An experimental investigation was made of the adsorption on silica gel of components from light hydrocarbon mixtures, and the results were used to test a multicomponent adsorption theory. Experimental methods included a volumetric technique to measure pure component adsorption and flow techniques for adsorption from mixtures. Although the majority of measurements was made at lOO"F., two mixtures were studied over the temperature range 40" to 160°F. Pressure was varied up to 1,800 Ib./sq.in.abs. The Brunauer-Emmett-Teller (BET) theory of adsorption, as extended to mixtures by Hill, wos tested against the experimental data and was found to be adequate for calculating adsorption from hydrocarbon mixtures of components heavier than methane. To account for nonideal behavior, the fugacity of each component in the gas and in the adsorbed phases was calculated by using the Benedict-Webb-Rubin equation of state. The differences in experimental and theoretical values for adsorption capacity were less than 10% for most of the conditions tested, but ranged up to about 25% for the highest pressures studied. Although the BET theory represents a simplified model of a complex process, it can be used to supply adsorption data for engineering application over ranges of pressure, temperature, and gas composition usually encountered in adsorption processing of natural gos mixtures.In the succeeding paragraphs, results of the adsorption capacity experiments are presented, and a multicomponent adsorption theory, capable of reproducing the experimen-countered in natural gas treating. App B icability of various Vol. '12, No. 6 A.1.Ch.E. Journal Journal November, 1966 Fig. 7. Effect of total pressure on silica gel adsorption of n-pentane and n-hexane from a complex gas mixture a t 100°F.