2023
DOI: 10.1016/j.enconman.2023.117349
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Advanced natural gas liquefaction and regasification processes: Liquefied natural gas supply chain with cryogenic carbon capture and storage

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Cited by 14 publications
(5 citation statements)
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“…Thus, the heat input is less than ¼ of the total heat generated in the proposed thermodynamic LNG regasification cycle. The use of secondary low-temperature heat sources as a hot heat source (cooling water or engine exhaust gases) will significantly reduce the cost of the LNG regasification process and increase the capacity and efficiency of the thermodynamic regasification cycle of all liquefied gases transported by sea [16][17][18]. Lrt us Calculate the theoretical mechanical capacity of a conditional terminal with a capacity of 1.0 billion nm 3 /year equipped with a device manufactured in accordance with the proposed thermodynamic regasification cycle.…”
Section: Fig 1 Thermodynamic Cycle Of Liquefied Gas Regasification Wi...mentioning
confidence: 99%
“…Thus, the heat input is less than ¼ of the total heat generated in the proposed thermodynamic LNG regasification cycle. The use of secondary low-temperature heat sources as a hot heat source (cooling water or engine exhaust gases) will significantly reduce the cost of the LNG regasification process and increase the capacity and efficiency of the thermodynamic regasification cycle of all liquefied gases transported by sea [16][17][18]. Lrt us Calculate the theoretical mechanical capacity of a conditional terminal with a capacity of 1.0 billion nm 3 /year equipped with a device manufactured in accordance with the proposed thermodynamic regasification cycle.…”
Section: Fig 1 Thermodynamic Cycle Of Liquefied Gas Regasification Wi...mentioning
confidence: 99%
“…Cooled air expands in a Joule-Thompson (J-T) valve, resulting in a two-phase fluid (4)(5). Liquefied air ( 8) is separated and stored, and the gas portion of the mixture (7) is sent back to the system. In real applications, no process can be completely isentropic.…”
Section: Linde-hampson Cyclementioning
confidence: 99%
“…where m comp is the mass flow rate of the gas; T 0 is the ambient temperature; s lq and h lq are the specific entropy and enthalpy of the liquefied gas, respectively; and s 0 and h 0 are the specific entropy and enthalpy of the gas, respectively, at ambient conditions. As all the gas entering the compressor is liquefied, the cooling effect (Q lq ) could be expressed as given in Equation (7).…”
Section: Performance Indicators and Validationmentioning
confidence: 99%
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“…Cryogenic could be the first choice due to its advantages, i.e., it is environmentally friendly, has physical separation without any harmful solvents, and is applicable for a large range of compositions of natural gas with CO 2 . , However, many challenges still exist because it requires a substantial cooling duty . Achieving the low temperatures necessary for efficient phase separation requires significant energy requirements, often leading to an expensive process.…”
Section: Introductionmentioning
confidence: 99%