摘要:
Provided is a piston ring (20) including: a low-pressure side ring (21) having a low-pressure side abutment (21a); and a high-pressure side ring (22) having a high-pressure side abutment (22a), the low-pressure side ring (21) and the high-pressure side ring (22) are arranged stacked in a direction along the axis (X) so that the high-pressure side ring (22) is closer to a fluid to be compressed, a low-pressure side rotation restriction part configured to restrict rotation in the circumferential direction (CD) relative to the piston is formed to the low-pressure side ring (21), a high-pressure side rotation restriction part (22b) configured to restrict rotation in the circumferential direction (CD) relative to the piston and a low-pressure side protrusion (22c) protruding toward the low-pressure side ring (21) and inserted in the low-pressure side abutment (21a) are formed to the high-pressure side ring (22), and the low-pressure side protrusion (22c) is inserted in the low-pressure side abutment (21a) with clearances being provided in both sides in the circumferential direction (CD) between the low-pressure side ring (21) and the low-pressure side protrusion (22c).
摘要:
A liquefied-gas vaporizer to be installed in a ship is an Open-Rack-type liquefied-gas vaporizer equipped with vertically-installed heat exchange panels (6) and troughs (10A and 10B) that are installed at top side portions thereof and that make a heating-medium fluid (W) overflow from overflow openings (18) so as to flow on the heat exchange panels, thus gasifying liquefied gas in heat transfer pipes (5), and the overflow openings of the troughs have edge portions (18a) that are disposed adjacent to the heat exchange panels and that the heating-medium fluid (W) flows over to the exterior when overflowing from the overflow openings and edge portions (18b) that are positioned on the opposite side from the heat exchange panels with the edge portions (18a) positioned therebetween, and the height of the edge portions (18b) in the vertical direction is greater than the height of the edge portions (18a) in the vertical direction.
摘要:
The purpose of the present invention is to use a compact configuration to economically vaporize a liquefied gas by effectively utilizing boil-off gas in a liquefied-gas tank, without having to take in any sea water. A liquefied-gas vaporization system (1) is provided with: a liquefied-gas vaporization unit (2) in which a liquefied gas stored in a liquefied-gas tank is subjected to heat exchange with a heat medium, and vaporized; a boil-off-gas combustion unit (3) which induces combustion of a boil-off gas of the liquefied gas; a turbine (4) which is rotationally driven by the energy of a combustion gas obtained after combustion has been performed in the boil-off-gas combustion unit (3); and a combustion-gas supply unit (8) which supplies, as the heat medium, to the liquefied-gas vaporization unit (2), the combustion gas discharged from the turbine (4). The boil-off-gas combustion unit (3) is a pressurized combustion unit which has compressed air supplied thereto, and in which the boil-off gas is subjected to pressurized combustion. A compressor (5), which generates the compressed air and supplies the compressed air to the boil-off-gas combustion unit (3) as air for pressurized combustion, is provided on the same axis as that of the turbine (4).
摘要:
A low-temperature slush fluid production apparatus that attains an increase of weight solidification ratio of slush fluid. There is provided low-temperature slush fluid production apparatus (1) comprising heat exchanger (12) with heat transfer plane (11) disposed in low-temperature fluid (L) of liquid form held within vessel (10); slush fluid production unit (2) equipped with scraping means (13) for scraping off any low-temperature fluid of solid form produced on the surface of the heat transfer plane (11); and extremely low temperature fluid generating unit (3) adapted to supply an extremely low temperature fluid whose temperature is lower than that of the low-temperature fluid (L) of liquid form held within the vessel (10) to the inside of the heat transfer plane (11), wherein not only the flow rate and temperature of the extremely low temperature fluid flowing into the inside of the heat transfer plane (11) but also the rotational speed or reciprocation speed of the scraping means (13) is regulated in accordance with the particle diameter of low-temperature fluid of solid form scraped off by the scraping means (13).
摘要:
The efficiency of a direct-injection diesel engine system that uses a low-temperature liquid fuel, such as LNG is improved by effectively utilizing the cooling energy of a high-pressure low-temperature liquid fuel. The system that uses high-pressure natural gas and combusts the engine fuel with intake air pressurized by a supercharger 30 includes a booster pump 3 that injects the high-pressure natural gas into a cylinder of the direct-injection diesel engine and pressurizes low-pressure liquefied natural gas introduced from an LNG tank 1; a cooling-energy recovery heat exchanger 51 that conducts heat exchange between a heat medium in a closed circuit and the high-pressure liquefied natural gas pressurized by the booster pump; and an air-cooling heat exchanger 54 that conducts heat exchange with the heat medium downstream of the cooling-energy recovery heat exchanger to cool air to be introduced into the supercharger and/or intake air compressed by the supercharger.
摘要:
A low-temperature-slush-fluid producing apparatus capable of achieving an increased weight solidification rate of slush fluid is provided. A low-temperature-slush-fluid producing apparatus 1 includes a slush-fluid producing unit 2 that includes a heat exchanger 12 having a heat-transfer surface 11 and disposed in a liquid-phase low-temperature fluid L stored in a container 10 and scraping means 13 for scraping a solid-phase low-temperature fluid formed on a surface of the heat-transfer surface 11; and a cryogenic-fluid generating unit 3 for supplying into the interior of the heat-transfer surface 11 a cryogenic fluid having a lower temperature than the liquid-phase low-temperature fluid L stored in the container 10. The low-temperature-slush-fluid producing apparatus 1 is configured so that the flow rate and temperature of the cryogenic fluid flowing into the interior of the heat-transfer surface 11 and the rotational speed or reciprocating speed of the scraping means 13 can be adjusted based on the particle size of the solid-phase low-temperature fluid scraped by the scraping means 13.