provided by steam jets a vacuum pump etc and that vacuum system 64 can include the usual vacuum train to recover materials removed from wiped film evaporator 58 since wiped film evaporator 58 has an integral condenser the dga is condensed and transferred via line 68 and pump 70 into product tank 52 again product tank 52 is provided with a vent 72 for co 2 and any other uncondensable gases product from product tank 52 can be transferred via line 72 and pump 74 back into the gas processing operation or for storage and later use it will be appreciated that the vacuum system 64 may recover waste products which can be transferred to waste stream 62 for appropriate disposal it will further be appreciated that various valves gauges etc commonly used have not been shown for simplicity 39 s sake as can be seen from the above the present invention provides a dynamic reaction process which avoids loss of dga by maximizing the conversion of bheeu and the subsequent recovery of the dga additionally the present invention provides such a dynamic reaction system in conjunction with a waste recovery system using a wiped film evaporator to further recover dga and remove waste from the system for proper disposal although specific embodiments of the invention have been described herein in some detail this has been done solely for the purposes of explaining the various aspects of the invention and.