Design and Optimization of Pressurized Liquefaction Processes for Offshore Natural Gas Using Two-Stage Cascade Refrigeration Cycles

Abstract

Because of increasing interests in offshore natural gas and due to limited deck space, simpler liquefied natural gas processes are necessary. The aim of this paper is to develop three pressurized liquefaction processes using two-stage cascade refrigeration cycles instead of the conventional three-stage refrigeration cycles. The proposed processes are CH4–C2H6, CH4–C2H4, and C2H4–C3H8 processes. Taking the specific energy consumption as the objective function, simulation based optimization is conducted for the three novel processes as well as two conventional cascade processes by a sequential search method. Optimization results show that the C2H4–C3H8 process is the most efficient one with a specific energy consumption of 0.2089 kWh/Nm3, 22% less than that of the conventional CH4–C2H4–C3H8 process. Moreover, a detailed thermodynamic analysis is carried out for the five processes. The thermodynamic analysis results confirm that the C2H4–C3H8 process presents the best composite curve match and the highest coefficient of performance. The CH4–C2H6 process requires the smallest heat transfer area, 70% less than that of the conventional CH4–C2H6–C3H8 process. The CH4–C2H4 process uses the least amount of key equipment, 35% less than that of the conventional CH4–C2H4–C3H8 process. In addition, an exergy analysis is performed for all processes and the results indicate that further improvements are requested the most in valves and heat exchangers, respectively, for the conventional and novel processes.

Shuffled Complex Evolution-Based Performance Enhancement and Analysis of Cascade Liquefaction Process for Large-Scale LNG Production

“…In a similar study, Ghorbani et al [29], integrated NGL recovery with LNG process while replacing absorption refrigeration system in lieu of precooling stage of MFC to lower required energy consumption. Lin et al [30] designed and optimized the two-stage cascade processes for pressurized LNG production. They conducted simulation-based optimization to find the optimal design corresponding to minimal energy consumption.…”

Special Issue on PSE Advances in Natural Gas Value Chain: Editorial

“…They find SMR to be the best option for LNG plant capacities of 1.0−2.2 MTPA, DMR for 2.2−4.0 MTPA, and C3MR for 4.0−7.0 MTPA. Lin et al9 propose and optimize three simpler two-stage cascade refrigeration cycles (methane−ethane, methane−ethylene, and ethylene−propane) for NG liquefaction and compare them with two conventional three-stage cascade processes. Among the five LNG processes, their ethane−propane cycle consumes the least amount of energy (KWh/Nm 3 ) and exhibits the highest coefficient of performance.…”