CN204610064U - High temperature jacket water surplus heat treatment system - Google Patents
High temperature jacket water surplus heat treatment system Download PDFInfo
- Publication number
- CN204610064U CN204610064U CN201520128142.6U CN201520128142U CN204610064U CN 204610064 U CN204610064 U CN 204610064U CN 201520128142 U CN201520128142 U CN 201520128142U CN 204610064 U CN204610064 U CN 204610064U
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- Prior art keywords
- high temperature
- jacket water
- heat
- heat exchanger
- temperature jacket
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of high temperature jacket water surplus heat treatment system, comprise residual heat using device, heat exchanger and large-scale sink, the entrance of described residual heat using device, heat exchanger and large-scale sink is respectively by the pipeline connection of switch and high temperature jacket water, described heat exchanger exports heating load, described large-scale sink heat radiation is to air, the outlet of described residual heat using device is communicated with the entrance of described heat exchanger with large-scale sink respectively, and the outlet of described heat exchanger is also communicated with the entrance of described large-scale sink.Carry out using energy source and heat radiation by residual heat using device, heat exchanger and large-scale sink to high temperature jacket water in the utility model, device is few, fabricating cost is low; And the outlet of residual heat using device is communicated with the entrance of heat exchanger with large-scale sink respectively, the outlet of heat exchanger is communicated with the entrance of large-scale sink, conveniently switches according to different demand and season, thus effectively utilizes the heat energy of high temperature jacket water.
Description
Technical field
The utility model relates to high temperature jacket water surplus heat treatment system, especially relevant with the recycling structure of the high temperature jacket water waste heat of combustion gas internal-combustion engine unit.
Background technique
Combustion gas internal-combustion engine unit is fuel with rock gas, and drive electrical generators generates electricity.Combustion gas internal-combustion engine unit produces a large amount of high temperature jacket waters and low temperature jacket water in running, low temperature jacket water carries out radiating treatment usually, high temperature jacket water is contained a large amount of heat energy, dispel the heat if can not be used and drain, can cause a large amount of energy wastes, and radiation processes own is also very complicated.Some utilizes the system of this high temperature jacket water at present, and structure is very complicated, and fabricating cost own is very high, and be difficult to need to switch according to the difference of Various Seasonal, cause the non-constant of validity of high temperature jacket water heat energy utilization, cost is very high, and Economy is bad.
Model utility content
For problems of the prior art, the purpose of this utility model effectively can either utilize high temperature jacket water heat energy for providing one, can reduce overall system architecture complexity again thus the high temperature jacket water surplus heat treatment system reduced costs.
For achieving the above object, the technical solution of the utility model is as follows:
A kind of high temperature jacket water surplus heat treatment system, comprise residual heat using device, heat exchanger and large-scale sink, the entrance of described residual heat using device, heat exchanger and large-scale sink is respectively by the pipeline connection of switch and high temperature jacket water, described heat exchanger exports heating load, described large-scale sink heat radiation is to air, the outlet of described residual heat using device is communicated with the entrance of described heat exchanger with large-scale sink respectively, and the outlet of described heat exchanger is also communicated with the entrance of described large-scale sink.
Preferably, described residual heat using device is residual heat type lithium bromide chiller.
Preferably, described heat exchanger is plate type heat exchanger.
Preferably, described large-scale sink is cooling tower.
Preferably, described system also includes the first three-way valve and the second three-way valve, first port of described first three-way valve is communicated with described high temperature jacket water, second port is communicated with described large-scale sink, third connectivity mouth is communicated with described second three-way valve, 4th port of described second three-way valve is communicated with described first three-way valve, and five-way mouth is communicated with described residual heat using device, and the 6th port is communicated with described heat exchanger.
Preferably, the passage that described residual heat using device is communicated with described heat exchanger and large-scale sink is respectively arranged with the first valve and the second valve.
Preferably, the passage that described heat exchanger is communicated with described large-scale sink is provided with the 3rd valve.
Preferably, described high temperature jacket water results from combustion gas explosive motor.
Preferably, described combustion gas explosive motor is in transmission connection generator, described generator output power.
Preferably, the low temperature jacket water of described combustion gas explosive motor is communicated to low temperature radiation water tank, and described low temperature radiation heat dissipation of water tank is to air.
The beneficial effects of the utility model are, compared with prior art, carry out using energy source and heat radiation by residual heat using device, heat exchanger and large-scale sink to high temperature jacket water in the utility model, device is few, fabricating cost is low for the utility model; And the outlet of residual heat using device is communicated with the entrance of heat exchanger with large-scale sink respectively, the outlet of heat exchanger is communicated with the entrance of large-scale sink, conveniently switches according to different demand and season, thus effectively utilizes the heat energy of high temperature jacket water.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in further detail:
Fig. 1 is the structural representation of a preferred embodiment of the utility model high temperature jacket water surplus heat treatment system.
Embodiment
The exemplary embodiments embodying the utility model feature & benefits will describe in detail in the following description.Be understood that the utility model can have various changes in different embodiments, it neither departs from scope of the present utility model, and explanation wherein and accompanying drawing are the use when explain in itself, and is not used to limit the utility model.
High temperature jacket water surplus heat treatment system of the present utility model, comprise residual heat using device, heat exchanger and large-scale sink, the entrance of residual heat using device, heat exchanger and large-scale sink is respectively by the pipeline connection of switch and high temperature jacket water, heat exchanger exports heating load, large-scale sink heat radiation is to air, the outlet of residual heat using device is communicated with the entrance of heat exchanger with large-scale sink respectively, and the outlet of heat exchanger is also communicated with the entrance of large-scale sink.Carry out using energy source and heat radiation by residual heat using device, heat exchanger and large-scale sink to high temperature jacket water in the utility model, device is few, fabricating cost is low; And the outlet of residual heat using device is communicated with the entrance of heat exchanger with large-scale sink respectively, the outlet of heat exchanger is communicated with the entrance of large-scale sink, conveniently switches according to different demand and season, thus effectively utilizes the heat energy of high temperature jacket water.Concrete structure of the present utility model, application are not limited, as long as above-mentioned acting on can be realized, but following for illustrating feature of the present utility model, carry out expansion explanation with the structure of a preferred embodiment.
As shown in Figure 1, be the structural representation of this preferred embodiment.In the preferred embodiment, the occasion that combustion gas internal-combustion engine unit 4 carries out generating electricity is applied in.In this preferred embodiment, combustion gas internal-combustion engine unit 4 inputs fuel Q, and drive electrical generators 5 action, to produce electric power D, and this electric power D is transported in power equipment and electric power system 12.In combustion gas internal-combustion engine unit 4 working procedure, produce high temperature jacket water GS and low temperature jacket water DS, low temperature jacket water DS enters low temperature radiation water tank 6, wherein will spill into air 16 by heat.
High temperature jacket water GS shunts through the first three-way valve 7, and a part directly enters in large-scale sink 3, and another part enters the second three-way valve 8.In this preferred embodiment, this large-scale sink 3 is cooling tower, and heat is spilt into air 16 through this cooling tower 3 by high temperature jacket water GS.The high temperature jacket water GS entering the second three-way valve 8 shunts again, and a part enters residual heat using device 1, and another part enters heat exchanger 2.In this preferred embodiment, residual heat using device 1 is residual heat type lithium bromide chiller, heat exchanger 2 is plate type heat exchanger, the high temperature jacket water GS entering residual heat type lithium bromide chiller 1 recycles, the high temperature jacket water GS entering plate type heat exchanger 2 produces heat load, and this heat load is delivered in HVAC system 15.Selected by the switch of the first three-way valve 7 and the second three-way valve 8, can need switch each water route of high temperature jacket water GS and regulate the ratio of the water yield in each water route of high temperature jacket water GS according to difference.
In this preferred embodiment, residual heat type lithium bromide chiller 1 is communicated with plate type heat exchanger 2 by the first valve 9, is communicated with cooling tower 3 by the second valve 10.Jacket water after residual heat type lithium bromide chiller 1 is recycled can be delivered to cooling tower 3 and cool, and also can be delivered in plate type heat exchanger 2 and again utilize, to produce heat load.In addition, in this preferred embodiment, plate type heat exchanger 2 is also communicated with cooling tower 3 by the 3rd valve 11.Change heat treated jacket water through plate type heat exchanger 2, can also be delivered in cooling tower 3 and dispel the heat.This structure can realize the heat radiation to plate type heat exchanger 2, especially in summer, avoids high temperature jacket water GS directly to discharge, and can reduce and arrange emergent high-temperature heat radiation device.
The embody rule of this preferred embodiment comprises in parallel and series connection two kinds of application, wherein application in parallel is as described below: during summer, high temperature jacket water GS preferentially enters residual heat type lithium bromide chiller 1 and carries out cycle heat exchange utilization, a part of cold water can be produced by residual heat type lithium bromide chiller 1 heat exchange, also can produce a part of unavailable hot water, unavailable hot water carries out cycle heat exchange by heat dissipation in air 16 by cooling tower 3 simultaneously.During winter, if residual heat type lithium bromide chiller 1 cannot use and need to dispel the heat to high temperature jacket water GS, then high temperature jacket water GS is delivered in plate type heat exchanger 2 and carries out cycle heat exchange, the heat that plate type heat exchanger 2 obtains is discharged in air by cooling tower 3, producing heat load after heat exchange exports in HVAC system 15, if do not need heat load to export, then heat-exchanging water is delivered to cooling tower 3 and cools.
Series connection application is as described below: no matter winter in summer, high temperature jacket water GS preferentially enters residual heat type lithium bromide chiller 1, from residual heat type lithium bromide chiller 1 out after unavailable hot water enter again plate type heat exchanger 2 heat exchange produce heat load export, dispelled the heat through cooling tower 3 again by the unavailable hot water after plate type heat exchanger 2 heat exchange.In addition, whether this preferred embodiment meets the requirement of combustion gas internal-combustion engine unit to temperature according to the return water temperature of high temperature jacket water GS in running regulates, when in the residual heat type lithium bromide chiller 1 that high temperature jacket water GS circulates, plate type heat exchanger 2 and cooling tower 3, either phase meets the demands, bypass is carried out by three-way valve, high temperature jacket water GS is avoided to enter other stages again, but direct recycling water utilization.
In this preferred embodiment, by the parallel connection of residual heat type lithium bromide chiller 1, plate type heat exchanger 2 and cooling tower 3, connect arranged in a crossed manner, while minimizing device, realize the repeatedly utilization of high temperature jacket water GS and multistage heat radiation, thus realize effective utilization of the energy, the Economy of application is very high, is suitable for promoting the use of.
The technical solution of the utility model is disclosed as above by preferred embodiment.The change that those skilled in the art do when should recognize the scope and spirit of the present utility model disclosed in the claim do not departed from appended by the utility model and retouching, within the protection domain all belonging to claim of the present utility model.
Claims (10)
1. a high temperature jacket water surplus heat treatment system, it is characterized in that, comprise residual heat using device, heat exchanger and large-scale sink, the entrance of described residual heat using device, heat exchanger and large-scale sink is respectively by the pipeline connection of switch and high temperature jacket water, described heat exchanger exports heating load, described large-scale sink heat radiation is to air, the outlet of described residual heat using device is communicated with the entrance of described heat exchanger with large-scale sink respectively, and the outlet of described heat exchanger is also communicated with the entrance of described large-scale sink.
2. high temperature jacket water surplus heat treatment system as claimed in claim 1, it is characterized in that, described residual heat using device is residual heat type lithium bromide chiller.
3. high temperature jacket water surplus heat treatment system as claimed in claim 1, it is characterized in that, described heat exchanger is plate type heat exchanger.
4. high temperature jacket water surplus heat treatment system as claimed in claim 1, it is characterized in that, described large-scale sink is cooling tower.
5. high temperature jacket water surplus heat treatment system as claimed in claim 1, it is characterized in that, described system also includes the first three-way valve and the second three-way valve, first port of described first three-way valve is communicated with described high temperature jacket water, second port is communicated with described large-scale sink, and third connectivity mouth is communicated with described second three-way valve, and the 4th port of described second three-way valve is communicated with described first three-way valve, five-way mouth is communicated with described residual heat using device, and the 6th port is communicated with described heat exchanger.
6. high temperature jacket water surplus heat treatment system as claimed in claim 5, is characterized in that, the passage that described residual heat using device is communicated with described heat exchanger and large-scale sink is respectively arranged with the first valve and the second valve.
7. high temperature jacket water surplus heat treatment system as claimed in claim 5, is characterized in that, the passage of the described large-scale sink of described heat exchanger connection is provided with the 3rd valve.
8. the high temperature jacket water surplus heat treatment system as described in as arbitrary in claim 1-7, it is characterized in that, described high temperature jacket water results from combustion gas explosive motor.
9. high temperature jacket water surplus heat treatment system as claimed in claim 8, is characterized in that, described combustion gas explosive motor is in transmission connection generator, described generator output power.
10. high temperature jacket water surplus heat treatment system as claimed in claim 9, it is characterized in that, the low temperature jacket water of described combustion gas explosive motor is communicated to low temperature radiation water tank, and described low temperature radiation heat dissipation of water tank is to air.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520128142.6U CN204610064U (en) | 2015-03-05 | 2015-03-05 | High temperature jacket water surplus heat treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520128142.6U CN204610064U (en) | 2015-03-05 | 2015-03-05 | High temperature jacket water surplus heat treatment system |
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| CN204610064U true CN204610064U (en) | 2015-09-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520128142.6U Expired - Fee Related CN204610064U (en) | 2015-03-05 | 2015-03-05 | High temperature jacket water surplus heat treatment system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113865142A (en) * | 2021-08-23 | 2021-12-31 | 深圳市燃气集团股份有限公司 | Skid-mounted efficient refrigerating device |
-
2015
- 2015-03-05 CN CN201520128142.6U patent/CN204610064U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113865142A (en) * | 2021-08-23 | 2021-12-31 | 深圳市燃气集团股份有限公司 | Skid-mounted efficient refrigerating device |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhang Yue Inventor before: Zhang Xiaodong Inventor before: Ma Junfeng |
|
| CB03 | Change of inventor or designer information | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150902 Termination date: 20210305 |
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| CF01 | Termination of patent right due to non-payment of annual fee |