Abstract: A process and plant for natural gas liquids (NGL) recovery includes a main heat exchanger, a cold gas/liquid separator, a separation or distillation column, and an overhead gas heat exchanger. A pressurized residue gas generated from an overhead gas stream removed the top of the separation or distillation column is expanded and used as a cooling medium in the overhead gas heat exchanger and the main heat exchanger. The expanded residue gas, used as a cooling medium, is then compressed up to a pressure to be combined with the overhead stream from the separation or distillation column.

Abstract: A method for oxidizing a waste stream having hydrogen therein includes flowing the waste stream with hydrogen into an oxidant stream for mixing the streams in a proportion for providing a mixture below lower flammability limits (LFL), including the LFL of hydrogen; and introducing the mixed streams into a ceramic matrix bed of a flameless thermal oxidizer maintained at a temperature above auto-ignition temperature of the mixture. A related apparatus is also provided.

Abstract: A flameless thermal oxidizer apparatus for a gaseous stream containing hydrogen includes a vessel containing a ceramic matrix bed; and a dip tube extending into the ceramic matrix bed, the dip tube including a first flow path for a first stream having hydrogen therein, and a second flow path for a second stream having an oxidant therein to be mixed with the first stream for introduction into the ceramic matrix bed. A related method is also provided.

Abstract: In a flameless thermal oxidizer including a vessel configured to contain a matrix bed of media, and a vent gas stream conduit and an oxidizing agent conduit each extending into an interior of the vessel at least partially within the matrix bed of media, a method of delivering a vent gas stream and oxidizing agents into the vessel includes the steps of distributing the vent gas stream through the vent gas stream conduit; distributing the oxidizing agents through a mixing conduit; and combining the vent gas stream and the oxidizing agents in the mixing conduit.

Abstract: A process and plant for natural gas liquids (NGL) recovery includes a main heat exchanger, a cold gas/liquid separator, a separation or distillation column, and an overhead gas heat exchanger. A pressurized residue gas generated from an overhead gas stream removed the top of the separation or distillation column is expanded and used as a cooling medium in the overhead gas heat exchanger and the main heat exchanger. The expanded residue gas, used as a cooling medium, is then compressed up to a pressure to be combined with the overhead stream from the separation or distillation column.

Abstract: In a flameless thermal oxidizer including a vessel configured to contain a matrix bed of media, and a vent gas stream conduit and an oxidizing agent conduit each extending into an interior of the vessel at least partially within the matrix bed of media, a method of delivering a vent gas stream and oxidizing agents into the vessel includes the steps of distributing the vent gas stream through the vent gas stream conduit; distributing the oxidizing agents through a mixing conduit; and combining the vent gas stream and the oxidizing agents in the mixing conduit.

Abstract: A diptube apparatus for a flameless thermal oxidizer having a matrix bed of media including a vent gas stream conduit at least partially positioned within the matrix bed for delivering a vent gas stream; an oxidizing agent conduit separate from the vent gas stream conduit and at least partially positioned within the matrix bed for delivering oxidizing agents; and at least one mixing conduit positioned within the matrix bed and configured to receive the vent gas stream and the oxidizing agents to deliver a combination of the vent gas stream and the oxidizing agents into the matrix bed. A related method and flameless thermal oxidizer are also provided.

Abstract: The invention relates to an integrated process and apparatus for liquefaction of natural gas and recovery of natural gas liquids. In particular, the improved process and apparatus reduces the energy consumption of a Liquefied Natural Gas (LNG) unit by using a portion of the already cooled overhead vapor from a fractionation column from an NGL (natural gas liquefaction) unit to, depending upon composition, provide, for example, reflux for fractionation in the NGL unit and/or a cold feed for the LNG unit, or by cooling, within the NGL unit, a residue gas originating from a fractionation column of the NGL unit and using the resultant cooled residue gas to, depending upon composition, provide, for example, reflux/feed for fractionation in the NGL and/or a cold feed for the LNG unit, thereby reducing the energy consumption of the LNG unit and rendering the process more energy-efficient.

Abstract: The invention relates to an integrated process and apparatus for liquefaction of natural gas and recovery of natural gas liquids. In particular, the improved process and apparatus reduces the energy consumption of a Liquefied Natural Gas (LNG) unit by using a portion of the already cooled overhead vapor from a fractionation column from an NGL (natural gas liquefaction) unit to, depending upon composition, provide, for example, reflux for fractionation in the NGL unit and/or a cold feed for the LNG unit, or by cooling, within the NGL unit, a residue gas originating from a fractionation column of the NGL unit and using the resultant cooled residue gas to, depending upon composition, provide, for example, reflux/feed for fractionation in the NGL and/or a cold feed for the LNG unit, thereby reducing the energy consumption of the LNG unit and rendering the process more energy-efficient.

Abstract: The present invention relates to a process for separating a hydrocarbon gas into a fraction containing a predominant portion of the methane or ethane and lighter components and a fraction containing a predominant portion of the C2 or C3 and heavier components in which process the feed gas is treated in one or more heat exchange, and expansion steps; partly condensed feed gas is directed into a separator wherein a first residue vapor is separated from a C2 or C3-containing liquid; and C2 or C3-containing liquids, at substantially the pressure of separation, are directed into a distillation column wherein said liquid is separated into a second residue is separated to recover a C2 or C3-containing product. The foregoing process is improved by cooling said second residue to partially condense it.

Abstract: An apparatus for altering a surface of a cylindrical object includes at least one container containing a fluid resist therein and having at least one opening from which the fluid resist is discharged; at least one roller operatively associated with the at least one container and having a surface sized and shaped to be exposed to the at least one opening, the surface area including a pattern of shapes and upon which the fluid resist is deposited; and at least one support member adjacent the at least one roller for supporting the cylindrical object during transit for contacting the at least one roller. A method is also provided.