A chemical looping combustion (CLC) based power generation, particularly using liquid fuel, ensures substantially complete fuel combustion and provides electrical efficiency without exposing metal oxide based oxygen carrier to high temperature redox process. An integrated fuel gasification (reforming)-CLC-followed by power generation model is provided involving (i) a gasification island, (ii) CLC island, (iii) heat recovery unit, and (iv) power generation system. To improve electrical efficiency, a fraction of the gasified fuel may be directly fed, or bypass the CLC, to a combustor upstream of one or more gas turbines. This splitting approach ensures higher temperature (efficiency) in the gas turbine inlet. The inert mass ratio, air flow rate to the oxidation reactor, and pressure of the system may be tailored to affect the performance of the integrated CLC system and process.

A process is provided for recycling Hydrogen enrichment tail gas to a combined cycle power system.

A heat exchanger according to one embodiment includes: a cyclone flow path into which a first fluid is introduced along a tangential direction, the first fluid flowing downward in the cyclone flow path; a lower case located below the cyclone flow path and forming a lower space having a flow path area larger than that of the cyclone flow path; a first outlet flow path located on an outer peripheral side of the cyclone flow path, the first outlet flow path communicating with the lower space; a second inlet flow path into which a second fluid is introduced, the second inlet flow path being located on the outer peripheral side of the cyclone flow path; a second outlet flow path located on an inner peripheral side of the cyclone flow path; and a second intermediate flow path connecting the second inlet flow path and the second outlet flow path.

Provided herein are methods, systems, and apparatuses for energy-efficient supercritical water oxidation of waste. The supercritical water oxidation processes and systems described herein may incorporate one or more of the following features: compression of large amounts of oxidant for plant-scale operations in an energy-efficient manner; the use of air as an oxidant; using reactor effluent to drive a turbine or other gas expander for energy recovery; and recovery of pressure and heat of reactor effluent. In some embodiments, the systems and methods are energy-neutral or energy-positive.

Provided herein are methods, systems, and apparatuses for energy-efficient supercritical water oxidation of waste. The supercritical water oxidation processes and systems described herein may incorporate one or more of the following features: compression of large amounts of oxidant for plant-scale operations in an energy-efficient manner; the use of air as an oxidant; using reactor effluent to drive a turbine or other gas expander for energy recovery; and recovery of pressure and heat of reactor effluent. In some embodiments, the systems and methods are energy-neutral or energy-positive.

A carbon-based fuel gasification power generation system is configured to remove ammonia from syngas using washing water, and effectively use the ammonia-containing washing water. The system includes a gasification facility provided with a water scrubber for removing ammonia in the syngas generated as gasified carbon-based fuel, and a power generation facility provided with a combustor for burning gas for combustion generated in the gasification facility and air for combustion humidified in the humidifying tower, and a gas turbine driven by combustion gas. The ammonia-containing water recovered in the water scrubber is supplied to the humidifying tower. Using the water, compressed air to be supplied to the combustor is humidified.

A carbon-based fuel gasification power generation system is configured to remove ammonia from syngas using washing water, and effectively use the ammonia-containing washing water. The system includes a gasification facility provided with a water scrubber for removing ammonia in the syngas generated as gasified carbon-based fuel, and a power generation facility provided with a combustor for burning gas for combustion generated in the gasification facility and air for combustion humidified in the humidifying tower, and a gas turbine driven by combustion gas. The ammonia-containing water recovered in the water scrubber is supplied to the humidifying tower. Using the water, compressed air to be supplied to the combustor is humidified.

System and methods are provided that use a recharge device to resupply a reservoir and tank with fluids used to power a turbine, which in turn powers a generator, wherein one of the resupplied fluids is used to cool a load that is powered by the generator.

System and methods are provided that use a recharge device to resupply a reservoir and tank with fluids used to power a turbine, which in turn powers a generator, wherein one of the resupplied fluids is used to cool a load that is powered by the generator.

A process is provided for separating syngas fuel into a CO-rich stream for feeding to oxyfuel combustor means of CO.sub.2 turbine means and a H.sub.2-rich stream for feeding to air-fuel gas turbine means for generating power provides opportunity to realize operating and equipment advantages.