Abstract:
A method for producing syngas from preferably vegetal biomass is described. The method provides for the use of a fixed bed gasifier, equipped with two reactors. The biomass is fed to both reactors together with a primary flow rate of air. Advantageously, the method according to the present invention is different from the known art since a secondary flow rate of air is withdrawn from the first reactor at the area where the biomass dries, and fed to the second reactor at the area where the biomass dries, and vice versa, alternately during time. Alternatively, an oscillating air flow is created in each reactor. The achievable result is a greater syngas production, but not exclusively. The syngas quality is improved too, since the biomass has a longer time for completing the gasification reactions.
Abstract:
A method for maximizing thermal efficiency of a power plant, the method comprising obtaining the current state of the plant from available measured data; obtaining a set of Variables representing a current state of the power plant; applying a set of constraints to the Variables; generating a revised set of Variables representing a revised state of the power plant; and testing the revised set of Variables within a mathematical model for convergence. Generating the revised set of Variable is based at least partly on: Euler's equation, the conservation of mass equation, and a mathematical description of a reversible continuum. There are also provided a related power plant thermal efficiency maximization system and computer program.
Abstract:
The present invention provides a method for producing a highly active catalyst for reforming tar-containing gas used to treat crude gas for chemical energy conversion consisting of converting to a fuel composition consisting mainly of methane, hydrogen and the like, by utilizing sensible heat possessed by crude gas generated during thermal decomposition of carbonaceous raw materials, and using the high chemical reaction activity of high-temperature tar contained in and incidental to the crude gas to convert the tar to light hydrocarbons in the presence of a catalyst; a tar reforming method; and, a method for regenerating a catalyst for reforming tar-containing gas.
Abstract:
Thermodynamic cycles with diluent that produce mechanical power, electrical power, and/or fluid streams for heating and/or cooling are described. Systems contain a combustion system producing an energetic fluid by combusting fuel with oxidant. Thermal diluent is preferably used in the cycle to improve performance, including one or more of power, efficiency, economics, emissions, dynamic and off-peak load performance, temperature regulation, and/or cooling heated components. Cycles include a heat recovery system and preferably recover and recycle thermal diluent from expanded energetic fluid to improve cycle thermodynamic efficiency and reduce energy conversion costs. Cycles preferably include controls for temperatures, pressures, and flow rates within a combined heat and power (CHP) system, and controls for power, thermal output, efficiency, and/or emissions.
Abstract:
A supercharging system (11) for a gas turbine system (13) is provided the supercharging system having a fan (41) mechanically coupled to the turbine shaft (27) of the turbine system. A bypass subsystem (59) is provided or optionally conveying a portion of the airstream output to other uses. The supercharging system may also be used in conjunction with a combined cycle power system and a bypass subsystem optionally conveys a portion of the airstream output to a heat recovery steam generator (15).
Abstract:
The present embodiments are directed towards the cooling of a solvent (15, 86, 222, 314) of a gas treatment system (14) using a fluid flow (30, 32) from an air separation unit (12). In one embodiment, a system (10) is provided that includes an air separation unit (12). The air separation unit (12) has an air inlet (22) configured to receive an air flow (18), an oxygen outlet (30) configured to output an oxygen flow (152, 226, 352, 354), a nitrogen outlet (32) configured to output a nitrogen flow (150, 226, 318, 324) and a cooling system (24, 210, 280, 340) configured to cool the air flow (18) to enable separation of the air flow (18) into the oxygen flow (30) and the nitrogen flow (32), wherein the cooling system (24, 210, 280, 340) is configured to cool a first solvent (15, 86, 222, 314) of a first gas treatment system (14).
Abstract:
A system and method for supercharging a combined cycle system (11) includes a forced draft fan (30) providing a variable air flow. At least a first portion of the air flow is directed to a compressor (15) and a second portion of the airflow is diverted to a heat recovery steam generator (23). A control system (39) controls the airflows provided to the compressor (15) and the heat recovery steam generator (23). The system allows a combined cycle system (11) to be operated at a desired operating state by controlling the flow of air from the forced draft fan (30) to the compressor (15) and the heat recovery steam generator (23).
Abstract:
The integration of plasma processes with combined cycle power plant, simple cycle power plant, and steam reforming processes. A method of producing purified hydrogen gas and fuel is described including compressing a feed stream of hydrogen, adding tail gas from a plasma process to the feed stream, passing the tail gas modified feed stream into a pressure swing adsorption system generating a purified hydrogen product and a pressure swing adsorption tail gas, separating and compressing the purified hydrogen product, and separating and compressing the pressure swing adsorption tail gas for use as fuel. A method of generating and recapturing electricity from a single or combined cycle power plant is also described including flowing natural gas into a plasma process and hydrogen generating plant, flowing the hydrogen produced into the power plant, flowing natural gas into the power plant, resulting in the production of electricity. The electricity is flowed back into the plasma process plant, and in the case of the combined cycle power plant the electricity is partially flowed into a power grid as well. A method of generating and recapturing electricity from a steam power plant is also described, including inputting electricity and natural gas into a plasma process air and hydrogen generating plant, flowing the air and hydrogen produced into a steam generating boiler, flowing the steam generated into a steam power plant, resulting in the production of electricity which is flowed back into the plasma process plant.
Abstract:
A method for enhanced cold (or warm) steam turbine start in a supplementary fired multi-gas turbine combined cycle plant is disclosed. Boiler supplementary firing, which is normally used to increase steam flow when the plant gas turbine is at maximum load, is used to augment steam production with a partly loaded, temperature matched gas turbine. This is done to satisfy minimum required steam flow for a cold (or warm) steam turbine start. Lighting the supplementary firing burners in the heat recovery steam generator/boiler and setting them at a minimum or low heat load serves to add enough steam, at the proper temperature, to insure a successful cold or warm steam turbine start when the gas turbine load and related steam production capacity from the gas turbine exhaust flow are limited by the need to match the required steam temperature and/or maintain low gas turbine exhaust emissions.
Abstract:
Die vorliegende Erfindung betrifft eine Kraft-Wärme-Kopplungsanordnung (100), welche eine Gasturbinenanlage (110) zum Erzeugen von mechanischer Leistung, eine Wärmekraftanlage (120) mit einem Wärmetauscher (121) und einer Turbine (122) und einen Verdichter (130) zum Verdichten eines Hilfsluftstroms aufweist. Der Gasturbinenanlage (110) ist ein Zuluftstrom (111) zuführbar und ein Abluftstrom (112) abführbar. Die Wärmekraftanlage (120) ist mit einem Arbeitsmedium (126) betreibbar, wobei der Wärmetauscher (121) mit der Gasturbinenanlage (110) derart gekoppelt ist, dass thermische Energie von dem Abluftstrom (112) auf das Arbeitsmedium (126) übertragbar ist, sodass die Turbine (122) mittels des Arbeitsmediums betreibbar ist. Der Verdichter (130) ist mittels der Turbine (122) antreibbar, wobei der Verdichter (130) mit der Gasturbinenanlage (110) derart gekoppelt ist, dass der verdichtete Hilfsluftstrom (131) in die Gasturbinenanlage (110) einspeisbar ist.