Exxonmobil Upstream Research Company

Exxon Production Research Company

Exxonmobil Technology and Engineering Company

Russell H Oelfke

Karla Schall Colle

Larry D Talley

Christine A Costello

Enock Berluche

Harry William Deckman

Robert A Johnson

Richard Alan Huntington

Robert D Denton

Ananda K Nagavarapu

Shwetha Ramkumar

O Angus Sites

Bruce T Kelley

Moses Minta

Franklin F Mittricker

Eugene R Thomas

Sulabh K Dhanuka

Dennis M O'Dea

Dennis M O'dea

Dennis G Peiffer

Michael R Miller

Ronald Richard Chance

Pamela Jean Wright

Bennett D Marshall

Donald J Victory

William Barnes

Manese Rabeony

Stanley O Uptigrove

Ransdall K Smith

John M Longo

Tor Vestad

Malcolm A Kelland

Patrick D J McMahon

Allen E Brimm

Enoch Berluche

Patrick D Mcmahon

Jorge Vincentelli

Patrick D J Mcmahon

Systems, methods, and apparatus are provided for generating power in low emission turbine systems and separating the exhaust into rich COand lean COstreams. In one or more embodiments, the exhaust is separated at an elevated pressure, such as between a high-pressure expansion stage and a low-pressure expansion stage.

Systems and methods for carbon dioxide capture and power generation in low emission turbine systems

Embodiments described herein provide methods and systems for separating a mixed ethane and CO. A method described includes generating a liquid stream including ethane and CO. The liquid stream is flashed to form an ethane vapor stream and solid CO. The solid COis accumulated in an accumulation vessel and the gas is removed from the top of the accumulation vessel.

Separating carbon dioxide and ethane from a mixed stream

Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to treat the pipeline quality natural gas to form a stream that complies with liquefied natural gas (LNG) specifications. The process may involve a combined TSA and PSA process, which is utilized to remove contaminants from the feed stream.

Apparatus and system for combined temperature and pressure swing adsorption processes related thereto

Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit is purged with a purge stream that is provided from the overhead of the demethanizer. The configuration integrates a PPSA dehydration system with a cryogenic recovery system.

Apparatus and system for swing adsorption processes related thereto

Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit is purged with a purge stream that is provided at a temperature less than 450&#xb0; F. The de-contaminated stream may be used with a liquefied natural gas (LNG) plant or other subsequent process requiring a de-contaminated stream. The swing adsorption process may involve a combined TSA and PSA process, which is utilized to remove contaminants from the feed stream.

Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to treat the feed stream to form a stream that complies with nitrogen rejection specifications. The process may involve using at least a portion of the nitrogen rejection process product streams as a purge for the swing adsorption process.

Methods and systems for low emission power generation in combined cycle power plants are provided. One system includes a gas turbine system that stoichiometrically combusts a fuel and an oxidant in the presence of a compressed recycle stream to provide mechanical power and a gaseous exhaust. The compressed recycle stream acts as a diluent to moderate the temperature of the combustion process. A boost compressor can boost the pressure of the gaseous exhaust before being compressed into the compressed recycle stream. A purge stream is tapped off from the compressed recycle stream and directed to a C0separator which discharges C0and a nitrogen-rich gas which can be expanded in a gas expander to generate additional mechanical power.

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A system and methods for processing a feed gas in a column are provided herein. A method includes feeding a feed gas into a port of a sleeve disposed around at least a portion of a periphery of the column. The sleeve includes a space between an outer wall of the column and an inner wall of the column. The sleeve releases the feed gas into the column through an opening disposed at an opposite end of the sleeve from the port.

Method for separating a feed gas in a column

Methods and systems for COseparation for low emission power generation in combined-cycle power plants are provided. One system includes a gas turbine system that stoichiometrically combusts a fuel and an oxidant in the presence of a compressed recycle stream to provide mechanical power and a gaseous exhaust. The compressed recycle stream acts as a diluent to moderate the temperature of the combustion process. A boost compressor can boost the pressure of the gaseous exhaust before being compressed into the compressed recycle stream. A purge stream is tapped off from the compressed recycle stream and directed to a COseparator configured to absorb COfrom the purge stream using a potassium carbonate solvent.

Low emission power generation systems and methods

Systems, methods, and apparatus are provided for generating power in combined low emission turbine systems and capturing and recovering carbon dioxide from the exhaust. In one or more embodiments, the exhaust from multiple turbine systems is combined, cooled, compressed, and separated to yield a carbon dioxide-containing effluent stream and a nitrogen-containing product stream. Portions of the recycled exhaust streams and the product streams may be used as diluents to regulate combustion in each combustor of the turbine systems.

Systems and methods for carbon dioxide capture in low emission combined turbine systems

The present techniques are directed to a system and method for generating power and producing liquefied natural gas (LNG). The system includes a power plant configured to generate power, wherein an exhaust gas from the power plant provides a gas mixture including nitrogen and carbon dioxide. The system also includes a dehydration system configured to dehydrate the gas mixture to generate a nitrogen refrigerant stream and a refrigeration system configured to produce LNG from a natural gas stream using the nitrogen refrigerant stream.

Power generation and LNG production

Methods and systems for recovery of natural gas liquids (NGL) and a pressurized methane-rich sales gas from liquefied natural gas (LNG) are disclosed. In certain embodiments, LNG passes through a heat exchanger, thereby heating and vaporizing at least a portion of the LNG. The partially vaporized LNG passes to a fractionation column where a liquid stream enriched with ethane plus and a methane-rich vapor stream are withdrawn. The withdrawn methane-rich vapor stream passes through the heat exchanger to condense the vapor and produce a two phase stream, which is separated in a separator into at least a methane-rich liquid portion and a methane-rich gas portion. A pump pressurizes the methane-rich liquid portion prior to vaporization and delivery to a pipeline. The methane-rich gas portion may be compressed and combined with the vaporized methane-rich liquid portion or used as plant site fuel.

Method of extracting ethane from liquefied natural gas

The invention relates to a method of separating one or more components from a multi-component gas stream comprising at least one non-acid gas component and at least one acid gas component. A multi-component gas stream at a pressure above 1,200 psia (82.8 bar) and a temperature above 120&deg; F. (48.9&deg; C.) with the concentration of at least one acid gas component in the gas stream being at least 20 mole percent is passed to a membrane system that selectively separates at least one acid gas component from the multi-component gas stream as a permeate stream. The permeate stream has a pressure at least 20% of the pressure of the feed pressure.

High-pressure separation of a multi-component gas

Method for inhibiting hydrate formation

Growing community of inventors

Houston, TX, United States of America

Russell H Oelfke