CN104595063A - Liquefied natural gas gasification system based on cooling water residual heat of dual-fuel ship engine - Google Patents
Liquefied natural gas gasification system based on cooling water residual heat of dual-fuel ship engine Download PDFInfo
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- 239000003949 liquefied natural gas Substances 0.000 title claims abstract description 143
- 239000000498 cooling water Substances 0.000 title claims abstract description 66
- 239000000446 fuel Substances 0.000 title claims abstract description 40
- 238000002309 gasification Methods 0.000 title claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 101
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 76
- 239000006200 vaporizer Substances 0.000 claims abstract description 27
- 238000001816 cooling Methods 0.000 claims abstract description 10
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 94
- 239000007789 gas Substances 0.000 claims description 64
- 239000003345 natural gas Substances 0.000 claims description 44
- 230000000087 stabilizing effect Effects 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 4
- 239000011435 rock Substances 0.000 claims 7
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 5
- 239000000567 combustion gas Substances 0.000 claims 3
- 239000000112 cooling gas Substances 0.000 claims 3
- 230000008676 import Effects 0.000 claims 3
- 238000010521 absorption reaction Methods 0.000 claims 1
- 230000011664 signaling Effects 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 abstract description 29
- 239000002918 waste heat Substances 0.000 abstract description 14
- 238000002485 combustion reaction Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 description 20
- 230000009977 dual effect Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000010248 power generation Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 230000032258 transport Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
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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
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Abstract
本发明公开一种基于双燃料船舶发动机冷却水余热的液态天然气气化系统,由缸套冷却水循环系统、工质循环系统、LNG供给气化系统和PLC控制系统这四个子系统构成;缸套冷却水循环系统包括缸套水泵、冷却水箱、LNG/柴油双燃料发动机、板式换热器及风扇式散热器;工质循环系统包括工质箱、工质泵,工质箱通过工质出口连接板式换热器的工质进口,LNG供给气化系统包括LNG泵、LNG气化器及辅助LNG储罐,辅助LNG储罐依次经手动调节阀、LNG泵、第三液体流量传感器、第三液体比例调节阀与LNG气化器连接;本发明利用LNG/柴油双燃料发动机的缸套水的余热对LNG进行气化,对高温缸套水冷却散热,同时又提高了LNG/柴油双燃料发动机燃料的燃烧效率。
The invention discloses a liquefied natural gas gasification system based on the waste heat of the cooling water of a dual-fuel marine engine, which is composed of four subsystems: a cylinder liner cooling water circulation system, a working medium circulation system, an LNG supply gasification system and a PLC control system; the cylinder liner cooling The water circulation system includes cylinder jacket water pump, cooling water tank, LNG/diesel dual-fuel engine, plate heat exchanger and fan radiator; The working medium inlet of the heater, the LNG supply gasification system includes LNG pump, LNG vaporizer and auxiliary LNG storage tank. The auxiliary LNG storage tank is regulated by manual regulating valve, LNG pump, third liquid flow sensor and third liquid ratio The valve is connected with the LNG gasifier; the invention utilizes the waste heat of the cylinder jacket water of the LNG/diesel dual-fuel engine to vaporize the LNG, cools and dissipates heat from the high-temperature cylinder jacket water, and improves the fuel combustion of the LNG/diesel dual-fuel engine at the same time efficiency.
Description
技术领域 technical field
本发明涉及废热气化LNG(Liquefied Natural Gas,液态天然气)的设备技术领域,特别是涉及一种LNG/柴油双燃料船舶发动机冷却水余热的LNG气化系统。 The invention relates to the technical field of waste heat gasification LNG (Liquefied Natural Gas, liquefied natural gas) equipment, in particular to an LNG gasification system for waste heat of cooling water of LNG/diesel dual-fuel ship engine.
背景技术 Background technique
与传统的柴油机相比,LNG/柴油双燃料发动机具有有害排放少等优点,能够满足日益严格的排放法规要求,是一种绿色的动力系统,有望广泛应用于船舶、城市交通、发电机组和中重型载货汽车等。而在-162℃温度下的液态LNG成为发动机燃料前需要气化成为气态,且每千克LNG气化需要吸收837kJ热量。由此同时,传统发动机的有效热效率不到50%,其余25%的热量被废气带走,另外20%的热量由缸套冷却水带走,剩余5%则通过热辐射和润滑油散发到大气。 Compared with traditional diesel engines, LNG/diesel dual-fuel engines have the advantages of less harmful emissions and can meet increasingly stringent emission regulations. Heavy-duty trucks, etc. However, liquid LNG at a temperature of -162°C needs to be vaporized into a gaseous state before it can be used as engine fuel, and every kilogram of LNG needs to absorb 837kJ of heat for gasification. At the same time, the effective thermal efficiency of the traditional engine is less than 50%, the remaining 25% of the heat is taken away by the exhaust gas, the other 20% of the heat is taken away by the cylinder liner cooling water, and the remaining 5% is dissipated to the atmosphere through heat radiation and lubricating oil .
公开号CN103899440A(公开日2014年07月02日)公开了一种基于排气能量回收的船用气体/双燃料发动机LNG气化系统及控制法,包括换热介质箱、排气换热器、散热器、发动机膨胀水箱、 LNG气化器、集液盘,换热介质箱里的换热介质通过第一可调节流量泵进入排气换热器,经散热器后进入LNG气化器再流回换热介质箱,外接水源通过集液盘经三通阀分别进入发动机膨胀水箱、散热器后排出,进入散热器的外接水源与换热介质不掺混,即按照各自对应的管路流动。该技术是将双燃料发动机排气废热进行回收,并用于LNG气化,但没有涉及到缸套冷却水的废热回收。 Publication number CN103899440A (published on July 02, 2014) discloses a marine gas/dual fuel engine LNG gasification system and control method based on exhaust energy recovery, including heat exchange medium tank, exhaust heat exchanger, heat dissipation The heat exchange medium in the heat exchange medium tank enters the exhaust heat exchanger through the first adjustable flow pump, enters the LNG vaporizer after passing through the radiator, and then flows back In the heat exchange medium tank, the external water source enters the engine expansion water tank and the radiator respectively through the liquid collecting tray and the three-way valve, and then is discharged. The external water source entering the radiator does not mix with the heat exchange medium, that is, flows according to their corresponding pipelines. This technology recovers exhaust waste heat from dual-fuel engines and uses it for LNG gasification, but does not involve the recovery of waste heat from cylinder liner cooling water.
中国专利公开号CN103967648A(公开日2014年8月6日) 的文献提供的是一种船舶低速柴油机余热综合回收系统,包括组合余热锅炉系统、动力涡轮发电系统、汽轮机发电系统、高温冷却水利用换热设备和有机工质汽轮机发电系统,其中与缸套水换热器并联的缸套水有机工质预热器,在工作时,有机工质经缸套水有机工质预热器后进入中温换热器再进入有机工质蒸发器段,高压的有机工质驱动汽轮机发电系统用来发电,将柴油机缸套水的废热用来发电。没有涉及到LNG/柴油双燃料发动机和LNG的气化技术,目前,未见有关回收冷却水余热并用于气化LNG的技术报道。 The document of Chinese Patent Publication No. CN103967648A (publication date: August 6, 2014) provides a comprehensive waste heat recovery system for marine low-speed diesel engines, including a combined waste heat boiler system, a power turbine power generation system, a steam turbine power generation system, and a high-temperature cooling water utilization system Thermal equipment and organic working medium steam turbine power generation system, in which the jacket water organic working medium preheater connected in parallel with the jacket water heat exchanger, when working, the organic working medium enters the medium temperature after passing through the jacket water organic working medium preheater The heat exchanger then enters the organic working medium evaporator section, and the high-pressure organic working medium drives the steam turbine power generation system to generate electricity, and the waste heat of the jacket water of the diesel engine is used to generate electricity. There is no LNG/diesel dual-fuel engine and LNG gasification technology. At present, there is no technical report on recovering the waste heat of cooling water and using it for gasification of LNG.
发明内容 Contents of the invention
本发明解决的技术问题是提供一种基于液态天然气/柴油双燃料船舶发动机冷却水余热的液态天然气气化系统,能回收冷却水余热并用于气化LNG。 The technical problem solved by the invention is to provide a liquid natural gas gasification system based on liquid natural gas/diesel dual-fuel ship engine cooling water waste heat, which can recover the cooling water waste heat and use it for gasifying LNG.
本发明采用的技术方案是:由缸套冷却水循环系统、工质循环系统、LNG供给气化系统和PLC控制系统这四个子系统构成,缸套冷却水循环系统包括缸套水泵、冷却水箱、LNG/柴油双燃料发动机、板式换热器及风扇式散热器,LNG/柴油双燃料发动机的缸套水出水口与冷却水箱上部的缸套水进水口之间的连接管道上依次接有第一温度传感器、第一三通阀、第一液体流量传感器及第一液体比例调节阀,第一三通阀的中间端口与发动机冷却系统小循环相接;冷却水箱底部的缸套水出水口与第一、第二液体电磁阀之间的第一个三通的中间端口相接,在冷却水箱底部的缸套水出水口与第一个三通的中间端口之间接有缸套水泵;第一个三通的上端口与板式换热器相接,第一个三通的下端口与风扇式散热器入水口相接;板式换热器出水口与第二个三通的左端口连接,在板式换热器出水口与第二个三通的左端口之间接有第三液体电磁阀,第二个三通的右端口与风扇式散热器的出水口相接,在第二个三通的右端口与风扇式散热器的出水口之间接有第四液体电磁阀;第二个三通的中间端口经液体单向阀、第二三通阀、第二温度传感器与LNG/柴油双燃料发动机的缸套水进水口连接,第二三通阀的中间端口与发动机冷却系统小循环相接;所述第一、第二温度传感器、第一液体比例调节阀、第一液体流量传感器、缸套水泵、第一、第二、第三、第四液体单向阀都连接PLC控制系统中的PLC控制器;工质循环系统包括工质箱、工质泵,工质箱通过工质出口连接板式换热器的工质进口,在工质箱与板式换热器之间依次接有第二液体比例调节阀、第二液体流量传感器、工质泵、第三温度传感器;板式换热器的工质出口与LNG气化器的工质进口连接,LNG气化器的工质出口与工质箱的工质进口连接;LNG供给气化系统包括LNG泵、LNG气化器及辅助LNG储罐,辅助LNG储罐依次经手动调节阀、LNG泵、第三液体流量传感器、第三液体比例调节阀与LNG气化器连接, LNG气化器顶端的气态天然气出口与天然气稳压气罐底部连接,第三液体流量传感器、第三液体比例调节阀、LNG泵分别连接 PLC控制器;当缸套出水口温度介于75℃到90℃之间时,PLC控制器控制第二、第三液体电磁阀关闭、第一、第四液体电磁阀开启,缸套水泵将高温缸套水输送到风扇式散热器中放热,降温后的缸套冷却水经液体单向阀流回到LNG/柴油双燃料发动机的缸套内吸热,当缸套出水口温度大于等于90℃时,PLC控制器控制液第二、第三体电磁阀开启、第一、第四液体电磁阀关闭,缸套水泵将高温缸套冷却水从缸套出水口输送到板式换热器中向工质放热,放热后的冷却水温度降低,经液体单向阀再次回到缸套内吸收热量;PLC控制器给工质泵指令将工质从工质箱中泵出,从板式换热器吸热后到LNG气化器中放热,放热后再次流向板式换热器吸收热量。 The technical solution adopted in the present invention is: it is composed of four subsystems, namely cylinder liner cooling water circulation system, working medium circulation system, LNG supply gasification system and PLC control system. The cylinder liner cooling water circulation system includes cylinder liner water pump, cooling water tank, LNG/ Diesel dual-fuel engine, plate heat exchanger and fan radiator, the connecting pipe between the jacket water outlet of the LNG/diesel dual-fuel engine and the jacket water inlet on the upper part of the cooling water tank is sequentially connected with the first temperature sensor , the first three-way valve, the first liquid flow sensor and the first liquid proportional regulating valve, the middle port of the first three-way valve is connected with the small circulation of the engine cooling system; the cylinder jacket water outlet at the bottom of the cooling water tank is connected with the first, The middle port of the first three-way between the second liquid solenoid valves is connected, and the jacket water pump is connected between the jacket water outlet at the bottom of the cooling water tank and the middle port of the first three-way; the first three-way The upper port of the plate heat exchanger is connected with the plate heat exchanger, and the lower port of the first tee is connected with the water inlet of the fan radiator; the water outlet of the plate heat exchanger is connected with the left port of the second tee. The third liquid solenoid valve is connected between the water outlet of the device and the left port of the second three-way, the right port of the second three-way is connected with the water outlet of the fan radiator, and the right port of the second three-way is connected with the water outlet of the fan radiator. The fourth liquid solenoid valve is connected between the water outlets of the fan radiator; the middle port of the second three-way passes through the liquid check valve, the second three-way valve, the second temperature sensor and the cylinder liner of the LNG/diesel dual-fuel engine. The water inlet is connected, and the middle port of the second three-way valve is connected with the small circulation of the engine cooling system; the first and second temperature sensors, the first liquid proportional regulating valve, the first liquid flow sensor, the cylinder jacket water pump, the first 1. The second, third, and fourth liquid check valves are all connected to the PLC controller in the PLC control system; the working medium circulation system includes a working medium tank and a working medium pump, and the working medium tank is connected to the plate heat exchanger through the working medium outlet The inlet of the working fluid, the second liquid proportional regulating valve, the second liquid flow sensor, the working fluid pump, and the third temperature sensor are sequentially connected between the working fluid tank and the plate heat exchanger; the working fluid outlet of the plate heat exchanger is connected to the The working fluid inlet connection of the LNG gasifier, the working fluid outlet of the LNG gasifier is connected to the working fluid inlet of the working fluid box; the LNG supply gasification system includes the LNG pump, the LNG gasifier and the auxiliary LNG storage tank, and the auxiliary LNG storage tank The tank is connected to the LNG vaporizer through the manual regulating valve, the LNG pump, the third liquid flow sensor, and the third liquid proportional regulating valve in sequence. The flow sensor, the third liquid proportional regulating valve and the LNG pump are respectively connected to the PLC controller; when the water outlet temperature of the cylinder liner is between 75°C and 90°C, the PLC controller controls the closing of the second and third liquid solenoid valves, and the closing of the third liquid solenoid valve. 1. The fourth liquid solenoid valve is opened, and the jacket water pump transports the high-temperature jacket water to the fan radiator to dissipate heat. The cooled jacket cooling water flows back to the cylinder of the LNG/diesel dual-fuel engine through the liquid check valve. The jacket absorbs heat. When the water outlet temperature of the cylinder jacket is greater than or equal to 90°C, the PLC controller controls the liquid The second and third body solenoid valves are opened, the first and fourth liquid solenoid valves are closed, and the jacket water pump transports the high-temperature jacket cooling water from the outlet of the jacket to the plate heat exchanger to release heat to the working medium. The temperature of the cooling water drops, and it returns to the cylinder liner to absorb heat through the liquid check valve; the PLC controller gives instructions to the working medium pump to pump the working medium out of the working medium tank, and after absorbing heat from the plate heat exchanger, it is delivered to the LNG gas. Heat is released in the carburetor, and then flows to the plate heat exchanger to absorb heat again.
本发明的有益效果为: The beneficial effects of the present invention are:
1.本发明提供了一套辅助LNG气化系统,利用LNG/柴油双燃料发动机的缸套水的余热对LNG进行气化,做到了对高温缸套水冷却散热,同时又提高了LNG/柴油双燃料发动机燃料的燃烧效率。 1. The present invention provides a set of auxiliary LNG gasification system, which utilizes the waste heat of the cylinder jacket water of the LNG/diesel dual-fuel engine to gasify LNG, so as to cool and dissipate heat from the high-temperature cylinder jacket water, and at the same time improve the LNG/diesel fuel efficiency. Combustion efficiency of dual fuel engine fuel.
2.本发明采用了PLC控制器对系统进行自动控制,可以保证工质、天然气、缸套水的精确输送以及确保了操作人员的安全性。 2. The present invention adopts a PLC controller to automatically control the system, which can ensure the precise delivery of working fluid, natural gas and jacket water and ensure the safety of operators.
3.本发明在发动机冷启动过程中采用温度传感器、流量传感器、液体比例调节阀和PLC控制系统的相互配合,取代了传统的发动机节温器,对进入发动机缸套的冷却水的温度进行精确控制,从而确保最终进入LNG/柴油双燃料发动机缸套的冷却水保持发动机缸套的最佳冷却温度。 3. The present invention adopts the mutual cooperation of temperature sensor, flow sensor, liquid proportional regulating valve and PLC control system in the process of engine cold start, replaces the traditional engine thermostat, and accurately controls the temperature of the cooling water entering the engine cylinder liner. Control, so as to ensure that the cooling water that finally enters the cylinder liner of the LNG/diesel dual fuel engine maintains the optimum cooling temperature of the engine liner.
下面结合附图及具体实施方式对本发明作更详细的描述。 The present invention will be described in more detail below in conjunction with the accompanying drawings and specific embodiments.
附图说明 Description of drawings
图1为本发明基于双燃料船舶发动机冷却水余热的液态天然气气化系统的结构示意图; Fig. 1 is the structure schematic diagram of the liquefied natural gas gasification system based on the waste heat of the cooling water of the dual-fuel marine engine of the present invention;
图中:1.气体电磁阀;2.天然气稳压气罐;3.压力传感器;4.手动调节阀;5.气体比例调节阀;6.燃气滤清器;7.天然气/空气混合器;8.发动机气缸;9.PLC控制器;10.异径三通;11.气体单向阀;12.LNG气化器;13.液体比例调节阀;14.液体流量传感器;15.三通阀;16.温度传感器;17.三通阀;18.液体单向阀;19.冷却水箱;20.LNG/柴油双燃料发动机;21.板式换热器;22.高温缸套水泵;23.工质液位传感器;24.工质箱;25.液体比例调节阀;26.温度传感器;27.温度传感器;28.温度传感器;29.流量传感器;30.工质泵;31.液体流量传感器;32.液体比例调节阀;33、34、35、36.液体电磁阀;37.可调速电机;38.风扇式散热器;39.LNG泵;40.手动调节阀;41.天然气泄漏报警器;42.辅助LNG储罐;43.LNG液位传感器;44.气体单向阀;45.闪蒸汽(Boil Off Gas ,简称BOG,闪蒸汽)储罐; 46.气体压力传感器;47.温度传感器;48.温度传感器。 In the figure: 1. Gas solenoid valve; 2. Natural gas regulator tank; 3. Pressure sensor; 4. Manual control valve; 5. Gas proportional control valve; 6. Gas filter; 7. Natural gas/air mixer; 8. Engine cylinder; 9. PLC controller; 10. Different diameter tee; 11. Gas one-way valve; 12. LNG vaporizer; 13. Liquid proportional regulating valve; 14. Liquid flow sensor; 15. Three-way valve ; 16. Temperature sensor; 17. Three-way valve; 18. Liquid one-way valve; 19. Cooling water tank; 20. LNG/diesel dual fuel engine; 21. Plate heat exchanger; 22. High temperature cylinder jacket pump; 23. Work 24. Working medium tank; 25. Liquid proportional regulating valve; 26. Temperature sensor; 27. Temperature sensor; 28. Temperature sensor; 29. Flow sensor; 30. Working medium pump; 31. Liquid flow sensor; 32. Liquid proportional regulating valve; 33, 34, 35, 36. Liquid solenoid valve; 37. Adjustable speed motor; 38. Fan radiator; 39. LNG pump; 40. Manual regulating valve; 41. Natural gas leakage alarm ;42. Auxiliary LNG storage tank; 43. LNG liquid level sensor; 44. Gas check valve; 45. Flash steam (Boil Off Gas, referred to as BOG, flash steam) storage tank; 46. Gas pressure sensor; 47. Temperature sensor ; 48. Temperature sensor.
具体实施方式 Detailed ways
如图1所示,本发明由四个子系统构成,分别是缸套冷却水循环系统、工质循环系统、LNG供给气化系统和PLC控制系统。 As shown in Fig. 1, the present invention is composed of four subsystems, which are cylinder jacket cooling water circulation system, working medium circulation system, LNG supply gasification system and PLC control system.
缸套冷却水循环系统包括高温缸套水泵22、冷却水箱19、LNG/柴油双燃料发动机20、板式换热器21、风扇式散热器38以及连接管道等。LNG/柴油双燃料发动机20左侧的缸套水出水口与冷却水箱19上部的缸套水进水口之间通过管道连接,在LNG/柴油双燃料发动机20的缸套水出水口与冷却水箱19上部的缸套水进水口之间的连接管道上依次接有温度传感器16、三通阀15、液体流量传感器14、液体比例调节阀13。其中,三通阀15的中间端口通过管道与发动机冷却系统小循环相接。冷却水箱19底部的缸套水出水口与液体电磁阀33和液体电磁阀34之间的三通的中间端口通过管道相接,在冷却水箱19底部的缸套水出水口与此三通的中间端口之间的连接管道上接有高温缸套水泵22。液体电磁阀33和液体电磁阀34之间的三通的上端口与板式换热器21左侧上部的高温缸套水进水口相接,在此三通的上端口与板式换热器21左侧上部的高温缸套水进水口之间的连接管道上接液体电磁阀34,此三通的下端口与风扇式散热器38左侧的入水口相接,此三通的下端口与风扇式散热器38左侧的入水口之间的管道上接液体电磁阀33。板式换热器21右侧下部的高温缸套水出水口与三通29的左端口通过管道连接,在板式换热器21右侧下部的高温缸套水出水口与三通29的左端口之间的管道上接有一液体电磁阀35,三通29的右端口与风扇式散热器38右侧的出水口之间通过管道相接,在三通29的右端口与风扇式散热器右侧38的出水口之间的管道上接有一液体电磁阀36。其中,风扇式散热器38连接可调速电机37,通过可调速电机37进行驱动;三通29的中间端口与LNG/柴油双燃料发动机20右侧的缸套水进水口之间通过管道连接,在三通29的中间端口与LNG/柴油双燃料发动机20右侧的缸套水进水口之间的连接管道上依次接有液体单向阀18、三通阀17、温度传感器27,其中,三通阀17的中间端口通过管道与发动机冷却系统小循环相接。在缸套冷却水循环系统中,温度传感器16、27、液体流量传感器14都通过信号线与模拟量输入模块相连,再接PLC控制器9;PLC控制器9通过控制线与放大器相连,之后分别接液体比例调节阀13、高温缸套水泵22、液体单向阀33、34、35、36以及风扇散热器38上的可调速电机37。 The liner cooling water circulation system includes a high-temperature liner water pump 22, a cooling water tank 19, an LNG/diesel dual-fuel engine 20, a plate heat exchanger 21, a fan radiator 38, and connecting pipes. The jacket water outlet on the left side of the LNG/diesel dual-fuel engine 20 is connected to the jacket water inlet on the top of the cooling water tank 19 through a pipeline, and the jacket water outlet of the LNG/diesel dual-fuel engine 20 and the cooling water tank 19 A temperature sensor 16, a three-way valve 15, a liquid flow sensor 14, and a liquid proportional regulating valve 13 are sequentially connected to the connecting pipes between the upper cylinder jacket water inlets. Wherein, the middle port of the three-way valve 15 is connected with the small circulation of the engine cooling system through a pipeline. The jacket water outlet at the bottom of the cooling water tank 19 is connected to the middle port of the tee between the liquid solenoid valve 33 and the liquid solenoid valve 34 through a pipeline, and the jacket water outlet at the bottom of the cooling water tank 19 is connected to the middle port of the tee. A high-temperature jacket water pump 22 is connected to the connecting pipeline between the ports. The upper port of the tee between the liquid solenoid valve 33 and the liquid solenoid valve 34 is connected to the high-temperature jacket water inlet on the upper left side of the plate heat exchanger 21, and the upper port of the tee is connected to the left side of the plate heat exchanger 21. The connection pipe between the high-temperature cylinder jacket water inlets on the upper side is connected to the liquid solenoid valve 34, the lower port of the tee is connected to the water inlet on the left side of the fan radiator 38, and the lower port of the tee is connected to the fan radiator. The pipeline between the water inlets on the left side of radiator 38 is connected with liquid electromagnetic valve 33. The high-temperature jacket water outlet on the lower right side of the plate heat exchanger 21 is connected to the left port of the tee 29 through a pipe, and between the high-temperature jacket water outlet on the lower right side of the plate heat exchanger 21 and the left port of the tee 29 A liquid solenoid valve 35 is connected to the pipeline between the three links. A liquid electromagnetic valve 36 is connected on the pipeline between the water outlets. Wherein, the fan radiator 38 is connected with the adjustable speed motor 37, and is driven by the adjustable speed motor 37; the middle port of the tee 29 is connected with the cylinder jacket water inlet on the right side of the LNG/diesel dual fuel engine 20 through a pipeline , a liquid check valve 18, a three-way valve 17, and a temperature sensor 27 are sequentially connected to the connecting pipe between the middle port of the tee 29 and the jacket water inlet on the right side of the LNG/diesel dual-fuel engine 20, wherein, The middle port of the three-way valve 17 is connected with the small circulation of the engine cooling system by a pipeline. In the cylinder liner cooling water circulation system, the temperature sensors 16, 27, and the liquid flow sensor 14 are all connected to the analog input module through signal lines, and then connected to the PLC controller 9; the PLC controller 9 is connected to the amplifier through the control line, and then respectively connected to the The speed-adjustable motor 37 on the liquid proportional regulating valve 13, the high-temperature cylinder jacket water pump 22, the liquid check valves 33, 34, 35, 36 and the fan radiator 38.
工质循环系统包括工质箱24、工质泵30和连接管道等。其中,工质箱24左侧下部是工质出口,工质箱24通过工质出口以及管道连接板式换热器21的右侧上部的工质进口,在工质箱24与板式换热器21之间的连接管道上依次接有液体比例调节阀32、液体流量传感器31、工质泵30、温度传感器28。板式换热器21左侧下部的工质出口与LNG气化器12下段侧部的工质进口之间通过管道连接,在板式换热器21左侧下部的工质出口与LNG气化器12下段侧部的工质进口之间的连接管道上接有一温度传感器26。LNG气化器12左侧上部的工质出口与工质箱24上部右侧的工质进口之间通过管道连接,在LNG气化器12左侧上部的工质出口与工质箱24上部右侧之间的连接管道上接有一温度传感器47,且温度传感器47尽量靠近LNG气化器12左侧上部的工质出口端。在工质箱24的上部接有一工质液位传感器23。在工质循环系统中,液体流量传感器31,温度传感器28、26、47、工质液位传感器23都通过信号线与模拟量输入模块相连,再接PLC控制器9;PLC控制器9通过控制线与放大器相连,之后分别接液体比例调节阀32、工质泵30。 The working medium circulation system includes a working medium tank 24, a working medium pump 30, connecting pipelines and the like. Wherein, the lower left side of the working medium box 24 is the working medium outlet, and the working medium box 24 is connected to the working medium inlet on the upper right side of the plate heat exchanger 21 through the working medium outlet and the pipeline, and between the working medium box 24 and the plate heat exchanger 21 The connecting pipelines are connected with a liquid proportional regulating valve 32 , a liquid flow sensor 31 , a working medium pump 30 and a temperature sensor 28 in sequence. The working medium outlet on the left lower part of the plate heat exchanger 21 is connected with the working medium inlet on the lower side of the LNG vaporizer 12 through a pipeline, and the working medium outlet on the left lower part of the plate heat exchanger 21 is connected to the LNG vaporizer 12 A temperature sensor 26 is connected to the connecting pipe between the working fluid inlets at the side of the lower section. The working medium outlet on the upper left side of the LNG gasifier 12 is connected with the working medium inlet on the upper right side of the working medium box 24 through a pipeline, and the working medium outlet on the upper left side of the LNG gasifier 12 is connected to the upper right side of the working medium box 24. A temperature sensor 47 is connected to the connecting pipe between the sides, and the temperature sensor 47 is as close as possible to the working medium outlet end on the upper left side of the LNG vaporizer 12 . A working fluid level sensor 23 is connected to the upper part of the working fluid tank 24 . In the working fluid circulation system, the liquid flow sensor 31, the temperature sensors 28, 26, 47, and the working fluid level sensor 23 are all connected to the analog input module through signal lines, and then connected to the PLC controller 9; the PLC controller 9 controls the The line is connected to the amplifier, and then connected to the liquid proportional regulating valve 32 and the working medium pump 30 respectively.
LNG供给气化系统包括LNG泵39、LNG气化器12、辅助LNG储罐42、闪蒸汽储罐45、异径三通10、天然气稳压气罐2、燃气滤清器6、天然气/空气混合器7、发动机气缸8以及连接管道等。其中,辅助LNG储罐42与LNG气化器12底端的LNG进口之间通过管道连接,在辅助LNG储罐42与LNG气化器12底端的LNG进口之间的连接管道上依次接有手动调节阀40、LNG泵39、液体流量传感器29、液体比例调节阀25。LNG气化器12顶端的气态天然气出口与天然气稳压气罐2底部的气态天然气进口之间通过管道连接,在LNG气化器12顶端的气态天然气出口与天然气稳压气罐2底部的气态天然气进口之间的连接管道上依次接有温度传感器48、气体单向阀11、异径三通10。其中异径三通10的中间端口与闪蒸汽储罐45的上部端口之间通过管道连接,在异径三通10的中间端口与闪蒸汽储罐45的上部端口之间的连接管道上装有一气体电磁阀1。在闪蒸汽储罐45的顶端装有一压力传感器46。辅助LNG储罐42左侧上部与闪蒸汽储罐45的底部之间通过管道连接,在辅助LNG储罐42左侧上部与闪蒸汽储罐45的底部之间的连接管道上装有一气体单向阀44。燃气滤清器6与天然气稳压气罐2顶部之间通过管道连接,在燃气滤清器6与天然气稳压气罐2顶部之间的连接管道上依次接有手动调节阀4、气体比例调节阀5,其中,天然气稳压气罐2的顶部装有一压力传感器3。燃气滤清器6与天然气/空气混合器7之间通过管道连接,天然气/空气混合器7与发动机气缸8之间通过管道连接。在LNG供给气化系统中,液体流量传感器29,温度传感器48、液位传感器43、压力传感器3都通过信号线与模拟量输入模块相连,再接PLC控制器9;PLC控制器9通过控制线与放大器相连,之后分别接液体比例调节阀25、LNG泵39、气体电磁阀1、气体比例调节阀5。 The LNG supply gasification system includes LNG pump 39, LNG vaporizer 12, auxiliary LNG storage tank 42, flash steam storage tank 45, reducing tee 10, natural gas regulator tank 2, gas filter 6, natural gas/air Mixer 7, engine cylinder 8 and connecting pipes, etc. Wherein, the auxiliary LNG storage tank 42 is connected with the LNG inlet at the bottom end of the LNG vaporizer 12 through a pipeline, and the connecting pipeline between the auxiliary LNG storage tank 42 and the LNG inlet at the bottom end of the LNG vaporizer 12 is sequentially connected with a manual adjustment Valve 40, LNG pump 39, liquid flow sensor 29, liquid proportional regulating valve 25. The gaseous natural gas outlet at the top of the LNG vaporizer 12 is connected with the gaseous natural gas inlet at the bottom of the natural gas regulator tank 2 through a pipeline, and the gaseous natural gas outlet at the top of the LNG gasifier 12 is connected with the gaseous natural gas at the bottom of the natural gas regulator tank 2 A temperature sensor 48, a gas one-way valve 11, and a tee with different diameters 10 are sequentially connected to the connecting pipeline between the inlets. Among them, the middle port of the reducing tee 10 and the upper port of the flash steam storage tank 45 are connected by a pipeline, and a gas is installed on the connecting pipe between the middle port of the reducing tee 10 and the upper port of the flash steam storage tank 45. Solenoid valve 1. A pressure sensor 46 is installed on the top of the flash gas storage tank 45 . The upper left side of the auxiliary LNG storage tank 42 is connected to the bottom of the flash gas storage tank 45 through a pipeline, and a gas check valve is installed on the connecting pipeline between the upper left side of the auxiliary LNG storage tank 42 and the bottom of the flash gas storage tank 45 44. The gas filter 6 is connected to the top of the natural gas regulator tank 2 through a pipeline, and the connection pipeline between the gas filter 6 and the top of the natural gas regulator tank 2 is sequentially connected with a manual regulating valve 4 and a gas ratio regulator. Valve 5, wherein a pressure sensor 3 is installed on the top of the natural gas regulator tank 2. The gas filter 6 is connected to the natural gas/air mixer 7 through pipelines, and the natural gas/air mixer 7 is connected to the engine cylinder 8 through pipelines. In the LNG supply gasification system, the liquid flow sensor 29, the temperature sensor 48, the liquid level sensor 43, and the pressure sensor 3 are all connected to the analog input module through the signal line, and then connected to the PLC controller 9; the PLC controller 9 is connected through the control line It is connected to the amplifier, and then respectively connected to the liquid proportional regulating valve 25, the LNG pump 39, the gas solenoid valve 1, and the gas proportional regulating valve 5.
PLC控制系统包括温度传感器16、液体比例调节阀13、液体流量传感器14、温度传感器27、液体比例调节阀32、液体流量传感器31、温度传感器28、温度传感器26、工质液位传感器23、LNG液位传感器43、液体流量传感器30、液体比例调节阀25、气体比例调节阀5、气体电磁阀1、气体压力传感器46、液体电磁阀33,34,35,36、可调速电机37、PLC控制器9、温度传感器47、温度传感器48和连接线路等。 PLC control system includes temperature sensor 16, liquid proportional regulating valve 13, liquid flow sensor 14, temperature sensor 27, liquid proportional regulating valve 32, liquid flow sensor 31, temperature sensor 28, temperature sensor 26, working fluid level sensor 23, LNG Liquid level sensor 43, liquid flow sensor 30, liquid proportional regulating valve 25, gas proportional regulating valve 5, gas solenoid valve 1, gas pressure sensor 46, liquid solenoid valves 33, 34, 35, 36, adjustable speed motor 37, PLC Controller 9, temperature sensor 47, temperature sensor 48 and connection lines etc.
传统的发动机采用节温器可以根据冷却水的温度高低自动调节进入散热器的水量,以保证发动机在合适的温度范围工作。本发明对发动机冷启动过程采用温度传感器16和流量传感器14、液体比例调节阀13和PLC控制系统来完成,即由LNG/柴油双燃料发动机20与三通阀17及三通阀15其他部件实现缸套冷却水的小循环,温度传感器16检测缸套出水口的水温,当水温慢慢达到或超过75℃时,此时小循环不再满足发动机的冷却要求,这时就要逐渐进入冷却水系统大循环,由于此时温差比较小,换热效果不明显,板式换热器21不能为LNG气化提供足够的热量,因此设置只有在缸套出水口温度达到90℃时,才开始采用板式换热器21进行换热,出口缸套水温度在75℃与90℃之间时,系统以风扇散热器38将中高温缸套水的热量排掉,散热后的缸套冷却水回到循环管路中。 The traditional engine uses a thermostat to automatically adjust the amount of water entering the radiator according to the temperature of the cooling water to ensure that the engine works in a suitable temperature range. The present invention adopts temperature sensor 16 and flow sensor 14, liquid proportional regulating valve 13 and PLC control system to finish to engine cold start process, promptly is realized by LNG/diesel dual-fuel engine 20 and three-way valve 17 and three-way valve 15 other components The small circulation of the cylinder liner cooling water, the temperature sensor 16 detects the water temperature of the water outlet of the cylinder liner, when the water temperature gradually reaches or exceeds 75°C, the small circulation no longer meets the cooling requirements of the engine, and the cooling water will gradually enter The system has a large cycle, because the temperature difference is relatively small at this time, the heat transfer effect is not obvious, and the plate heat exchanger 21 cannot provide enough heat for LNG gasification, so the plate heat exchanger is only used when the water outlet temperature of the cylinder liner reaches 90°C. The heat exchanger 21 performs heat exchange. When the outlet jacket water temperature is between 75°C and 90°C, the system uses the fan radiator 38 to discharge the heat of the medium and high temperature jacket water, and the jacket cooling water returns to the circulation after heat dissipation. In pipeline.
在缸套出水口温度介于75℃到90℃之间时,此时PLC控制器9控制液体电磁阀34、35都处于关闭状态,而控制液体电磁阀33、36处于开启状态,此时缸套冷却水泵22将高温缸套水从缸套出水口输送到风扇式散热器38中进行放热,降温后的缸套冷却水经液体单向阀18流回到发动机的缸套内吸热,可调速电机37可以调节风扇转速以调节散热量的大小。当缸套出水口温度在大于等于90℃时,此时,PLC控制器9控制液体电磁阀34、35都处于开启状态,而液体电磁阀33、36处于关闭状态,缸套水泵22将高温缸套冷却水从缸套出水口输送到板式换热器21中向工质放热,在此与工质进行热交换,放热后的冷却水温度降低, 经液体单向阀18再次回到缸套内吸收热量,以此循环流动。驱使缸套冷却水循环流动的是缸套水泵22,冷却水箱19用于存储多余或补充不足冷却水。液体单向阀18的作用是防止冷却水小循环回路中的冷却水倒流回板式换热器21或风扇式散热器38中,促使冷却水只能在大循环内单向流动。 When the water outlet temperature of the cylinder liner is between 75°C and 90°C, the PLC controller 9 controls the liquid solenoid valves 34 and 35 to be in the closed state, and the control liquid solenoid valves 33 and 36 are in the open state. The jacket cooling water pump 22 transports the high-temperature jacket water from the outlet of the jacket to the fan radiator 38 for heat release, and the cooled jacket cooling water flows back to the cylinder jacket of the engine through the liquid check valve 18 to absorb heat. The speed-adjustable motor 37 can adjust the fan speed to adjust the heat dissipation. When the water outlet temperature of the cylinder liner is greater than or equal to 90°C, at this time, the PLC controller 9 controls the liquid solenoid valves 34, 35 to be in the open state, while the liquid solenoid valves 33, 36 are in the closed state, and the liner water pump 22 will turn the high temperature cylinder The jacket cooling water is transported from the water outlet of the cylinder liner to the plate heat exchanger 21 to release heat to the working medium, where heat exchange is performed with the working medium, and the temperature of the cooling water after heat release decreases, and then returns to the cylinder through the liquid check valve 18 The heat is absorbed in the sleeve, and the flow is circulated in this way. It is the cylinder jacket water pump 22 that drives the cylinder jacket cooling water to circulate, and the cooling water tank 19 is used to store excess or replenish insufficient cooling water. The effect of the liquid check valve 18 is to prevent the cooling water in the cooling water small circulation loop from flowing back into the plate heat exchanger 21 or the fan radiator 38, so that the cooling water can only flow in one direction in the large circulation.
冷却水在大循环流动后,PLC控制器9给工质泵30指令启动,将工质从工质箱24中泵出,从板式换热器21吸热后到LNG气化器12中放热。放热后工质温度降低,通过管道再次流向板式换热器21从缸套冷却水内吸收热量,以此循环流动,循环流动阻力依靠工质泵30来克服。工质箱24储存多余的或补充不足的工质。LNG泵39驱使LNG辅助LNG储罐42流向LNG气化器12,并在此从工质吸收热量气化成天然气,天然气储存于天然气稳压罐2内,天然气经燃气滤清器6滤清后在天然气/空气混合器7内混合成可燃混合气,吸入气缸内燃烧作功。发动机气缸8仅用柴油工作时,高温缸套冷却水不流经板式换热器21,而是流经风扇式散热器38,降温后的冷却水再次流向发动机缸套,而工质和LNG气化器12不参与工作。其中,液体流量传感器31的作用是测量工质管路的流量,温度传感器47的作用是检测LNG气化器12中工质出口处的温度值,液体比例调节阀32的作用是控制工质流量的大小。板式换热器21的工质入口与出口端分别装有一温度传感器26和温度传感器28,分别用来测量板式换热器21的工质入口与出口端的温度值。工质箱24上方装有一工质液位传感器23用于监控工质箱24中工质的液面高度。 After the cooling water flows in the large circulation, the PLC controller 9 instructs the working medium pump 30 to start, pumps the working medium out of the working medium tank 24, and releases heat from the plate heat exchanger 21 to the LNG vaporizer 12 after absorbing heat . After the heat release, the temperature of the working medium decreases, and it flows to the plate heat exchanger 21 again through the pipeline to absorb heat from the cooling water of the cylinder liner, and circulates in this way, and the circulation flow resistance is overcome by the working medium pump 30 . The working fluid box 24 stores surplus or insufficient working fluid. The LNG pump 39 drives the LNG auxiliary LNG storage tank 42 to flow to the LNG gasifier 12, where it absorbs heat from the working medium and gasifies it into natural gas. The natural gas is stored in the natural gas surge tank 2, and the natural gas is filtered by the gas filter 6. The natural gas/air mixer 7 is mixed into a combustible mixture, which is inhaled into the cylinder to burn for work. When the engine cylinder 8 only works with diesel oil, the high-temperature cylinder liner cooling water does not flow through the plate heat exchanger 21, but flows through the fan radiator 38, and the cooled cooling water flows to the engine cylinder liner again, while the working fluid and LNG gas Converter 12 is not involved in the work. Wherein, the function of the liquid flow sensor 31 is to measure the flow rate of the working medium pipeline, the function of the temperature sensor 47 is to detect the temperature value at the outlet of the working medium in the LNG vaporizer 12, and the function of the liquid proportional regulating valve 32 is to control the flow rate of the working medium the size of. A temperature sensor 26 and a temperature sensor 28 are respectively installed at the inlet and outlet of the plate heat exchanger 21 for measuring the temperature values of the inlet and outlet of the plate heat exchanger 21 . A working fluid level sensor 23 is installed above the working medium box 24 for monitoring the liquid level of the working medium in the working medium box 24 .
冷却水在大循环流动后,LNG泵39将LNG从辅助LNG储罐42中抽出进入LNG气化器12,并在LNG气化器12中吸收工质的热量,并使LNG气化成天然气,后经气体单向阀11储存于天然气稳压气罐2中,为防止天然气回流设有气体单向阀11。天然气稳压气罐2为LNG/柴油双燃料发动机20存储稳定压力的天然气,天然气经燃气滤清器6滤清后与空气在天然气/空气混合器7中形成可燃混合气,吸入发动机气缸8中燃烧作功。为了实时检测LNG流量设有流量传感器29,而温度传感器48检测LNG气化器12出气口气温,气体比例调节阀5的作用是控制天然气的流量,手动调节阀40的作用是手动调节LNG管路中LNG的通断,手动调节阀4的作用是手动调节天然气在管路中的通断,当系统发生故障时工作人员可以及时的关闭手动调节阀40与手动调节阀4,以防止危险情况的发生,在PLC控制器9运行正常的情况下手动调节阀40与手动调节阀4是常开的,并且开度最大。天然气稳压气罐2上方安装压力传感器3,它的作用是测量天然气稳压气罐2中的气体压力。在辅助LNG储罐42设有液位传感器43,它的作用是测量辅助LNG储罐42中LNG液面高度。由于辅助LNG储罐42中的LNG会产生蒸发,这部分气体被称为BOG闪蒸汽,BOG闪蒸汽使LNG储罐42气象空间压力升高,这部分BOG闪蒸汽通过气体单向阀44进入到闪蒸汽储罐45中,气体单向阀44的作用是防止闪蒸汽倒回辅助LNG储罐42中,闪蒸汽储罐45经异径三通10与天然气稳压气罐2相连接,这样可以使闪蒸汽进去到天然气稳压气罐2中去,在闪蒸汽储罐45与异径三通10之间有气体电磁阀1,它的作用是控制闪蒸汽进入到天然气稳压灌2的通与断,在闪蒸汽储罐45的上方设有压力传感器46,它的作用是测量闪蒸汽储罐45中天然气的压力。在LNG气化系统中,分别在闪蒸汽储罐45两端管口法兰处、LNG泵39的两端管口法兰处、辅助LNG储罐42与LNG泵39之间的接口法兰连接处、LNG气化器12的气体进出口的管口法兰连接处、天然气稳压气罐2的出口法兰连接处以及闪蒸汽储罐45两端管口法兰处均装有一天然气泄漏报警器41,在LNG泵39的两端管口法兰处分别装有一天然气泄漏报警器41,在闪蒸汽储罐45与LNG泵39之间的接口法兰处也接有一天然气泄漏报警器41,在LNG气化器12的气体进出口的管口法兰处也分别装有一天然气泄漏报警器41,报警器的作用是当天然气发生泄漏时,工作人员可以及时发现,并及时作出相应措施。 After the cooling water flows in a large circulation, the LNG pump 39 pumps LNG from the auxiliary LNG storage tank 42 into the LNG vaporizer 12, and absorbs the heat of the working fluid in the LNG vaporizer 12, and vaporizes the LNG into natural gas. The gas is stored in the natural gas pressure-stabilized gas tank 2 through the gas check valve 11, and a gas check valve 11 is provided to prevent natural gas from flowing back. The natural gas stabilized gas tank 2 stores natural gas at a stable pressure for the LNG/diesel dual-fuel engine 20. After the natural gas is filtered by the gas filter 6, it forms a combustible mixture with air in the natural gas/air mixer 7 and is sucked into the engine cylinder 8. Combustion works. In order to detect the LNG flow in real time, a flow sensor 29 is provided, and a temperature sensor 48 detects the air temperature at the gas outlet of the LNG vaporizer 12. The function of the gas ratio regulating valve 5 is to control the flow of natural gas, and the function of the manual regulating valve 40 is to manually adjust the LNG pipeline. The function of manual control valve 4 is to manually adjust the on-off of natural gas in the pipeline. When the system fails, the staff can close the manual control valve 40 and manual control valve 4 in time to prevent dangerous situations. When the PLC controller 9 operates normally, the manual control valve 40 and the manual control valve 4 are normally open, and the opening degree is the largest. A pressure sensor 3 is installed above the natural gas stabilizing gas tank 2, and its function is to measure the gas pressure in the natural gas stabilizing gas tank 2. The auxiliary LNG storage tank 42 is provided with a liquid level sensor 43 whose function is to measure the liquid level of LNG in the auxiliary LNG storage tank 42 . Since the LNG in the auxiliary LNG storage tank 42 will evaporate, this part of the gas is called BOG flash steam, and the BOG flash steam increases the pressure of the meteorological space of the LNG storage tank 42, and this part of the BOG flash steam enters through the gas check valve 44 In the flash steam storage tank 45, the function of the gas check valve 44 is to prevent the flash steam from falling back into the auxiliary LNG storage tank 42, and the flash steam storage tank 45 is connected with the natural gas pressure stabilizing gas tank 2 through the reducing tee 10, so that Let the flash steam go into the natural gas regulator tank 2, and there is a gas solenoid valve 1 between the flash steam storage tank 45 and the different-diameter tee 10, and its function is to control the passage of the flash steam into the natural gas regulator tank 2. In addition, a pressure sensor 46 is arranged above the flash steam storage tank 45 , and its function is to measure the pressure of the natural gas in the flash steam storage tank 45 . In the LNG gasification system, the nozzle flanges at both ends of the flash gas storage tank 45, the nozzle flanges at both ends of the LNG pump 39, and the interface flanges between the auxiliary LNG storage tank 42 and the LNG pump 39 A natural gas leakage alarm is installed at the nozzle flange connection of the gas inlet and outlet of the LNG vaporizer 12, the outlet flange connection of the natural gas pressure regulator tank 2, and the nozzle flanges at both ends of the flash gas storage tank 45. A natural gas leakage alarm 41 is respectively installed at the nozzle flanges at both ends of the LNG pump 39, and a natural gas leakage alarm 41 is also connected at the interface flange between the flash steam storage tank 45 and the LNG pump 39, A natural gas leakage alarm 41 is also respectively installed at the nozzle flange of the gas inlet and outlet of the LNG vaporizer 12. The effect of the alarm is that when the natural gas leaks, the staff can find out in time and take corresponding measures in time.
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Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106828859A (en) * | 2017-01-20 | 2017-06-13 | 中国船舶重工集团公司第七研究所 | For the liquified natural gas gasification heating system of ship |
CN107448305A (en) * | 2017-09-25 | 2017-12-08 | 百发动力(无锡)有限公司 | A kind of double fuel engine unit control system and its control method |
CN107489529A (en) * | 2017-08-25 | 2017-12-19 | 浙江海洋大学 | A kind of inlet duct of LNG gas turbines steam combined cycle power generating |
CN108699945A (en) * | 2015-12-17 | 2018-10-23 | 日立汽车系统株式会社 | Cooling device and control method for vehicle internal combustion engine |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008157457A (en) * | 2006-12-22 | 2008-07-10 | Man Diesel Se | Gas supply device for drive machine |
CN102235269A (en) * | 2010-04-27 | 2011-11-09 | 潍柴动力股份有限公司 | Fuel supply system and vehicle system comprising same |
KR20120059350A (en) * | 2011-09-27 | 2012-06-08 | 에스티엑스조선해양 주식회사 | Liquefied Natural Gas Supply System for Marine Vessel or Offshore Plant |
CN102996194A (en) * | 2012-12-06 | 2013-03-27 | 西安交通大学 | Comprehensive energy recycling system based on liquefied natural gas automobile |
CN103557071A (en) * | 2013-10-25 | 2014-02-05 | 张毅 | System and method for utilizing gas cold energy to improve engine heat efficiency and achieve aims of saving energy and reducing emission |
CN103899440A (en) * | 2014-03-11 | 2014-07-02 | 哈尔滨工程大学 | Ship gas/dual fuel engine LNG gasifying system based on exhaust energy recycling and control method thereof |
CN203730162U (en) * | 2013-12-24 | 2014-07-23 | 山东大学 | Inlet gas temperature control system of liquefied natural gas engine |
-
2015
- 2015-01-28 CN CN201510041519.9A patent/CN104595063B/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008157457A (en) * | 2006-12-22 | 2008-07-10 | Man Diesel Se | Gas supply device for drive machine |
CN102235269A (en) * | 2010-04-27 | 2011-11-09 | 潍柴动力股份有限公司 | Fuel supply system and vehicle system comprising same |
KR20120059350A (en) * | 2011-09-27 | 2012-06-08 | 에스티엑스조선해양 주식회사 | Liquefied Natural Gas Supply System for Marine Vessel or Offshore Plant |
CN102996194A (en) * | 2012-12-06 | 2013-03-27 | 西安交通大学 | Comprehensive energy recycling system based on liquefied natural gas automobile |
CN103557071A (en) * | 2013-10-25 | 2014-02-05 | 张毅 | System and method for utilizing gas cold energy to improve engine heat efficiency and achieve aims of saving energy and reducing emission |
CN203730162U (en) * | 2013-12-24 | 2014-07-23 | 山东大学 | Inlet gas temperature control system of liquefied natural gas engine |
CN103899440A (en) * | 2014-03-11 | 2014-07-02 | 哈尔滨工程大学 | Ship gas/dual fuel engine LNG gasifying system based on exhaust energy recycling and control method thereof |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108699945B (en) * | 2015-12-17 | 2020-10-09 | 日立汽车系统株式会社 | Cooling device and control method for internal combustion engine for vehicle |
CN108699945A (en) * | 2015-12-17 | 2018-10-23 | 日立汽车系统株式会社 | Cooling device and control method for vehicle internal combustion engine |
CN106828859A (en) * | 2017-01-20 | 2017-06-13 | 中国船舶重工集团公司第七研究所 | For the liquified natural gas gasification heating system of ship |
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CN107448305A (en) * | 2017-09-25 | 2017-12-08 | 百发动力(无锡)有限公司 | A kind of double fuel engine unit control system and its control method |
CN107448305B (en) * | 2017-09-25 | 2023-05-12 | 百发动力(无锡)有限公司 | Dual-fuel generator set control system and control method thereof |
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CN109878680A (en) * | 2019-02-28 | 2019-06-14 | 哈尔滨工程大学 | A gas-electric parallel ship hybrid power system with LNG cooling |
CN109878685A (en) * | 2019-02-28 | 2019-06-14 | 哈尔滨工程大学 | A gas-electric hybrid ship hybrid power system with LNG cooling |
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RU2820608C1 (en) * | 2023-11-16 | 2024-06-06 | Общество с ограниченной ответственностью "ЛИНОЛИТ" | Concrete finishing trowel |
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