CN204060975U - A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment - Google Patents
A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment Download PDFInfo
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- CN204060975U CN204060975U CN201420535611.1U CN201420535611U CN204060975U CN 204060975 U CN204060975 U CN 204060975U CN 201420535611 U CN201420535611 U CN 201420535611U CN 204060975 U CN204060975 U CN 204060975U
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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
- Y02T10/30—Use of alternative fuels, e.g. biofuels
Abstract
The utility model provides a kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment, comprises high-pressure gas air supply system and low-pressure fuel gas air supply system; High-pressure gas supply system adopts the transportation by lighter spray pump be arranged in or beyond described liquid container to be connected successively with working tank, suction booster, high-pressure gasified heater, pressurized gas valve cell and pressurized fuel gas machine by pipeline; Low-pressure fuel gas supply system adopts pipeline to be connected with from supercharging vaporizer at the liquid port of described working tank, the described outlet from supercharging vaporizer is connected to described working tank gas phase interface, and another liquid port of working tank is connected with low-pressure gasifying heater by pipeline, low-pressure fuel gas knock out drum, low-pressure gas valve cell and low-pressure gas fuel machine connect successively.The utility model solves fuel storage and gas gasification, the heating problems of non-LNG ships that transport, meets the supply gas pressure of high-voltage main and low pressure machines and the requirement of temperature simultaneously, and controls the pressure in LNG liquid storage cabin.
Description
Technical field
The utility model relates to a kind of air supply system peculiar to vessel, and particularly a kind of take rock gas as the high voltage/low voltage fuel gas supply system of the Ship Power Equipment of fuel.
Background technique
In recent years, along with pollution of atmosphere is day by day serious, the whole world is to the day by day serious lattice of the control of the gas discharging of boats and ships.The developed country such as American-European has established oneself emission control district, reaches TierII and TierIII emission standard at the appointed time.
Boats and ships natural gas fuel can reduce by carbon emission and discharged nitrous oxides, the sulfide emission of more than 98% and the fuel cost of about 30% of more than 30%.Therefore, to be fuel be energy-saving and emission-reduction that rock gas used instead by boats and ships, transport benefits the most directly effective measures are improved.In recent years, nearly all shipowner is the boats and ships of main fuel considering its existing ship to be transformed into LNG, and being at least transformed into LNG is the boats and ships of auxiliary fuel, can use LNG in emission control district of various countries, reaches emission standard.Nearly all shipyard is all the various boats and ships of fuel with LNG in consideration construction, and the double fuel tugboat project that first, China take LNG as main fuel has started to build, and provides LNG fuel storage supply system by our company, adopts the low service system of our company.
LNG fuel requirement, through gasification heating, becomes the gas of more than 0 DEG C could meet the requirement of cabin power plant from the liquid state of about-160 DEG C.Gasification and heating process need heat energy, and heating source can utilize the used heat of cabin power plant, also can utilize the waste gas that boiler produces.
The lower two-stroke low speed dual-fuel diesel engine (as the MEGI type main frame that MANB & W develops) of the energy consumption developed of present stage, the supply gas pressure needed is about 300Bar, gas compression is very huge to the volume of this stress level not only compressor, expensive, and the power consumption needed is also very high, LNG is pressurized to more than 300Bar by usual employing LNG suction booster, to meet the air feed demand of high-voltage main.Subsidiary engine on usual ship, as generator and boiler are also considered to adopt LNG as marine fuel, the supply gas pressure of usual subsidiary engine, at about 6Bar, for this reason, ship needs consider to be equipped with a set of low pressure air supply system, to meet the air supply requirement of low pressure main frame simultaneously.Simultaneously because LNG liquid storage cabin constantly absorbs heat from the external world, along with the increase of time, the pressure in LNG liquid storage cabin constantly raises, until reach the design pressure of storage tank.For this reason, during ship's navigation, need to take measures, the vapour tension in LNG liquid storage cabin is effectively controlled, prevents storage tank superpressure.
Model utility content
The technical problem that [1] will solve
In order to overcome problems of the prior art, the utility model provides a kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment, for solving the boats and ships being fuel with LNG Liquefied natural gas (LNG), the fuel storage of non-LNG ships that transport and gas gasification, heating especially, meet the supply gas pressure of high-voltage main and low pressure subsidiary engine and the requirement of temperature simultaneously, and the pressure in LNG liquid storage cabin is controlled.
The technological scheme of [2] dealing with problems
The utility model provides a kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment, and comprise LNG fueling station 1 and the liquid container 2 being provided with supervisory device, it also comprises high-pressure gas air supply system and low-pressure fuel gas air supply system;
Described high-pressure gas supply system adopts the LNG transportation by lighter/spray pump 3 be arranged in described liquid container 2 or outside liquid container 2 to be connected successively with LNG working tank 4, LNG suction booster 7, high-pressure gasified heater, pressurized gas valve cell 10 and pressurized fuel gas machine 11 by pipeline;
Described low-pressure fuel gas supply system adopts pipeline to be connected with from supercharging vaporizer 6 at the liquid port of described LNG working tank 4, the described outlet from supercharging vaporizer 6 is connected to described LNG working tank 4 gas phase interface, and another liquid port of described LNG working tank 4 is connected with low-pressure gasifying heater 13 by pipeline, low-pressure fuel gas knock out drum 12, low-pressure gas valve cell 14 and low-pressure gas fuel machine 15 connect successively.
Further, described low-pressure fuel gas supply system is connected with BOG compressor unit 5, low-pressure fuel gas knock out drum 12, low-pressure gas valve cell 14 and low-pressure gas fuel machine 15 by pipeline successively on the top of LNG liquid container 2.
Further, described high-pressure gasified heater comprises the high-pressure gasified heater of one-level 8 and/or the high-pressure gasified heater 9 of secondary.
Further, the outlet end of described high-pressure gasified heater is connected with the entry end of described low-pressure gasifying heater 13 after reduction valve.
Further, boil-off gas from described LNG liquid container 2 is connected with gas-liquid separator 5a, BOG heater 5b, BOG heater 5c in BOG compressor unit 5, compressor suction inlet thermostat valve 5d, BOG compressor 5e, compressor outlet thermostat valve 5f successively by pipeline, is finally connected with low-pressure fuel gas knock out drum 12.
Further, described BOG compressor 5e can adopt helical-lobe compressor or the piston compressor of normal temperature.
Further, the high-pressure gasified heater 8 of described one-level, low-pressure gasifying heater 13, from supercharging vaporizer 6, BOG heater 5c, BOG compressor 5e adopt pipeline be connected with Heating Cyclic unit 16.
Further, described Heating Cyclic unit 16 adopts ethylene glycol and water according to certain proportional arrangement, and the swelling water tank in described Heating Cyclic unit 16 is provided with ventilation mouth, and described ventilation mouth is connected to ventilative mast.
Further, described heating unit utilizes water glycol as middle heat medium, thermal oil system on the waste gas that the recycling main frame circulating water of coming or lubricating oil or boiler produce or ship carrys out heating water ethylene glycol solution, the waste gas heating LNG that the circulating water that also can directly utilize main frame to come or boiler produce, and controlled by the temperature of the water glycol in heat exchanger 17 pairs of Heating Cyclic unit 16, ensure that the temperature constant of glycol system is in settings.
Further, the high voltage/low voltage fuel gas supply system of described Ship Power Equipment is also applicable to the gas supply system of LNG cargo ship.
Utilize the method for work of the high voltage/low voltage fuel gas supply system of this Ship Power Equipment a kind of of the present utility model as follows, boil-off gas in described liquid container 2 is after BOG compressor unit 5 processes, heat exchange is carried out with from the high pressure low temperature LNG liquid in the high-pressure gasified heater 8 of one-level, get back to after condensation in LNG working tank 4 and mix with the cryogenic liquide from storage tank, after LNG suction booster 7 pressurizes, supply pressurized fuel gas machine 11 use;
Low-temperature evaporation gas in described liquid container 2 carries out heat exchange with the high-temperature gas of discharging from BOG compressor 5e in BOG heater 5b, enter in secondary BOG heater 5c subsequently and carry out BOG and carry out heat exchange from the circulating water of compressor, by the adjustment of compressor suction inlet thermostat valve 5d, the boil-off gas temperature entering compressor suction inlet is made to bring up to more than 0 DEG C, by the adjustment of the thermostat valve 5f on compressor air-discharging pipeline, the temperature controlling to enter low-pressure fuel gas knock out drum 12 controls within the scope of 20 ~ 40 DEG C, low-pressure gas in low-pressure fuel gas knock out drum 12 after low-pressure gas valve cell for low-pressure gas fuel machine,
Or low-temperature evaporation gas in described LNG liquid container 2 directly in BOG heater 5c with carry out BOG from the circulating water of compressor or Heating Cyclic unit 16 heating source carries out heat exchange, make the boil-off gas temperature entering compressor suction inlet bring up to more than 0 DEG C, by BOG compressor outlet heat exchanger 5g, compressor exhaust temperature is regulated, the temperature controlling to enter low-pressure fuel gas knock out drum 12 controls within the scope of 20 ~ 40 DEG C, the low-pressure gas in low-pressure fuel gas knock out drum 12 after low-pressure gas valve cell for low-pressure gas fuel machine.
[3] beneficial effect
The boats and ships that it is fuel that the high voltage/low voltage fuel gas supply system of the utility model Ship Power Equipment solves with LNG Liquefied natural gas (LNG), the gaseous fuel storage of non-LNG ships that transport especially, and gas gasification, heating, gas booster is to more than 300Bar, improve the high efficiency performance of low speed two stroke diesel engine, solve the air feed demand of low pressure air feed equipment on ship simultaneously, effectively the boil-off gas in LNG liquid storage cabin is controlled, maintain the pressure accumulation time of storage tank, reduce the design pressure of storage tank, save the construction cost in LNG liquid storage cabin greatly, ensure that LNG fuel system stores and the Security of air supplying operation and reliability aboard ship.
Accompanying drawing explanation
Fig. 1 is the high voltage/low voltage fuel gas supply system figure (LNG shifts spray pump and is arranged in storage tank) of a kind of Ship Power Equipment of the utility model;
Fig. 2 is the high voltage/low voltage fuel gas supply system figure (LNG shifts spray pump and is arranged on outside storage tank) of a kind of Ship Power Equipment of the utility model;
Fig. 3 is the BOG compressor unit schematic diagram of the high voltage/low voltage fuel gas supply system of a kind of Ship Power Equipment of the utility model;
Fig. 4 is the schematic diagram of another structure of BOG compressor unit of the high voltage/low voltage fuel gas supply system of a kind of Ship Power Equipment of the utility model.
Embodiment
Below in conjunction with accompanying drawing, introduce the utility model embodiment in detail.
Consult Fig. 1 to Fig. 4, the high voltage/low voltage fuel gas supply system of a kind of Ship Power Equipment of the utility model, comprise LNG fueling station 1 and be provided with the liquid container 2 of supervisory device, high-pressure gas air supply system and low-pressure fuel gas air supply system;
High-pressure gas supply system is adopted and is arranged on LNG transportation by lighter/spray pump in described liquid container 2 or outside liquid container 23 (this pump is with shifting the effect of LNG liquid to working tank and upper spray) and is connected successively with LNG working tank 4, LNG suction booster 7, high-pressure gasified heater, pressurized gas valve cell 10 and pressurized fuel gas machine 11 by pipeline; The discharge capacity of LNG suction booster 7 is regulated by the supply gas pressure of main frame, on the pipeline being exported to LNG working tank 4 by the discharge capacity of control LNG suction booster 7 and LNG suction booster 7 control valve 7a flow thus reach and control gas outlet pressure, ensure the stability of pressurized fuel gas main frame air feed.
Low-pressure fuel gas supply system can take one or several modes in following two kinds of modes to combine:
First method: low-pressure fuel gas supply system adopts pipeline to be connected with from supercharging vaporizer 6 at the liquid port of LNG working tank 4, the described outlet from supercharging vaporizer 6 is connected to described LNG working tank 4 gas phase interface, the deadweight of liquid in LNG working tank 4 is utilized to flow through in supercharging vaporizer 6, get back in LNG working tank 4 after gasification, carry out supercharging to working tank, make its pressure maintain the supply gas pressure of low-pressure gas fuel machine; Another liquid port of LNG working tank 4 is connected with low-pressure gasifying heater 13 by pipeline, low-pressure fuel gas knock out drum 12, low-pressure gas valve cell 14 and low-pressure gas fuel machine 15 connect successively; Utilize the self-pressure in LNG working tank 4, make liquid stream through low-pressure gasifying heater 13, the fuel gas supply low-pressure gas fuel machine after gasification, heating uses, and the combustion gas of the maximum 10Bar of providing uses to auxiliary power plant.
The second way: low-pressure fuel gas supply system is connected with BOG compressor unit 5, low-pressure fuel gas knock out drum 12, low-pressure gas valve cell 14 and low-pressure gas fuel machine 15 by pipeline successively on the top of LNG liquid container 2; To enter in secondary BOG heater 5c and carry out heat exchange, adjustment by compressor suction inlet thermostat valve 5d from the circulating water of compressor after carrying out heat exchange with the high-temperature gas of discharging from BOG compressor 5e from the BOG of liquid container in BOG heater 5b, subsequently, the boil-off gas temperature entering compressor suction inlet is made to bring up to more than 0 DEG C, by the adjustment of the thermostat valve 5f on compressor air-discharging pipeline, control compressor exit temperature within the scope of 20 ~ 40 DEG C, (consulting Fig. 3).Or also can directly by BOG heater 5c with from compressor circulating water or Heating Cyclic unit 16 heating source carries out heat exchange, make the boil-off gas temperature entering compressor suction inlet bring up to more than 0 DEG C, regulated compressor exhaust temperature by compressor outlet heat exchanger 5g, the temperature controlling to enter low-pressure fuel gas knock out drum 12 controls (to consult Fig. 4) within the scope of 20 ~ 40 DEG C.The combustion gas of the maximum 10Bar of providing uses to low-pressure gas fuel machine 15.
The third mode: the outlet end of high-pressure gasified heater is connected with the entry end of described low-pressure gasifying heater 13 after reduction valve, through high-pressure gasified heater high-pressure gas out, after reduction valve 9a step-down, flow through low-pressure gasifying heater 13, supply low-pressure gas fuel machine 15 uses.
Heating Cyclic unit 16 adopts ethylene glycol and water according to the configuration of certain ratio row, in the present embodiment, the volume ratio of ethylene glycol and water is 1/2-2/1, swelling water tank in Heating Cyclic unit 16 is provided with ventilation mouth, ventilation mouth is connected to ventilative mast, once high-pressure gas pipeline leaks to water glycol system, combustion gas is separated in swelling water tank, and combustion gas is disposed in air by ventilation mouth.This system can be arranged in safety zone, and can make heat medium continuous circulation between safety zone and hazardous area, swelling water tank is provided with combustible gas detecting device, for detecting the leakage of combustion gas, and triggers corresponding warning reminding.This Heating Cyclic unit 16, consider from security standpoint: this heating source can be utilize water glycol as middle heat medium, the circulating water that recycling main frame is come, lubricating oil, boiler produce waste gas or ship on thermal oil system carry out heating water ethylene glycol solution, the waste gas heating LNG that the circulating water that also can directly utilize main frame to come or boiler produce, controlled by the temperature of heat exchanger 17 to the water glycol in this Heating Cyclic unit 16, ensure that the temperature constant of glycol system is in settings: the high-pressure gasified heater 8 of one-level, low-pressure gasifying heater 13, from supercharging vaporizer 6, BOG heater 5c, BOG compressor 5e adopts pipeline to be connected with Heating Cyclic unit 16, BOG compressor 5e can adopt helical-lobe compressor or the piston compressor of normal temperature.
In the present embodiment, comprise the high-pressure gasified heater of one-level 8 and/or the high-pressure gasified heater 9 of secondary at high-pressure gasified heater.
Boil-off gas from LNG liquid container 2 is connected with gas-liquid separator 5a, BOG heater 5b, BOG heater 5c in BOG compressor unit 5, compressor suction inlet thermostat valve 5d, BOG compressor 5e, compressor outlet thermostat valve 5f successively by pipeline, is finally connected with low-pressure fuel gas knock out drum 12.
A method of work for the high voltage/low voltage fuel gas supply system of this Ship Power Equipment, it comprises high-pressure air feed and low pressure air feed two processes;
High-pressure air feed: the boil-off gas in liquid container 2 is after BOG compressor unit 5 processes, heat exchange is carried out with from the high pressure low temperature LNG liquid in the high-pressure gasified heater 8 of one-level, get back to after condensation in LNG working tank 4 and mix with the cryogenic liquide from storage tank, after LNG suction booster 7 pressurizes, supply pressurized fuel gas machine 11 use;
Low pressure air feed has two kinds of modes:
Mode one: the low-temperature evaporation gas in liquid container 2 carries out heat exchange with the high-temperature gas of discharging from BOG compressor 5e in BOG heater 5b, enter in secondary BOG heater 5c subsequently and carry out BOG and carry out heat exchange from the circulating water of compressor, by the adjustment of compressor suction inlet thermostat valve 5d, the boil-off gas temperature entering compressor suction inlet is made to bring up to more than 0 DEG C, by the adjustment of the thermostat valve 5f on compressor air-discharging pipeline, the temperature controlling to enter low-pressure fuel gas knock out drum 12 controls within the scope of 20 ~ 40 DEG C, low-pressure gas in low-pressure fuel gas knock out drum 12 after low-pressure gas valve cell for low-pressure gas fuel machine,
Mode two: the low-temperature evaporation gas in liquid container 2 directly in BOG heater 5c with carry out BOG from the circulating water of compressor or Heating Cyclic unit 16 heating source carries out heat exchange, make the boil-off gas temperature entering compressor suction inlet bring up to more than 0 DEG C, by BOG compressor outlet heat exchanger 5g, compressor exhaust temperature is regulated, the temperature controlling to enter low-pressure fuel gas knock out drum 12 controls within the scope of 20 ~ 40 DEG C, the low-pressure gas in low-pressure fuel gas knock out drum 12 after low-pressure gas valve cell for low-pressure gas fuel machine.
The high voltage/low voltage fuel gas supply system of the utility model Ship Power Equipment, the liquid shifted by control LNG in the discharge capacity control LNG working tank 4 of spray pump 3 is within the scope of certain liquid level all the time.The supply gas pressure of low-pressure gas fuel machine is maintained by the pressure in supercharging vaporizer 6 control LNG working tank 4; The air demand of pressurized fuel gas machine is regulated by the discharge capacity of control LNG suction booster 7 and the flow of booster pump outlet pipe-line control valve 7a.
The high voltage/low voltage fuel gas supply system of the utility model Ship Power Equipment is also applicable to the gas supply system of LNG cargo ship.
Adopt the high voltage/low voltage fuel gas supply system of technique scheme, by suction booster by/heating of gasifying after LNG fluid pressurization to 315bar, than adopting gas compressor supercharging, energy consumption saves more than 95%, adopt LNG working tank to carry out storage compartment liquid fuel simultaneously, by the control of the liquid level in LNG working tank and pressure, effectively ensure that the stability of high pressure air feed system and low pressure air supply system.Adopt less and low pressure compressor treatments B OG, supply low pressure gas equipment, can make LNG fuel longer-term storage aboard ship, the design of BOG compressor unit, the design pressure of storage tank can be made lower, reduce the expenditure of construction of storage tank.BOG simultaneously in LNG liquid storage cabin is getting back in LNG working tank through high-pressure service pump supercharging after condensation again, the used up scheme of supply high-voltage main after gasification heating, effectively solve when ship not being installed low-pressure gas fuel machine, or low-pressure gas fuel cannot all by problem that subsidiary engine consumes.This intrasystem BOG compressor process is gas at normal temperature simultaneously, compares low temperature BOG compressor, the manufacturing expense of the compressor effectively reduced.
Claims (10)
1. a high voltage/low voltage fuel gas supply system for Ship Power Equipment, comprises LNG fueling station (1) and is provided with the liquid container (2) of supervisory device, it is characterized in that: also comprise high-pressure gas air supply system and low-pressure fuel gas air supply system;
Described high-pressure gas supply system employing is arranged in described liquid container (2) or liquid container (2) LNG transportation by lighter/spray pump (3) is outward connected with LNG working tank (4), LNG suction booster (7), high-pressure gasified heater, pressurized gas valve cell (10) and pressurized fuel gas machine (11) successively by pipeline;
Described low-pressure fuel gas supply system adopts pipeline to be connected with from supercharging vaporizer (6) at the liquid port of described LNG working tank (4), the described outlet from supercharging vaporizer (6) is connected to described LNG working tank (4) gas phase interface, and another liquid port of described LNG working tank (4) is connected with low-pressure gasifying heater (13) by pipeline, low-pressure fuel gas knock out drum (12), low-pressure gas valve cell (14) and low-pressure gas fuel machine (15) connect successively.
2. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 1, is characterized in that: described low-pressure fuel gas supply system is connected with BOG compressor unit (5), low-pressure fuel gas knock out drum (12), low-pressure gas valve cell (14) and low-pressure gas fuel machine (15) by pipeline successively on the top of LNG liquid container (2).
3. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 2, is characterized in that: described high-pressure gasified heater comprises the high-pressure gasified heater of one-level (8) and/or the high-pressure gasified heater of secondary (9).
4. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 3, is characterized in that: the outlet end of described high-pressure gasified heater is connected with the entry end of described low-pressure gasifying heater (13) after reduction valve.
5. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 3, it is characterized in that: the boil-off gas from described LNG liquid container (2) is connected with the gas-liquid separator (5a) in BOG compressor unit (5), BOG heater (5b), BOG heater (5c), compressor suction inlet thermostat valve (5d), BOG compressor (5e), compressor outlet thermostat valve (5f) successively by pipeline, be finally connected with low-pressure fuel gas knock out drum (12).
6. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 5, is characterized in that: described BOG compressor (5e) can adopt helical-lobe compressor or the piston compressor of normal temperature.
7. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 5, is characterized in that: the high-pressure gasified heater of described one-level (8), low-pressure gasifying heater (13), adopt pipeline to be connected with Heating Cyclic unit (16) from supercharging vaporizer (6), BOG heater (5c), BOG compressor (5e).
8. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 7, it is characterized in that: described Heating Cyclic unit (16) adopts ethylene glycol and water according to certain proportional arrangement, swelling water tank in described Heating Cyclic unit (16) is provided with ventilation mouth, and described ventilation mouth is connected to ventilative mast.
9. the high voltage/low voltage fuel gas supply system of Ship Power Equipment as claimed in claim 8, it is characterized in that: described heating unit utilizes water glycol as middle heat medium, thermal oil system on the waste gas that the recycling main frame circulating water of coming or lubricating oil or boiler produce or ship carrys out heating water ethylene glycol solution, the waste gas heating LNG that the circulating water that also can directly utilize main frame to come or boiler produce, and controlled by the temperature of heat exchanger (17) to the water glycol in Heating Cyclic unit (16), ensure that the temperature constant of glycol system is in settings.
10. the high voltage/low voltage fuel gas supply system of the Ship Power Equipment as described in any one of claim 1 to 9, is characterized in that: the high voltage/low voltage fuel gas supply system of described Ship Power Equipment is also applicable to the gas supply system of LNG cargo ship.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420535611.1U CN204060975U (en) | 2014-09-17 | 2014-09-17 | A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420535611.1U CN204060975U (en) | 2014-09-17 | 2014-09-17 | A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment |
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| CN204060975U true CN204060975U (en) | 2014-12-31 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420535611.1U Withdrawn - After Issue CN204060975U (en) | 2014-09-17 | 2014-09-17 | A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104265512A (en) * | 2014-09-17 | 2015-01-07 | 刘国满 | High-pressure/low-pressure gas supply system of ship power plant |
| CN105909379A (en) * | 2016-06-12 | 2016-08-31 | 深圳市金动科力实业有限公司 | Multifunctional V-shaped power integrated machine |
| CN109506126A (en) * | 2018-11-30 | 2019-03-22 | 上海海威斯特保温工程有限公司 | A kind of re-liquefied fuel dispensing system of small-sized LNG fuel ship BOG |
| CN110475713A (en) * | 2017-04-13 | 2019-11-19 | 三菱造船株式会社 | Ship |
| CN111392019A (en) * | 2020-03-27 | 2020-07-10 | 大连船舶重工集团有限公司 | Clean ship power system who discharges |
| CN115370467A (en) * | 2022-08-02 | 2022-11-22 | 上海海事大学 | Carbon reduction system for LNG power ship and EEDI calculation method |
-
2014
- 2014-09-17 CN CN201420535611.1U patent/CN204060975U/en not_active Withdrawn - After Issue
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104265512A (en) * | 2014-09-17 | 2015-01-07 | 刘国满 | High-pressure/low-pressure gas supply system of ship power plant |
| CN104265512B (en) * | 2014-09-17 | 2017-05-24 | 刘国满 | High-pressure/low-pressure gas supply system of ship power plant |
| CN105909379A (en) * | 2016-06-12 | 2016-08-31 | 深圳市金动科力实业有限公司 | Multifunctional V-shaped power integrated machine |
| CN105909379B (en) * | 2016-06-12 | 2018-12-07 | 深圳市金动科力实业有限公司 | A kind of Multi-functional V-shaped power all-in-one machine |
| CN110475713A (en) * | 2017-04-13 | 2019-11-19 | 三菱造船株式会社 | Ship |
| CN110475713B (en) * | 2017-04-13 | 2021-06-08 | 三菱造船株式会社 | Ship with a detachable cover |
| CN109506126A (en) * | 2018-11-30 | 2019-03-22 | 上海海威斯特保温工程有限公司 | A kind of re-liquefied fuel dispensing system of small-sized LNG fuel ship BOG |
| CN111392019A (en) * | 2020-03-27 | 2020-07-10 | 大连船舶重工集团有限公司 | Clean ship power system who discharges |
| CN115370467A (en) * | 2022-08-02 | 2022-11-22 | 上海海事大学 | Carbon reduction system for LNG power ship and EEDI calculation method |
| CN115370467B (en) * | 2022-08-02 | 2024-04-19 | 上海海事大学 | Carbon reduction system for LNG power ship and EEDI calculation method |
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