Exxonmobil Chemical Patents Inc.

Xyz Energy Group, LLC

Exxonmobil Upstream Research Company

Exxonmobil Research and Engineering Company

Exxon Chemical Patents, Inc.

Frank F Mittricker

Richard Alan Huntington

Loren K Starcher

Donald J Victory

David Charles Calabro

Narasimhan Sundaram

Hans Thomann

Keith Holroyd Kuechler

Gary F Janda

Frank Roberto

John J Guide

Michael Turner

Methods and systems for generating power (and optionally heat) from a high value heat source using a plurality of circulating loops comprising a primary heat transfer loop, several power cycle loops and an intermediate heat transfer loop that transfers heat from the high-temperature heat transfer loop to the several power cycle loops. The intermediate heat transfer loop is arranged to eliminate to the extent practical the shell and tube heat exchangers especially those heat exchangers that have a very large pressure difference between the tube side and shell side, to eliminate shell and tube, plate type, double pipe and similar heat exchangers that transfer heat directly from the primary heat transfer loop to the several power cycle loops with very high differential pressures and to maximize the use of heat transfer coils similar in design as are used in a heat recovery steam generator commonly used to transfer heat from gas turbine flue gas to steam or other power cycle fluids as part of a combined cycle power plant.

System and method for the generation of heat and power using multiple loops comprising a primary heat transfer loop, a power cycle loop and an intermediate heat transfer loop

Systems and methods for transferring and converting heat to a power cycle using a plurality of heat transfer fluids, loops and heat exchange devices to convert heat to useful work and/or power. Power is generated using intermediate heat transfer loops (IHTL) and an intermediate heat transfer fluid (IHTF) to cool the hot exhaust power cycle fluid (PCF) stream that is at or above its critical conditions. The temperature of the IHTF can be increased by 100&#xb0; C., 150&#xb0; C., 200&#xb0; C., 250&#xb0; C., 300&#xb0; C., 350&#xb0; C., 400&#xb0; C., 450&#xb0; C., 500&#xb0; C., 550&#xb0; C. or more by exchanging heat with the PCF, either directly or indirectly.

Multiple loop power generation using super critical cycle fluid with split recuperator

Methods and systems for producing a thermally converted product stream (and optionally heat and power) from a high value heat source using a plurality of circulating loops comprising a primary heat transfer loop, several substantially not recirculated process heater, reactor or separator systems and an intermediate heat transfer loop that transfers heat from the high-temperature heat transfer loop to the several process heater, reactor or separator systems. The intermediate heat transfer loop is arranged to eliminate to the extent practical the shell and tube heat exchangers especially those heat exchangers that have a very large pressure difference between the tube side and shell side, to eliminate shell and tube, plate type, double pipe and similar heat exchangers that transfer heat directly from the primary heat transfer loop to the several process heater, reactor or separator systems with very high differential pressures and to maximize the use of heat transfer coils similar in design as are used in a heat recovery steam generator commonly used to transfer heat from gas turbine flue gas to steam or other power cycle fluids as part of a combined cycle power plant.

System and method for thermal conversion of materials using multiple loops comprising a primary heat transfer loop, an intermediate heat transfer loop and a thermal conversion circuit

An adsorption module and associated processes for conducting advanced separations processes such as sorption enhanced water-gas shift (SEWGS). The adsorption module contains at least one angled baffle to create at least two tapered adsorbent beds within the adsorption module. The taper is such that the adsorbent beds' cross-sections within the adsorption module decrease in the direction of feed flow, thereby taking advantage of increased product purity and process efficiency provided by tapered adsorption beds.

Increasing scales, capacities, and/or efficiencies in swing adsorption processes with hydrocarbon gas feeds

In various aspects, methods are provided for hydrogen production while reducing and/or mitigating emissions during various refinery processes that produce syngas, such as power generation. Syngas can be effectively separated to generate high purity carbon dioxide and hydrogen streams, while reducing and/or minimizing the energy required for the separation, and without needing to reduce the temperature of the flue gas. In various aspects, the operating conditions, such as high temperature, mixed metal oxide adsorbents, and cycle variations, for a pressure swing adsorption reactor can be selected to minimize energy penalties while still effectively capturing the COpresent in syngas.

High temperature pressure swing adsorption for advanced sorption enhanced water gas shift

The invention is directed to a method of fueling gas turbines from natural gas reserves with relatively low methane concentrations. The invention permits the use of such reserves to be used to fuel gas turbines to generate electric power. The method of the invention includes providing a natural gas comprising not more than about 40 percent methane on a volume basis and mixing the methane of the natural gas with hydrogen gas to provide a hydrogen enhanced methane/hydrogen gas blend which has sufficient hydrogen to provide flame stability during burning. Thereafter, if required, the hydrogen enhanced methane/hydrogen gas blend is dehydrated to remove a sufficient amount of water to provide a flame stable hydrogen enhanced dehydrated methane/hydrogen gas blend. The hydrogen enhanced natural gas blend is used to fuel gas turbine generators.

Method for utilizing gas reserves with low methane concentrations for fueling gas turbines

The invention is directed to a method of fueling gas turbines from natural gas reserves with relatively low methane concentrations. The invention uses such reserves to generate electric power. The invention permits the use of these reserves at significantly lower cost than by producing pipeline natural gas to fuel gas turbines to generate electric power. These reserves currently generally are used only after the removal of impurities to produce pipeline natural gas quality turbine fuel. The latter current technology is capital intensive, and at current natural gas prices, economically unattractive. The process of the invention can remove the impurities from the gas from the natural gas reserve necessary for protection of the environment and leaves inert gasses in the fuel in an amount which will increase the output of a gas turbine for the generation of power by about 5 to about 20%.

Method for utilizing gas reserves with low methane concentrations and high inert gas concentrations for fueling gas turbines

A cogeneration system having a gas turbine generator () that provides combustion air via an exhaust to a heat recovery steam generator () has a gas-seal stack () coupled there between. The gas-seal stack () prevents substantial portions of the exhaust gas from exiting there through due to formation of a column of higher density ambient air. This blockage is achieved without resort to mechanical. pneumatic pathway control devices. Conversely, if and when the gas turbine generator () shuts down, ambient air is drawn through the gas-seal stack () and serves to support continued combustion in the heat recovery steam generator (). In one embodiment, an induction fan (or fans) () is located at the exhaust of the heat recovery steam generator () such that combustion air is pulled through the heat recovery steam generator () rather than pushed there through. This aids in minimizing backpressure at the exhaust of the gas turbine generator ().

Gas seal apparatus and method for use in cogeneration applications

The invention is directed to a method of fueling gas turbines from natural gas reserves with relatively low methane concentrations. The invention uses such reserves to generate electric power. The invention permits the use of these reserves at significantly lower cost than by producing pipeline natural gas to fuel gas turbines to generate electric power. These reserves currently generally are used only after the removal of impurities to produce pipeline natural gas quality turbine fuel. The latter current technology is capital intensive, and at current natural gas prices, economically unattractive. The process of the invention can remove the impurities from the gas from the natural gas reserve necessary for protection of the environment, and leaves inert gasses in the fuel in an amount which will increase the output of a gas turbine for the generation of power by about 5 to about 20%.

A method and system for generating power include using a cogeneration power system having a gas turbine. The gas turbine has a compressor section for receiving air to be compressed. The compressed air is fed to a combustor section where it is mixed with fuel and the fuel is burned to produce heated combustion gas. The heated combustion gas is expanded in an expander section to generate shaft work which is used to drive a generator or alternator for producing electric power. The heated combustion gas leaves the expander as turbine exhaust which is cooled by transferring at least part of its heat to the air ahead of the combustor.

Growing community of inventors

Houston, TX, United States of America

Frank F Mittricker