NOVELTY - A plant (100) comprises an absorber (110) that receives first and second reflux streams (107, 146). The first reflux stream comprises a cooled lean overhead product (114) from a distillation column. The second reflux stream comprises a cooled vapor portion of a natural gas feed (101) that is reduced in pressure via a device other than a turbo expander.    USE - For natural gas liquids recovery.    ADVANTAGE - The invented plant exhibits 3C recovery of at least 99% and 2C recovery of at least 90%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (a) a method of operating a plant comprising providing an absorber and a distillation column (140); feeding a cooled lean overhead product from the distillation column to the absorber as a first reflux stream; reducing pressure of a cooled vapor portion of a natural gas feed via a device other than a turbo expander; and feeding the cooled vapor portion that is reduced in pressure to the absorber as a second reflux stream in addition to the first reflux stream; and    (b) a method of increasing throughput in a natural gas recovery plant having an absorber and a distillation column comprising providing a first reflux stream to the absorber, where the first reflux stream comprises an overhead product from the distillation column; providing a bypass upstream of a turbo expander, where the bypass receives a vapor portion of a cooled natural gas liquid and provides the vapor portion to the absorber; reducing pressure of the vapor portion before the vapor portion enters the absorber as a second reflux stream; and providing a heat exchanger that cools at least one of the first reflux stream and the second reflux stream using an absorber bottom product (112) and an absorber overhead product.    DESCRIPTION OF DRAWING(S) - The figure is a schematic diagram of a plant configuration.    Plant (100)    Natural gas feed (101, 102)    Reflux streams (107, 146)    Absorber (110)    Bottom product (112)    Overhead product (114)    Distillation column (140)