Samira Ahmadi - موسسه آموزش عالی آزاد پژوهش، تهران، ایران
Nargess Eyvazi-Abhari - موسسه آموزش عالی آزاد پژوهش، تهران، ایران
Melika Esperi - موسسه آموزش عالی آزاد پژوهش، تهران، ایران
Hanieh Asvadi - موسسه آموزش عالی آزاد پژوهش، تهران، ایران
Fateme Ezati Kamkar - موسسه آموزش عالی آزاد پژوهش، تهران، ایران
Sayna Rahbari - موسسه آموزش عالی آزاد پژوهش، تهران، ایران

The sweetening of sour gas by amine solvent has attracted a lot of attention due to the high ability of amines to remove acidic compounds from natural gas. In this process, an adsorption column and a distillation column are used to recover the amine. The operating costs of the conventional sour gas sweetening process are very high due to the high energy consumption in the solvent recovery column. Therefore, process energy optimization is very essential. In this research, first, the conventional gas sweetening process was subjected to heat integration (HI) so instead of using utility in supplying process energy, the energy of process flows has been used. Then, the amine recovery column is thermally integrated into this process by Vapor Recompression (VRC) and Bottom Flashing (BF) methods. The results showed that the HI, VRC, and BF processes reduced energy consumption compared to the conventional process about ۲۵%, ۸۸%, and ۹۰%, respectively. Although the compressor consumption of the VRC and BF processes is almost the same, the reduction in hot and cold utility consumption in BF is ۳۳% higher than in VRC. So, the BF process performs better than the VRC process. Moreover, BF process could reduce total annual cost (TAC) of the base process in the maximum value of ۹۶%. That is why BF process is selected as the best choice of heat integration in this case study.

شیرین سازی گاز ترش, انتگراسیون حرارتی, تراکم بخار, تبخیر ناگهانی محصول پایین