Xdi Holdings, LLC

Heat IP Holdco, LLC

Raymond Clifford Skinner

James Charles Juranitch

Alan Craig Reynolds

Thomas Raymond Juranitch

Embodiments of the present disclosure can include a system for harvesting salt and generating distilled water from at least one of a produced water and salt water, comprising. A direct steam generator (DSG) can be configured to generate saturated steam and combustion exhaust constituents from the at least one of the produced water and salt water. A separation system can be configured to separate the salt from at least one of the saturated steam and combustion exhaust constituents in brine form or solid form. An expansion turbine can be configured to recover energy from the steam and combustion exhaust constituents.

Dirty water distillation and salt harvesting system, method, and apparatus

Various embodiments of the present disclosure include a system for reducing an operating expense and a steam oil ratio (SOR) of at least one of an enhanced oil recovery system and a gas recovery system. The system can include a boiler configured to produce steam. The system can further include a super-heater in fluid communication with the boiler, the super-heater configured to generate a plurality of super-heat levels in a plurality of sections of the at least one of the enhanced oil recovery system and the gas recovery system downstream of the super-heater, wherein the plurality of super-heat levels are implemented per each one of the plurality of downstream sections of the at least one of the enhanced oil recovery system and gas recovery system to reduce the SOR.

Method, apparatus, real time modeling and control system, for steam and steam with super-heat for enhanced oil and gas recovery

Embodiments of the present disclosure include a system for harvesting salt, and other valued material, and generating distilled water from at least one of a produced water and salt water. The system can include a direct steam generator (DSG) configured to generate saturated steam and combustion exhaust constituents. The system can include a separation system operating after the DSG, configured to separate salt from the saturated steam and combustion exhaust constituents in at least one of brine form and solid form. The system can include an energy recovery system that includes an expansion turbine configured to recover energy from the steam and exhaust constituents.

Embodiments of the present disclosure include a system, method, and apparatus comprising a large scale direct steam generator operating on an oxidant of air or enriched air configured to generate steam and combustion exhaust constituents. An exhaust constituent separation system and an energy recovery system to reclaim energy and improve the efficiency of the thermodynamic cycle. An optional CO2 separation system and Non Condensable Gas injection system may be included.

Large scale cost effective direct steam generator system, method, and apparatus

Embodiments of the present disclosure include a system, method, and apparatus comprising a direct steam generator configured to generate saturated steam and combustion exhaust constituents.

Dirty water and exhaust constituent free, direct steam generation, convaporator system, apparatus and method

Embodiments of the present disclosure can include a system for generating steam. The system can include a direct steam generator configured to generate saturated steam and combustion exhaust constituents. A close coupled heat exchanger can be fluidly coupled to the direct steam generator, the close coupled heat exchanger can be configured to route the saturated or superheated steam and combustion exhaust constituents through an exhaust constituent removal system. The system can include an energy recovery system that reclaims the energy from the exhaust constituents.

Method, apparatus, real time modeling and control system, for steam and super-heat for enhanced oil and gas recovery

A system and method can comprise a heat source, a plasma assisted vitrifier comprising a syphon valve; and a self-cleaning heat exchanger comprising a fired tube side and a water tube side. The self-cleaning heat exchanger can be configured to receive a heat source comprising an oxidized fossil fuel to one of the fire tube side or the water tube side and the self-cleaning heat exchanger can be further configured to receive a dirty water input on the other of the fire tube side and the water tube side to generate a steam. The plasma assisted vitrifier can be configured to process an organic or inorganic solid waste. The syphon valve is configured to assist in generating a reclaimed product, and the plasma assisted vitrifier is further configured to supply a portion of the process heat to the self-cleaning heat exchanger.

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Coral Springs, FL, United States of America

Raymond Clifford Skinner