The combined cycle power device in the present invention belongs to the field of energy and power technology. A combined cycle power device comprising an expander, the second expander, a compressor, the third expander, a pump, a high-temperature heat exchanger, a condenser and an evaporator. An evaporator connects the second expander has a vapor channel connected the that a condenser has a liquid refrigerant pipe which passes through a pump and connects the evaporator. The second expander connects the high-temperature heat exchanger. A compressor connects the high-temperature heat exchanger. The high-temperature heat exchanger connects an expander. The evaporator connects the compressor and the third expander respectively has a vapor channel connected the that the expander connects the evaporator. The third expander connects the condenser. The high-temperature heat exchanger connects the outside. The condenser has the cooling medium channel. The expander, the second expander and the third expander connects the compressor.

The single-working-medium vapor combined cycle is provided in this invitation and belongs to the field of energy and power technology. A single-working-medium vapor combined cycle consists of nine processes which are conducted with M.sub.1 kg of working medium and M.sub.2 kg of working medium separately or jointly: a pressurization process 1-2 of the M.sub.1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M.sub.1 kg of working medium, a depressurization process 3-4 of the M.sub.1 kg of working medium, a pressurization process 7-4 of M.sub.2 kg of working medium, a heat-absorption process 4-5 of the M.sub.3 kg of working medium, a depressurization process 5-6 of the M.sub.3 kg of working medium, a heat-releasing process 6-7 of the M.sub.3 kg of working medium, a heat-releasing and condensation process 7-1 of the M.sub.1 kg of working medium; M.sub.3 is the sum of M.sub.1 and M.sub.2.

The single-working-medium vapor combined cycle is provided in this invitation and belongs to the field of energy and power technology. A single-working-medium vapor combined cycle consists of nine processes which are conducted with M.sub.1 kg of working medium and M.sub.2 kg of working medium separately or jointly: a pressurization process 1-2 of the M.sub.1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M.sub.1 kg of working medium, a depressurization process 3-4 of the M.sub.1 kg of working medium, a pressurization process 7-4 of M.sub.2 kg of working medium, a heat-absorption process 4-5 of the M.sub.3 kg of working medium, a depressurization process 5-6 of the M.sub.3 kg of working medium, a heat-releasing process 6-7 of the M.sub.3 kg of working medium, a heat-releasing and condensation process 7-1 of the M.sub.1 kg of working medium; M.sub.3 is the sum of M.sub.1 and M.sub.2.

The combined cycle power device of the present invention belongs to the field of energy and power technology. A combined cycle power device comprises an expander, a compressor, the second expander, a pump, the second pump, a high-temperature heat exchanger, a high-temperature evaporator, a condenser and a mixed evaporator. A condenser connects a mixed evaporator. An expander connects the mixed evaporator. The mixed evaporator connects a compressor. The mixed evaporator passes through the second expander and connects the condenser. The compressor connects a high-temperature heat exchanger. A high-temperature evaporator connects the high-temperature heat exchanger after that the condenser passes through the second pump and connects the high-temperature evaporator. The high-temperature heat exchanger connects the expander. The high-temperature heat exchanger and the high-temperature evaporator have connect the outside respectively. The condenser connects the outside. The expander connects the compressor and transmits power.

The single-working-medium vapor combined cycle is provided in this invitation and belongs to the field of energy and power technology. A single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M.sub.1 kg of working medium, M.sub.2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M.sub.1 kg of working medium, performing a heat-absorption and vaporization process to set a state (2) to (3) of the M.sub.1 kg of working medium, performing a depressurization process to set a state (3) to (4) of the M.sub.1 kg of working medium, performing a heat-absorption process to set a state (4) to (5) of the M.sub.1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set a state (e) to (8) of the H kg of working medium, performing a pressurization process to set a state (8) to (5) of the M.sub.2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M.sub.1+M.sub.2) kg of working medium, performing a depressurization process to set a state (6) to (7) of the (M.sub.1+M.sub.2) kg of working medium, performing a heat-releasing process to set a state (7) to (f) of the (M.sub.1+M.sub.2) kg of working medium, performing a mixing heat-releasing process to set a state (f) to (8) of the (M.sub.1+M.sub.2) kg of working medium and H kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M.sub.1+H) kg of working medium, performing a heat-releasing and condensation process to set a state (9) to (1) of the (M.sub.1+H) kg of working medium.

Operating coal fired energy systems. A method of operating a coal fired energy system comprises operating a coal fired steam generator comprising a coal feed system and a main air feed system to provide a coal-air mixture as a heating source for a boiler for generating steam. The method includes operating an auxiliary air compression system comprising a fueled engine coupled to a compressor for providing an auxiliary supply of compressed air to a soot blower of the coal-fired steam generator. The method comprises injecting the auxiliary supply of compressed air along walls of the boiler to remove soot and ash buildup from the boiler.

Operating coal fired energy systems. A method of operating a coal fired energy system comprises operating a coal fired steam generator comprising a coal feed system and a main air feed system to provide a coal-air mixture as a heating source for a boiler for generating steam. The method includes operating an auxiliary air compression system comprising a fueled engine coupled to a compressor for providing an auxiliary supply of compressed air to a soot blower of the coal-fired steam generator. The method comprises injecting the auxiliary supply of compressed air along walls of the boiler to remove soot and ash buildup from the boiler.

The invention relates generally to electrical power systems or steam generator systems including generating capacity of a coal plant where specific emissions and power is improved with an alternately fueled engine driving one or more air processes.

The invention relates generally to electrical power systems or steam generator systems including generating capacity of a coal plant where specific emissions and power is improved with an alternately fueled engine driving one or more air processes.

A system includes a waste heat recovery heat exchanger configured to heat a heating fluid stream by exchange with a heat source in a crude oil associated gas processing plant. The system includes an Organic Rankine cycle energy conversion system including a pump, an energy conversion heat exchanger configured to heat the working fluid by exchange with the heated heating fluid stream, a turbine and a generator configured to generate power by expansion of the heated working fluid, a cooling element configured to cool the expanded working fluid after power generation, and an accumulation tank. The heating fluid flows from the accumulation tank, through the waste heat recovery heat exchanger, through the Organic Rankine cycle energy conversion system, and back to the accumulation tank.