Experimental Study of a Hydrophobic Solvent for Natural Gas Sweetening Based on the Solubility and Selectivity for Light Hydrocarbons (CH 4 , C 2 H 6 ) and Acid Gases (CO 2 and H 2 S) at 298–353 K
The Henry’s constants of H 2 S, CO 2 , CH 4 , and C 2 H 6 in a hydrophobic solvent (HPS) were determined to evaluate the potential use of the HPS for natural gas sweetening applications. The gas solubilities were evaluated at atmospheric pressure in the temperature range of 298-353 K. The Henry’s constant of N 2 O in the HPS was also determined and used to differentiate the physical absorption of the acid gases from the chemical absorption. The temperature-dependent Henry’s constant correlations of these gases were developed and used to determine the separation performance of the HPS in a simple absorber process simulation. Here, the simulation results suggest that HPS can remove acid contaminants and achieve the targeted quality of natural gas for liquid natural gas (LNG) production. The HPS exhibits rather high CH 4 and C 2 H 6 absorption, and consequently, has low acid gas selectivity compared to the commercially available physical solvent. the acid gas selectivity can be optimized with the inclusion a limited quantity of a hydrophilic component to enhance H 2 S and CO 2 while still minimizing the hydrocarbons solubilities.