Abstract: A liquid energy storage system where the mixed refrigerant may include the following components with concentrations in mole volume percentages as follows: about 12.0% Nitrogen, about 15.0% Ethylene, about 39.0% Methane, about 20.0% Ethane, about 10.0% Propane, and about 4.0% Iso-Butane. A liquid energy storage system where the thermodynamic relationship for lost work is characterized by: Wlost=TOIntegral(T1?T2)/(T1×T2)dH, where To is the ambient temperature and T1, and T2 are the temperatures of the hot and cold streams, respectively, all temperatures are absolute temperatures, and H represents the enthalpy or heat content of the fluids in the heat exchange process.

Abstract: A liquid air energy storage system, the system comprising: a liquid air storage means; an input of a first pump in fluid communication with the liquid air storage means; a first heat exchanger in fluid communication with an output of the first pump; a second heat exchanger in fluid communication first heat exchanger and configured to receive the fluid stream from the first pump and the first heat exchanger; a first expander turbine generator in fluid communication with the second heat exchanger; the first heat exchanger in fluid communication with the first expander turbine generator; a third heat exchanger in fluid communication with the first heat exchanger and configured to receive the fluid stream from the first expander turbine generator and the first heat exchanger; a second expander turbine generator in fluid communication with the third heat exchanger; the first heat exchanger in fluid communication with the second expander turbine generator; the fluid stream from second expander turbine generator and

Abstract: A liquid air energy storage system, the system comprising: a liquid air storage means; an input of a first pump in fluid communication with the liquid air storage means; a first heat exchanger in fluid communication with an output of the first pump; a second heat exchanger in fluid communication first heat exchanger and configured to receive the fluid stream from the first pump and the first heat exchanger; a first expander turbine generator in fluid communication with the second heat exchanger; the first heat exchanger in fluid communication with the first expander turbine generator; a third heat exchanger in fluid communication with the first heat exchanger and configured to receive the fluid stream from the first expander turbine generator and the first heat exchanger; a second expander turbine generator in fluid communication with the third heat exchanger; the first heat exchanger in fluid communication with the second expander turbine generator; the fluid stream from second expander turbine generator and

Abstract: A liquid air energy storage system, the system comprising: a liquid air storage means; an input of a first pump in fluid communication with the liquid air storage means; a first heat exchanger in fluid communication with an output of the first pump; a second heat exchanger in fluid communication first heat exchanger and configured to receive the fluid stream from the first pump and the first heat exchanger; a first expander turbine generator in fluid communication with the second heat exchanger; the first heat exchanger in fluid communication with the first expander turbine generator; a third heat exchanger in fluid communication with the first heat exchanger and configured to receive the fluid stream from the first expander turbine generator and the first heat exchanger; a second expander turbine generator in fluid communication with the third heat exchanger; the first heat exchanger in fluid communication with the second expander turbine generator; the fluid stream from second expander turbine generator and

Abstract: Machinery and methods for converting inexpensive electricity to higher value electricity. A system includes means for compressing a gas such as air, means for condensing the gas to a liquid stream, means for storing liquefied gas, means for pumping the liquefied gas, means for evaporating and heating the liquefied gas or for heating the liquefied gas to form a supercritical fluid, and introducing this stream into a means for producing electricity. The means for compressing a gas may include sources of electricity from renewable energy sources. A method of storing energy may comprise (a) compressing and liquefying air using energy from a renewable energy source; and (b) subsequently expanding vapor generated from the liquefied air through an expander to drive a generator and produce electricity. Various systems and methods disclosed herein allow electricity from renewable sources and produced during off-peak periods to be utilized during peak demand periods for electricity with low capital and installed costs.

Abstract: A method and system for the small-scale production of LNG.

Abstract: A method and system for the small-scale production of LNG.

Abstract: A method of cold recovery in a cold compressed natural gas cycle, the method comprising: compressing air; drying air; heat exchanging air with cold compressed natural gas from a storage vessel, in a first heat exchanger, thereby forming cooled air; heat exchanging the cooled air with liquid methane, in a second heat exchanger, such that the cooled air becomes liquid air and the liquid methane becomes methane; heat exchanging the liquid air with natural gas from a pipeline, in a third heat exchanger, such that the natural gas cools to a cold compressed natural gas and the liquid air becomes air in a gaseous state; discharging the air in a gaseous state.

Abstract: A combined cycle power plant comprising: a first cycle comprising: a prime mover; a prime mover exhaust in fluid communication with the prime mover; a second cycle comprising: a liquid air supply; a heat exchanger in fluid communication with the liquid air supply and the prime over exhaust; a turbo expander in fluid communication with the heat exchanger; wherein liquid air is heated to gaseous air by the heat exchanger, and the gaseous air is expanded in the turbo expander thereby producing work. A liquid air combined cycle method comprising: providing pressurized liquid air; heating the pressurized liquid air to pressurized gaseous air; expanding the pressurized gaseous air with a turbo expander; using work from the expansion of the pressurized gaseous air to compress ambient air; heating the expanded pressurized gaseous air; sending the heated expanded air to a turbine combustion chamber; and using waste heat from a turbine to heat pressurized liquid air.

Abstract: A method of cold recovery in a cold compressed natural gas cycle, the method comprising: compressing air; drying air; heat exchanging air with cold compressed natural gas from a storage vessel, in a first heat exchanger, thereby forming cooled air; heat exchanging the cooled air with liquid methane, in a second heat exchanger, such that the cooled air becomes liquid air and the liquid methane becomes methane; heat exchanging the liquid air with natural gas from a pipeline, in a third heat exchanger, such that the natural gas cools to a cold compressed natural gas and the liquid air becomes air in a gaseous state; discharging the air in a gaseous state.

Abstract: A method of transporting or storing a natural gas. The method comprises: compressing and chilling the natural gas; changing a state of the natural gas into a cold compressed state; pumping the natural gas to an appropriate transportation pressure or storage pressure and maintaining the natural gas in the cold compressed state. A system for the transportation of a cold compressed natural gas.

Abstract: A method for the separation of gaseous mixtures such as air and for producing medium purity oxygen, comprising compressing the gaseous mixture in a first compressor to about 3.9-4.