Abstract
This paper describes data of an integrated process, cryogenic energy storage system combined with liquefied natural gas (LNG) regasification process. The data in this paper is associated with the article entitled “Conceptual Design and Exergy Analysis of Combined Cryogenic Energy Storage and LNG Regasification Processes: Cold and Power Integration” (Lee et al., 2017) [1]. The data includes the sensitivity case study dataset of the air flow rate and the heat exchanging feasibility data by composite curves. The data is expected to be helpful to the cryogenic energy process development.
Highlights
Data on conceptual design of cryogenic energy storage system combined with liquefied natural gas regasification process
This paper describes data of an integrated process, cryogenic energy storage system combined with liquefied natural gas (LNG) regasification process
Data In this data article, we share sensitivity analysis data of the cryogenic energy storage system combined with liquefied natural gas (LNG) regasification process
Summary
The increase of the air flow rate causes decrease of the minimum temperature difference of the heat exchanger. The pinch point can be shown at the inlet or outlet and inside the heat exchanger when the phase changing occurs. In this data article, we share sensitivity analysis data of the cryogenic energy storage system combined with liquefied natural gas (LNG) regasification process. We share sensitivity analysis data of the cryogenic energy storage system combined with liquefied natural gas (LNG) regasification process In this data, the case study simulation results by air flow rate and the heat exchanging composite curves are illustrated
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