Techno-economic Analysis of Acid Gas Removal and Liquefaction for Pressurized LNG

• Published in: IOP conference series. Materials Science and Engineering 2018-05, Vol.358 (1), p.12066
• Main Authors: Lee, S H, Seo, Y K, Chang, D J
• Format: Article
• Language: English
• Subjects: Acids; Aqueous solutions; Carbon dioxide; Diethanolamine; Economic analysis; High temperature; Life cycle assessment; Life cycle costs; Liquefaction; Liquefied natural gas
• ISSN: 1757-8981; 1757-899X
• DOI: 10.1088/1757-899X/358/1/012066

This study estimated the life cycle cost (LCC) of an acid gas removal and a liquefaction processes for Pressurized LNG (PLNG) production and compared the results with the cost of normal LNG production. PLNG is pressurized LNG that is liquefied at a higher pressure and temperature than normal LNG. Due to the high temperature, the energy for liquefaction is reduced. The allowable CO2 concentration in PLNG is increased up to 3 mol% when the product pressure 25 bar. An amine process with 35 wt% of diethanolamine (DEA) aqueous solution and a nitrogen expansion cycle were selected for the acid gas removal and the liquefaction processes, respectively. Two types of CO2 concentration in the feed gas were investigated to analyze their impacts on the acid gas removal unit. When the CO2 concentration was 5 mol%, the acid gas removal unit was required for both LNG and PLNG production. However, the acid gas removal unit was not necessary in PLNG when the concentration was 0.5 mol% and the pressure was higher than 15 bar. The results showed that the LCC of PLNG was reduced by almost 35% relative to that of LNG when the PLNG pressure was higher than 15 bar.