensate pump by valve
Reflux pipeline 5 is connected with main steam header road return piping 6.
As a kind of preferred embodiment of the utility model, also connected on the condensate pump reflux pipeline 5 by valve branch
It is connected to device area technique water pipeline 8.
As another preferred embodiment of the utility model, described device area technique water pipeline 8 is connected with by valve
Heating line 9.
It is described that heating line 9 is gone to connect by valve and heat-exchange unit A12 as another preferred embodiment of the utility model
It connects, heat-exchange unit A12 is connect by valve with heat-exchange unit B13；Heat-exchange unit B13 passes through valve and heat-exchange unit B discharge nozzles
Line 14 connects, and heat-exchange unit B discharging pipelines 14 are connect by valve with heat exchange pump 15, and heat exchange pump 15 is pumped out by valve and heat exchange
Expects pipe line 16 connects.
As another preferred embodiment of the utility model, the cut light tower feed preheater steam lead line 1 takes off
Lights column feed preheater steam return pipeline 2 is connected to dehydrogenation component tower feed exchanger 17 by valve respectively.
In Fig. 1, condensate water pot 10 is mainly received from main steam header road return piping 6 and water stripping water return tank pipeline
4 collect steam condensation water, and cut light tower feed preheater steam return pipeline 2 is secondary recovery；Then it is steamed in condensate water pot 10
For vapour then by cut light tower feed preheater steam lead line 1, indirect steam provides energy to concentration tower heating pipeline 3 to it
Source；Water in condensate water pot 10 is connected to by condensate pump outlet line 7, condensate pump 11 and condensate pump reflux pipeline 5
Reflux is formed together；Device area technique water pipeline 8 goes heating line 9 to be connected to condensate pump reflux pipeline 5, removes heating line 9
It is connect by valve with heat-exchange unit A12, heat-exchange unit A12 is connect by valve with heat-exchange unit B13；Heat-exchange unit B13 leads to
It crosses valve to connect with heat-exchange unit B discharging pipelines 14, heat-exchange unit B discharging pipelines 14 are connect by valve with heat exchange pump 15, are changed
Heat pump 15 pumps out expects pipe line 16 with heat exchange by valve and connect.
It is understood that above with respect to the specific descriptions of the utility model, it is merely to illustrate the utility model and is not
The described technical solution of the utility model embodiment is limited to, it will be understood by those of ordinary skill in the art that, it still can be with
It modifies to the utility model or equivalent replacement, to reach identical technique effect；As long as meet using needs, all in this reality
Within novel protection domain.
Claims (5)
1. a kind of recycle device of steam condensation water, including condensate water pot（10）, condensate pump（11）, it is characterised in that：Institute
The condensate water pot stated（10）On be connected separately with indirect steam give concentration tower heating pipeline（3）, cut light tower feed preheater
Steam return pipeline（2）, cut light tower feed preheater steam lead line（1）, water stripping water return tank pipeline（4）, condensed water
Pump return line（5）, main steam header road return piping（6）, condensate pump outlet line（7）, the indirect steam is to concentration tower
Heat pipeline（3）Condensate water pot is connected to by valve（10）, the cut light tower feed preheater steam return pipeline（2）
Condensate water pot is connected to by valve（10）, the cut light tower feed preheater steam lead line（1）It is connected by valve
To condensate water pot（10）, the water stripping water return tank pipeline（4）Condensate water pot is connected to by valve（10）, the condensate pump
Reflux pipeline（5）Condensate water pot is connected to by valve（10）, main steam header road return piping（6）It is connected to by valve
Condensate water pot（10）, the condensate pump outlet line（5）Condensate water pot is connected to by valve（10）；The condensed water pumps out
Mouth pipeline（7）Condensate pump is connected to by valve（11）, the condensate pump（11）Condensed water blowback is connected to by valve
Flow tube line（5）, the condensate pump reflux pipeline（5）With main steam header road return piping（6）It is connected.
2. a kind of recycle device of steam condensation water according to claim 1, it is characterised in that：The condensed water blowback
Flow tube line（5）On device area technique water pipeline is also connected with by valve branch（8）.
3. a kind of recycle device of steam condensation water according to claim 2, it is characterised in that：Described device area technique
Water pipeline（8）Heating line is connected with by valve（9）.
4. a kind of recycle device of steam condensation water according to claim 3, it is characterised in that：It is described to remove heating line
（9）Pass through valve and heat-exchange unit A（12）Connection, heat-exchange unit A（12）Pass through valve and heat-exchange unit B（13）Connection；Heat exchange
B of Unit（13）Pass through valve and heat-exchange unit B discharging pipelines（14）Connection, heat-exchange unit B discharging pipelines（14）By valve with
Heat exchange pump（15）Connection, heat exchange pump（15）Expects pipe line is pumped out by valve and heat exchange（16）Connection.
5. a kind of recycle device of steam condensation water according to claim 1, it is characterised in that：The cut light tower
Feed preheater steam lead line（1）, cut light tower feed preheater steam return pipeline（2）It is connected to respectively by valve
Dehydrogenation component tower feed exchanger（17）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721531679.2U CN207472100U (en) | 2017-11-16 | 2017-11-16 | A kind of recycle device of steam condensation water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721531679.2U CN207472100U (en) | 2017-11-16 | 2017-11-16 | A kind of recycle device of steam condensation water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207472100U true CN207472100U (en) | 2018-06-08 |
Family
ID=62260966
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721531679.2U Expired - Fee Related CN207472100U (en) | 2017-11-16 | 2017-11-16 | A kind of recycle device of steam condensation water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207472100U (en) |
-
2017
- 2017-11-16 CN CN201721531679.2U patent/CN207472100U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 124000 fine chemical (plastic) industry zone, Panjin, Liaoning Patentee after: Liaoning Haide New Chemical Group Co.,Ltd. Address before: 124010 Hongqi Street, Shuangtaizi District, Panjin, Liaoning Patentee before: LIAONING HAIDEXIN CHEMICAL Co.,Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180608 |