Abstract: Provided is an indirect heated separation assembly that includes a vessel assembly having a heating section and a separation section, a wall separating the heating section from the separation section, the wall configured to be heated by a heating fluid in the heating section to provide indirect heat to the separation section, and a coil assembly at least partially disposed in the heating section, the coil assembly including an inlet configured to receive a process fluid and an outlet in communication with an inlet of the separation section to direct the process fluid after heating to the separation section.

Abstract: Provided is an indirect heated separation assembly that includes a vessel having a heating section and a separation section, a plate separating the heating section from the separation section, the plate being configured to be heated by a heating fluid in the heating section to provide indirect heat to the separation section, and a coil assembly disposed in the heating section, the coil assembly including an inlet configured to receive a process fluid and an outlet in communication with an inlet of the separation section to direct the process fluid after heating to the separation section.

Abstract: Provided is an assembly including a vessel having first and second ends and an interior, an inlet diverter disposed in the interior at the first end, at least one flow baffle disposed in the interior and having a gas section including a plurality of gas openings extending through the baffle, a liquid section below the gas section including a plurality of liquid openings extending through the baffle, and a bottom surface spaced from a bottom interior surface of the vessel to define a fluid flow path between the bottom surface and the bottom interior surface, and at least one vane section disposed in the interior downstream of the at least one flow baffle, the at least one vane section having a bottom surface spaced from the bottom interior surface of the vessel to define a fluid flow path between the bottom surface and the bottom interior surface.

Abstract: Provided is an assembly including a vessel having first and second ends and an interior, an inlet diverter disposed in the interior at the first end, at least one flow baffle disposed in the interior and having a gas section including a plurality of gas openings extending through the baffle, a liquid section below the gas section including a plurality of liquid openings extending through the baffle, and a bottom surface spaced from a bottom interior surface of the vessel to define a fluid flow path between the bottom surface and the bottom interior surface, and at least one vane section disposed in the interior downstream of the at least one flow baffle, the at least one vane section having a bottom surface spaced from the bottom interior surface of the vessel to define a fluid flow path between the bottom surface and the bottom interior surface.

Abstract: Provided is an indirect heated separation assembly that includes a vessel having a heating section and a separation section, a plate separating the heating section from the separation section, the plate being configured to be heated by a heating fluid in the heating section to provide indirect heat to the separation section, and a coil assembly disposed in the heating section, the coil assembly including an inlet configured to receive a process fluid and an outlet in communication with an inlet of the separation section to direct the process fluid after heating to the separation section.

Abstract: Provided is an indirect heated separation assembly that includes a vessel assembly having a heating section and a separation section, a wall separating the heating section from the separation section, the wall configured to be heated by a heating fluid in the heating section to provide indirect heat to the separation section, and a coil assembly at least partially disposed in the heating section, the coil assembly including an inlet configured to receive a process fluid and an outlet in communication with an inlet of the separation section to direct the process fluid after heating to the separation section.

Abstract: The methods improve the separation of hydrocarbon containing fluids. More particularly, the disclosure is relevant to separating fluids having a gas phase and a hydrocarbon liquid phase using indirect heating. In general, the methods use a first gas separation step followed by indirect heating and then a second gas separation step. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.

Abstract: The methods improve the separation of hydrocarbon containing fluids. More particularly, the disclosure is relevant to separating fluids having a gas phase and a hydrocarbon liquid phase using indirect heating. In general, the methods use a first gas separation step followed by indirect heating and then a second gas separation step. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.

Abstract: The methods improve the separation of hydrocarbon containing fluids. More particularly, the disclosure is relevant to separating fluids having a gas phase, a hydrocarbon liquid phase, and an aqueous liquid phase using indirect heating. In general, the methods use a first three-phase gas separation stop followed by indirect heating and then a second three-phase gas separation step. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.

Abstract: The methods improve the separation of hydrocarbon containing fluids. More particularly, the disclosure is relevant to separating fluids having a gas phase, a hydrocarbon liquid phase, and an aqueous liquid phase using indirect heating. In general, the methods use a first three-phase gas separation stop followed by indirect heating and then a second three-phase gas separation step. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.

Abstract: Systems and methods for separation of hydrocarbon containing fluids are provided. More particularly, the disclosure is relevant to separating fluids having a gas phase, a hydrocarbon liquid phase, and an aqueous liquid phase using indirect heating. In general, the system uses a first three-phase gas separation followed by indirect heating and then a second three-phase gas separation. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.

Abstract: Systems and methods for separation of hydrocarbon containing fluids are provided. More particularly, the disclosure is relevant to separating fluids having a gas phase, a hydrocarbon liquid phase, and an aqueous liquid phase using indirect heating. In general, the system uses a first three-phase gas separation followed by indirect heating and then a second three-phase gas separation. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.

Abstract: Systems and methods for separation of hydrocarbon containing fluids are provided. More particularly, the disclosure is relevant to separating fluids having a gas phase, a hydrocarbon liquid phase, and an aqueous liquid phase using indirect heating. In general, the system uses a first three-phase gas separation followed by indirect heating and then a second three-phase gas separation. Pressure reduction of the hydrocarbon containing fluid occurs either before or after the indirect heating.