A process that has come to be known locally as ?multistagestabilization" has been developed in the Haft Kel field of theAnglo-Iranian Oil Co. in southwest Iran, for the recovery of casingheadgasoline. It consists in releasing the dissolved gases from the crude bystages, a practice common in many fields, but which, so far as is known, hasnowhere been carried to the extent to which it is employed in Iran. It has beenin use there for nearly nine years, during which time some 200 million barrelsof crude have been handled by the process. This process of gasoline retentionconsists in preventing the greater part of the casinghead gasoline hydrocarbons(the butanes and pentanes) from ever leaving the crude, instead of allowingthem to be vaporized and then recovered from the lighter gases by the usualcompression or absorption processes. Its efficiency is fully equal to thatobtained by the absorption process; its disadvantage is that it increases thequantities of ethane and propane in the crude sent to the refinery, but withthe growing demand for propane this drawback is vanishing. When casinghead gasoline is recovered as a separate liquid in the Iranianfields, it is blended with the crude, as the only outlet is through therefinery, and the crude-oil pipe line offers the cheapest means oftransportation. It is under these conditions that the retention of the butanesand pentanes in the crude by multistage stabilization is a most attractiveprocess, possessing as it does the following advantages:extremesimplicity,low first cost,easy installation,practically 100 percent operating-time efficiency,no operators required,no water orother services required,negligible maintenance,once established, verylittle routine testing is necessary. The one essential for reasonably efficient multistage stabilization is that theflowing pressures of the wells should be relatively high; i.e.,' they shouldnot be less than about one-third the saturation pressure of the crude in thereservoir. This is a very general statement, of course, and much depends on thetype of crude and its temperature. T.P. 1085