CN204415698U - LNG Multi-class propagation system on ship - Google Patents
LNG Multi-class propagation system on ship Download PDFInfo
- Publication number
- CN204415698U CN204415698U CN201420714724.8U CN201420714724U CN204415698U CN 204415698 U CN204415698 U CN 204415698U CN 201420714724 U CN201420714724 U CN 201420714724U CN 204415698 U CN204415698 U CN 204415698U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- lng
- electrical generator
- pipeline
- turbine expansion
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- 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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- 239000000446 fuel Substances 0.000 claims abstract description 30
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000013535 sea water Substances 0.000 claims abstract description 18
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000004134 energy conservation Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000003949 liquefied natural gas Substances 0.000 description 21
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 8
- 239000001294 propane Substances 0.000 description 4
- 238000002309 gasification Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- 230000005611 electricity Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 238000010795 Steam Flooding Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
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- Engine Equipment That Uses Special Cycles (AREA)
Abstract
LNG Multi-class propagation system on ship, comprise dual-fuel diesel, natural fuels turbine expansion electrical generator, first heat exchanger, second heat exchanger, LNG storage tank, cabin evaporator, 3rd heat exchanger, methane turbine expansion electrical generator and sea water pump, described dual-fuel diesel connects the generating of natural fuels turbo-expander successively by pipeline, first heat exchanger, second heat exchanger and LNG storage tank, methane turbine expansion electrical generator connects the second heat exchanger and the 3rd heat exchanger successively by pipeline, and form closed cycle pipeline, sea water pump and cabin evaporator is connected on the left of 3rd heat exchanger.The utility model has the advantages that: solve the waste of LNG cold energy and the waste problem of dual-fuel diesel exhaust temperature that there is environmental protection, the feature such as energy-conservation, efficient.
Description
Technical field
The utility model relates to LNG Multi-class propagation system on ship, belong to technical field of ships.
Background technology
Natural fuels, as one of three large energy, more and more obtains favor both domestic and external in recent years.And after natural gas liquefaction, the rapid contraction of its volume, to original 1/625, has huge advantage to storage and transport.User is when using natural fuels, and LNG uses after needing gasification.The normal pressure storage temperature of liquefied natural gas (LNG) is 111K(-162 DEG C), gasification rewarming are to about normal temperature 300K(27 DEG C) process by discharging a large amount of cold energy, be about 883 kJ/kg.Propane boiling point is-42.1 DEG C, is applicable to the working medium doing Rankine cycle.The recycling of this part cold energy is significant to raising LNG service efficiency, saving energy resource consumption, and how to realize is a urgent problem at present.
Summary of the invention
The purpose of this utility model is to provide LNG Multi-class propagation system on ship.
Problem to be solved in the utility model is the existing deficiency effectively do not utilized the LNG energy.
For realizing the purpose of this utility model, the technical solution adopted in the utility model is:
LNG Multi-class propagation system on ship, comprise dual-fuel diesel, natural fuels turbine expansion electrical generator, first heat exchanger, second heat exchanger, LNG storage tank, cabin evaporator, 3rd heat exchanger, methane turbine expansion electrical generator and sea water pump, described dual-fuel diesel connects the generating of natural fuels turbo-expander successively by pipeline, first heat exchanger, second heat exchanger and LNG storage tank, methane turbine expansion electrical generator connects the second heat exchanger and the 3rd heat exchanger successively by pipeline, and form closed cycle pipeline, sea water pump and cabin evaporator is connected on the left of 3rd heat exchanger.
The offgas duct of described dual-fuel diesel accesses the first heat exchanger.
In described sea water pump access seawater.
The utility model has the advantages that: the utility model relates to a kind of recycle scheme making liquefied natural gas Multi-class propagation aboard ship, solve the waste of LNG cold energy and the waste problem of dual-fuel diesel exhaust temperature that there is environmental protection, the feature such as energy-conservation, efficient.Its design plan is the principle based on Rankine cycle, and utilize principle to realize its object with energy cycle multistage, cabin cooling decreases the use of air-conditioning, environmental protection, energy-conservation, economical, should have the wide market space.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of LNG Multi-class propagation system on the utility model ship;
In figure: 1, dual-fuel diesel 2, natural fuels turbine expansion electrical generator 3, first heat exchanger 4, second heat exchanger 5, LNG storage tank 6, cabin evaporator 7, the 3rd heat exchanger 8, methane turbine expansion electrical generator 9, sea water pump.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described.
LNG Multi-class propagation system on ship, comprise dual-fuel diesel 1, natural fuels turbine expansion electrical generator 2, first heat exchanger 3, second heat exchanger 4, LNG storage tank 5, cabin evaporator 6, the 3rd heat exchanger 7, methane turbine expansion electrical generator 8 and sea water pump 9, described dual-fuel diesel 1 connects natural fuels turbo-expander generating the 2, first heat exchanger 3, second heat exchanger 4 and LNG storage tank 5 successively by pipeline, realizes the utilization of cold energy; Methane turbine expansion electrical generator 8 connects the second heat exchanger 4 and the 3rd heat exchanger 7 successively by pipeline, and forms closed cycle pipeline, connects sea water pump 9 and cabin evaporator 6 on the left of the 3rd heat exchanger 7.
The offgas duct of described dual-fuel diesel 1 accesses the first heat exchanger 3, realizes the effective utilization to using waste heat from tail gas.
Described sea water pump 9 accesses in seawater, for extracting seawater.
Using method of the present utility model: LNG cold generating flow process, adopting with propane is the Rankine hybrid cycle of working medium and the direct expansion turbine of natural fuels.Propane liquid absorption seawater heat gasifies, and high pressure steam drives methane turbine expansion electrical generator 8, and cooled seawater is used for accessing cabin evaporator 6 and lowers the temperature to cabin.Subsequently in propane second heat exchanger 4 heat release by LNG condensation.Meanwhile, high pressure LNG endothermic gasification, becomes high pressure steam, drives natural fuels turbine expansion electrical generator 2 to generate electricity.By the fuelled with natural gas gasified for boats and ships provide power, using waste heat from tail gas enters the first heat exchanger 3 conversely again to the heated by natural gas gasified, allow its high pressure steam be generated electricity by natural fuels turbine, natural fuels afterwards enters dual-fuel diesel again for boats and ships provides power.Realize the recycle of the energy.
Claims (3)
1. LNG Multi-class propagation system on ship, comprise dual-fuel diesel (1), natural fuels turbine expansion electrical generator (2), first heat exchanger (3), second heat exchanger (4), LNG storage tank (5), cabin evaporator (6), 3rd heat exchanger (7), methane turbine expansion electrical generator (8) and sea water pump (9), described dual-fuel diesel (1) connects natural fuels turbo-expander generating (2) successively by pipeline, first heat exchanger (3), second heat exchanger (4) and LNG storage tank (5), methane turbine expansion electrical generator (8) connects the second heat exchanger (4) and the 3rd heat exchanger (7) successively by pipeline, and form closed cycle pipeline, 3rd heat exchanger (7) left side connects sea water pump (9) and cabin evaporator (6).
2. LNG Multi-class propagation system on ship according to claim 1, is characterized in that: the offgas duct of described dual-fuel diesel (1) accesses the first heat exchanger (3).
3. LNG Multi-class propagation system on ship according to claim 1, is characterized in that: in described sea water pump (9) access seawater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420714724.8U CN204415698U (en) | 2014-11-25 | 2014-11-25 | LNG Multi-class propagation system on ship |
Applications Claiming Priority (1)
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CN201420714724.8U CN204415698U (en) | 2014-11-25 | 2014-11-25 | LNG Multi-class propagation system on ship |
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CN204415698U true CN204415698U (en) | 2015-06-24 |
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CN201420714724.8U Expired - Fee Related CN204415698U (en) | 2014-11-25 | 2014-11-25 | LNG Multi-class propagation system on ship |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105028296A (en) * | 2015-07-09 | 2015-11-11 | 青岛大学 | Special transport box device for liquefied natural gas fishing boat |
CN106482414A (en) * | 2016-12-01 | 2017-03-08 | 浙江海洋大学 | One kind is used for fishing boat power LNG cold energy stair device |
CN106672189A (en) * | 2016-08-24 | 2017-05-17 | 江苏省船舶设计研究所有限公司 | Single LNG (liquefied natural gas) fuel powered freighter |
-
2014
- 2014-11-25 CN CN201420714724.8U patent/CN204415698U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105028296A (en) * | 2015-07-09 | 2015-11-11 | 青岛大学 | Special transport box device for liquefied natural gas fishing boat |
CN106672189A (en) * | 2016-08-24 | 2017-05-17 | 江苏省船舶设计研究所有限公司 | Single LNG (liquefied natural gas) fuel powered freighter |
CN106672189B (en) * | 2016-08-24 | 2018-07-06 | 江苏省船舶设计研究所有限公司 | A kind of single LNG fuels and energies freighter |
CN106482414A (en) * | 2016-12-01 | 2017-03-08 | 浙江海洋大学 | One kind is used for fishing boat power LNG cold energy stair device |
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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: 20150624 Termination date: 20151125 |