CN208475297U - A kind of industry flash steam thermal energy recycling circulation recycling system - Google Patents
A kind of industry flash steam thermal energy recycling circulation recycling system Download PDFInfo
- Publication number
- CN208475297U CN208475297U CN201820794891.6U CN201820794891U CN208475297U CN 208475297 U CN208475297 U CN 208475297U CN 201820794891 U CN201820794891 U CN 201820794891U CN 208475297 U CN208475297 U CN 208475297U
- Authority
- CN
- China
- Prior art keywords
- water
- steam
- condensed water
- low temperature
- temperature steam
- 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
Links
- 238000004064 recycling Methods 0.000 title claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 91
- 238000000034 method Methods 0.000 claims abstract description 20
- 230000006835 compression Effects 0.000 claims abstract description 11
- 238000007906 compression Methods 0.000 claims abstract description 11
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 41
- 230000003020 moisturizing effect Effects 0.000 claims description 7
- 238000010025 steaming Methods 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 3
- 239000002918 waste heat Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000008929 regeneration Effects 0.000 abstract 2
- 238000011069 regeneration method Methods 0.000 abstract 2
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000005265 energy consumption Methods 0.000 abstract 1
- 239000013589 supplement Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 description 3
- 230000001351 cycling effect Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
Landscapes
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
A kind of industrial flash steam thermal energy of the utility model recycles circulation recycling system, the system includes the industrial equipment using steam for heat source production technology, the waste heat flash steam containing condensed water that Low Temperature Steam compressor discharges production process equipment carries out compression temperature raising and the water of heat exchanger carries out heat exchange acquisition secondary recycling Low Temperature Steam, low-temp recovery both vapor compression is the regeneration high-temp steam of manufacturing technique requirent under the action of high-temperature steam compression machine by secondary recycling Low Temperature Steam, and regeneration high-temp steam insufficient section meets system needs by a high-temperature steam supplement；Low Temperature Steam after Low Temperature Steam compressor compresses is used by that can supply boiler with the condensed water generated after a hydrothermal exchange, can also be added to a water back warp heat exchange and be generated secondary recycling Low Temperature Steam.The present invention solves the problems, such as that prior art technology can not recycle flash steam circulation and stress, and energy conservation and consumption reduction effects are significant, can effectively reduce production cost.
Description
Technical field
The industrial flash steam thermal energy of the utility model recycles circulation recycling system category industrial energy saving technical field.
Background technique
, with the fast development of China's industrialization degree in recent years, steam is many with the best in quality of it, clean and environmental protection
Industry is widely used as heating energy source.When using steam as indirect heating, extra steam is with flash steam and condensed water
Mode is discharged, and heat recovery technology is varied at present, but the heat recycled is confined to provide industry, life or north of china in winter confession
Warm hot water can not digest a large amount of return since demand of many industrial enterprises to industry, life or heating hot water is limited
The thermal energy of receipts, can be lower because of the temperature and pressure of steam the initial steam generated using heat pump techniques recycling, can not be with one
Secondary high temperature and high pressure steam mixing is produced and used for system process, and a large amount of flash steam recycling cycling and reutilization is had become industry
Technical staff's urgent problem to be solved, the recycling of flash steam not only conform to the industry energy saving policy of country, significantly reduce enterprise
Production cost, more saved the energy that increasingly deficient water resource and day are becoming tight.
Summary of the invention
The utility model is directed to the deficiencies in the prior art, proposes that a kind of industrial flash steam thermal energy recycling circulation is sharp again
Use system.
Purpose of the utility model is realized as follows: a kind of industry flash steam thermal energy recycles circulation recycling system, until
It less include: the process equipment using high-temperature steam as heat source, flash steam and condensed water discharge pipe, Low Temperature Steam compressor and heat exchange
Device；What is be connected with process equipment is flash steam and condensed water discharge pipe, and the discharge pipe is connect with Low Temperature Steam compressor；Institute
It states heat exchanger and is equipped with Low Temperature Steam inlet end, condensed water water outlet, a water water inlet end, secondary low temperature initial steam outlet side,
The Low Temperature Steam inlet end of the heat exchanger is connected with Low Temperature Steam compressor, heat exchanger condensed water water outlet with
Condensed water water tank is connected, and a water water inlet end of the heat exchanger is connected with a water inlet pipe, the heat exchanger
Secondary low temperature initial steam outlet side and high-temperature steam compression machine be connected；The high-temperature steam compression machine and a high-temperature steam
Pipeline is connected；The condensed water water tank is connected with two groups of condensed water water-delivery pumps, two groups of condensed water water-delivery pumps its
In one group by condensed water be transported to boiler carry out moisturizing, condensed water is transported to an aqueduct and enters heat exchanger by another group
Heat exchange is carried out as moisturizing.
Further, the vapour compression machine is reciprocating compressor, centrifugal or Roots blower.
Further, the condensed water savings water pot is connected with valve, water pump and condensed water water-supply-pipe, by condensed water
It is transported to boiler and is used as moisturizing.
Further, the condensed water savings water pot is connected with valve, water pump, condensed water water-supply-pipe and threeway, will
Condensed water makees moisturizing to heat exchanger progress heat exchange by a water water inlet pipe and generates new steam.
Further, a water of a water water inlet pipe and a water water-delivery pump, valve and pipeline and heat exchanger
Water inlet end is connected.
Further, the condensed water water tank is normal pressure water tank or normal pressure reservoir.
The utility model industrial flash steam thermal energy recycling circulation recycling system new technology, can to greatest extent by
All types of industries process system waste heat flash steam and condensed water adequately carry out recycling cycling and reutilization, and heat reclaiming system technique is matched
It sets simply, equipment investment is small, and recovery efficiency is high, can significantly reduce user's production cost.
Detailed description of the invention: Fig. 1 is that a kind of industrial flash steam thermal energy of the utility model recycles the signal of circulation recycling system
Figure.
Legend: 1. Low Temperature Steam compressor, 2. high-temperature steam compresses 3. heat exchanger of machine, 4. condensed water water tank, 5. valve
6. valve of door, 7. threeway, 8. flash steam and condensed water conveying 9. Low Temperature Steam escape pipe of discharge pipe, 10. water inlet pipe 11. are cold
Condensate boiler replenishing water pumps 12. condensed water water-delivery pump, 13. valve, 14. condensed water outlet pipe, 15. 2 low temperature initial steam outlets
18. water water inlet pipes of pipe 16. high temperature steam pipes, 17. condensed water water-supply-pipe, 19. boiler replenishing water water-supply-pipe 20. 2
23. water water-delivery pumps of secondary high temperature initial steam pipe 21. threeway, 22. process equipment, 24. Low Temperature Steam inlet end 25. is primary
26. 2 low temperature initial steam outlet sides of water water inlet end, 27. condensed water water outlet, 28. condensed water water tank water inlet ends 29. are cold
30. condensed water water tank water outlet of condensate water tank water outlet.
Specific embodiment: the present invention is not limited by the following examples, can according to the technique and scheme of the present invention with reality
Situation determines specific embodiment.
Refering to attached drawing.This specification structure depicted in this specification institute accompanying drawings, ratio, size etc., only to cooperate specification
Revealed content is not intended to limit the invention enforceable limit for being familiar with professional person's understanding of this technology and reading
Fixed condition, therefore do not have technical essential meaning, the modification of any structure, the adjustment of proportionate relationship or the change of size,
In the case where not influencing the attainable purpose of function and institute that the present invention can be generated, it should all be included in disclosed technology
In the range of content can cover；Simultaneously in this specification it is cited as "upper", "lower", "left", "right", "front", "rear",
The term of " centre ", " side " and " one " etc. is also only being illustrated for narration, rather than is limited the scope of the invention with this,
Its relativeness is altered or modified, under the content of no substantial changes in technology, when should be regarded as the enforceable scope of the present invention.
Embodiment: it as shown in Figure 1, a kind of industry flash steam thermal energy recycles circulation recycling system, includes at least: with high temperature
Steam is the process equipment 22 of heat source, and what is be connected with process equipment 22 is flash steam and condensed water discharge pipe 8, the discharge pipe
8 connect with Low Temperature Steam compressor 1, the Low Temperature Steam inlet end 24 of the heat exchanger 3 through Low Temperature Steam discharge pipe 9 with it is low
Warm vapour compression machine 1 is connected, and a water water inlet end 25 of the heat exchanger 3 is through water inlet pipe 10 and 7 valve 13, one of threeway
Secondary water water-delivery pump 23 and a water water inlet pipe 18 are connected, and the condensed water water outlet 27 of the heat exchanger 3 goes out through condensed water
Water pipe 14 is connected with the condensed water water tank water inlet end 28 of condensed water water tank 4, and the secondary low temperature of the heat exchanger 3 newly steams
Vapour outlet side 26 is connected through secondary low temperature initial steam escape pipe 15 with high-temperature steam compression machine 2, and the high-temperature steam compresses machine 2
It is connected through secondary high-temperature initial steam pipe 20 with the threeway 21 on a high temperature steam pipe 16, a high temperature steam pipe 16
It is connected through threeway 21 with process equipment 22.
The condensed water water tank water outlet 29 of the condensed water water tank 4 is through condensed water water-delivery pump 12, valve 6 and condensation
Water water-supply-pipe 17 is connected with threeway 7.
It is mended through condensed water water-delivery pump 11, valve 5 and boiler the condensed water water tank water outlet 30 of the condensed water water tank 4
Water water-supply-pipe 19 is connected.
In use, condensed water and flash steam that the process equipment 22 of the present embodiment is discharged are through flash steam and condensed water conveying row
Outlet pipe 8 enters Low Temperature Steam compressor 1, and the effect through Low Temperature Steam compressor 1 generates Low Temperature Steam, and Low Temperature Steam is handed over through heat
Parallel operation 3 and the water covered of water inlet pipe 10 or the condensed water of recycling carry out heat exchange, a water or recycling through heat exchange
Condensed water produces new Low Temperature Steam by the secondary low temperature initial steam outlet side 26 of heat exchanger 3 through secondary low temperature initial steam outlet
Pipe 15 enters high-temperature steam and compresses machine 2, and low temperature initial steam generates secondary high-temperature under the action of high-temperature steam compresses machine 2 and newly steams
Vapour, secondary high-temperature initial steam are connected and will be recycled with the threeway 21 on a high temperature steam pipe 16 by secondary high-temperature initial steam pipe 20
Regenerated high-temperature steam inputs process equipment 22, and the compressed Low Temperature Steam of Low Temperature Steam compressor 1 is handed over through 3 heat of heat exchanger
Generated after changing condensed water by heat exchanger 3 condensed water water outlet 27, condensed water outlet pipe 14 is by being discharged into condensed water water tank
Water inlet end 28 enters condensed water water tank 4.
The condensed water of condensed water water tank 4 both can be by condensed water water tank water outlet 29 through condensed water water-delivery pump 12, valve
Door 6 and condensed water water-supply-pipe 17 are connected with the threeway 7 on a water water inlet pipe 18, and condensed water is inputted in heat exchanger 3 and is passed through
Heat exchange generates low temperature initial steam.
The condensed water of condensed water water tank 4 can also be by condensed water water tank water outlet 30 through condensed water water-delivery pump 11, valve
Door 5 is connected with boiler replenishing water water-supply-pipe 19 inputs boiler.
When in use, the secondary high-temperature initial steam described in the utility model generated after high-temperature steam compression machine 2 compresses
Pressure and temperature value it is identical as the high temperature and high pressure steam in a high temperature steam pipe 16, for meeting wanting for process equipment 22
It asks, the quantity of steam insufficient section of secondary high-temperature initial steam is supplemented by a high-temperature steam, mixes supply process equipment through threeway 21
22, meet the normal production of process equipment 22.
Using the utility model technology can by the prior art can not practical application all types of industries flash steam waste heat recycling follow
Ring recycles, and the energy loss of system can be greatly reduced, and will generate far-reaching positive meaning for energy-saving and emission-reduction, protection environment
Justice.
Above-described embodiment only exemplary illustrated the principle of the present invention and process flow, and is not intended to limit the present invention；It is any
Person skilled in the art scholar can modify above-described embodiment or be changed without violating the spirit and scope of the present invention
Become.Therefore, as long as thinking without departing from disclosed spirit with technology in technical field with this field skill
Think lower completed all equivalent modifications or change, should be covered by the claims of the present invention.
Claims (6)
1. a kind of industry flash steam thermal energy recycles circulation recycling system, includes at least: being set by the technique of heat source of high-temperature steam
It is standby, flash steam and condensed water discharge pipe, Low Temperature Steam compressor and heat exchanger；Be connected with process equipment be flash steam and
Condensed water discharge pipe, the discharge pipe are connect with Low Temperature Steam compressor；The heat exchanger is equipped with Low Temperature Steam inlet end, cold
Condensate water outlet, a water water inlet end, secondary low temperature initial steam outlet side, the Low Temperature Steam inlet end of the heat exchanger with it is low
Warm vapour compression machine is connected, and heat exchanger condensed water water outlet is connected with condensed water water tank, the heat exchanger
A water water inlet end be connected with a water inlet pipe, the secondary low temperature initial steam outlet side of the heat exchanger and high-temperature steam
Compressor is connected；The high-temperature steam compression machine is connected with a high temperature steam pipeline；The condensed water water tank and two
Group condensed water water-delivery pump is connected, two groups of condensed water water-delivery pumps wherein one group condensed water be transported to boiler mend
Water, condensed water is transported to an aqueduct and enters heat exchanger as moisturizing progress heat exchange by another group.
2. a kind of industrial flash steam thermal energy as described in claim 1 recycles circulation recycling system, which is characterized in that the steaming
Vapour compressor is reciprocating compressor, centrifugal or Roots blower.
3. a kind of industrial flash steam thermal energy as described in claim 1 recycles circulation recycling system, which is characterized in that described cold
Condensate savings water pot is connected with valve, water pump and condensed water water-supply-pipe, and condensed water is transported to boiler and is used as moisturizing.
4. a kind of industrial flash steam thermal energy as described in claim 1 recycles circulation recycling system, which is characterized in that described cold
Condensate savings water pot is connected with valve, water pump, condensed water water-supply-pipe and threeway, and condensed water is made by a water water inlet pipe
Moisturizing to heat exchanger carries out heat exchange and generates new steam.
5. a kind of industrial flash steam thermal energy as described in claim 1 recycles circulation recycling system, which is characterized in that described one
Secondary water water inlet pipe is connected with a water water-delivery pump, valve and pipeline with a water water inlet end of heat exchanger.
6. a kind of industrial flash steam thermal energy as described in claim 1 recycles circulation recycling system, which is characterized in that described cold
Condensate water tank is normal pressure water tank or normal pressure reservoir.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820794891.6U CN208475297U (en) | 2018-05-21 | 2018-05-21 | A kind of industry flash steam thermal energy recycling circulation recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820794891.6U CN208475297U (en) | 2018-05-21 | 2018-05-21 | A kind of industry flash steam thermal energy recycling circulation recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208475297U true CN208475297U (en) | 2019-02-05 |
Family
ID=65218882
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820794891.6U Expired - Fee Related CN208475297U (en) | 2018-05-21 | 2018-05-21 | A kind of industry flash steam thermal energy recycling circulation recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208475297U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112963823A (en) * | 2021-03-31 | 2021-06-15 | 成都三山粮油有限公司 | Steam heat recovery system |
-
2018
- 2018-05-21 CN CN201820794891.6U patent/CN208475297U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112963823A (en) * | 2021-03-31 | 2021-06-15 | 成都三山粮油有限公司 | Steam heat recovery system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202419765U (en) | Circulating water cooling heating apparatus of turbine condenser in thermal power plant | |
| CN208222621U (en) | A kind of steam exhaust heat recovery utilization system based on steam jet heat pump | |
| CN105444247A (en) | Regional energy supply system based on comprehensive recycle of various low-grade waste heat | |
| CN206439810U (en) | A kind of hydrophobic development unit dead steam recovery system | |
| CN105570861A (en) | Energy cascade utilization device and method for extraction steam heating system | |
| CN103383106A (en) | Steam recycling system | |
| CN110864274B (en) | Hot water recycling system for flue gas waste heat recovery | |
| CN105737235A (en) | Waste heat recovery system and method | |
| CN208475297U (en) | A kind of industry flash steam thermal energy recycling circulation recycling system | |
| CN207688430U (en) | A kind of residual heat of air compressor recycling central hot-water system of solar air source auxiliary | |
| CN102192555A (en) | Air compressor waste heat recovery and utilization system | |
| CN205591974U (en) | Regional energy supply system based on multiple low -grade waste heat comprehensive recovery utilization | |
| CN205535722U (en) | A energy cascade utilization device for drawing gas heating system | |
| CN205065867U (en) | Indirect air cooling unit steam turbine steam exhaust waste heat recovery is used for heat supply network circulation water heating system | |
| CN203080282U (en) | Grade heat exchange draining and water-wind sensible heat gradient utilization return-air-free loosening heat setting machine | |
| CN201903219U (en) | Hot Wastewater Reuse System | |
| CN205477791U (en) | Low -grade waste heat energy supply system of industry | |
| CN215489985U (en) | High-parameter heating system based on energy level matching | |
| CN110108144A (en) | A kind of bigeminy waste heat recovery of circulatory system | |
| CN215336248U (en) | High-efficiency energy-saving steam regeneration system | |
| CN211739051U (en) | Hot water recirculation system for flue gas waste heat recovery | |
| CN205156097U (en) | Novel recirculated cooling water water supply system | |
| CN203489249U (en) | Steam recycling system | |
| CN206386911U (en) | A kind of chemical water heating system | |
| CN208702473U (en) | Closed-up water back heating system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190205 Termination date: 20200521 |