The invention provides a method and system for extracting stranded gas (such as natural gas or hydrogen) or a mixture of oil and natural gas from a subterranean environment such as beneath the ocean floor and converting it into a solid hydrate such as a clathrate featuring a) extracting stranded gas (such as natural gas or hydrogen) or a mixture of oil and natural gas; b) optionally separating the natural gas from the mixture of oil and natural gas in a first tank or vessel; c) transporting the stranded gas to a second tank or vessel; d) introducing sea water into the second tank or vessel; e) mixing the stranded gas and water to form a clathrate hydrate/water slurry; f) removing excess water from the clathrate hydrate slurry to form a solid comprising a clathrate hydrate; and g) processing the solid comprising a clathrate hydrate into a transportable form; and h) optionally collecting the gas into a transportable vessel.

The invention relates a method for storing a solution of methane and a C2-C30 hydrocarbon, the method comprising: mixing gaseous methane and a C2-C30 hydrocarbon to provide a mixture of methane and C2-C30 hydrocarbon, wherein the mixture comprises greater than or equal to about 50 mole percent of methane; maintaining the mixture of methane and C2-C30 hydrocarbon as a liquid solution at a pressure of 30 to 150 bar within a storage vessel, wherein the storage vessel comprises a porous adsorbent framework. The invention also relates to similar methods for storing hydrogen, nitrogen and carbon dioxide. The invention also relates to the use of a non-polar solvent such as a hydrocarbon for storing a non-polar gas in a porous adsorbent framework.

The invention relates a method for storing a solution of methane and a C2-C30 hydrocarbon, the method comprising: mixing gaseous methane and a C2-C30 hydrocarbon to provide a mixture of methane and C2-C30 hydrocarbon, wherein the mixture comprises greater than or equal to about 50 mole percent of methane; maintaining the mixture of methane and C2-C30 hydrocarbon as a liquid solution at a pressure of 30 to 150 bar within a storage vessel, wherein the storage vessel comprises a porous adsorbent framework. The invention also relates to similar methods for storing hydrogen, nitrogen and carbon dioxide. The invention also relates to the use of a non-polar solvent such as a hydrocarbon for storing a non-polar gas in a porous adsorbent framework.

A system and method for the on-site separating and treating of a hydrocarbon liquid stream at an oil and gas production site is disclosed. The system comprises an oil and condensate distillation unit and a vapor recovery unit. In one embodiment, the oil and condensate distillation unit operates at low pressure or vacuum conditions to reduce the vapor pressure above the column of oil within a distillation column, thereby increasing the production of oil and condensate and capturing entrained natural gas otherwise lost or burned off. In another embodiment, oil from the distillation column can be measured by a flow meter and then transferred to one or more of an oil tank, a mobile tank, and an oil pipeline. Optionally, produced water at the production site can be run through the oil and condensate distillation unit to reduce the volume of produced water. The system further functions to improve the quality and volume of recovered natural gas and to decrease air pollution, in addition to increasing oil and condensate production at the well site.

Systems and methods to provide low carbon intensity (CI) hydrogen through one or more targeted reductions of carbon emissions based upon an analysis of carbon emissions associated with a combination of various options for feedstock procurement, feedstock refining, processing, or transformation, and hydrogen distribution pathways to end users. Such options are selected to maintain the total CI (carbon emissions per unit energy) of the hydrogen below a pre-selected threshold that defines an upper limit of CI for the hydrogen.

Systems and methods to provide low carbon intensity (CI) hydrogen through one or more targeted reductions of carbon emissions based upon an analysis of carbon emissions associated with a combination of various options for feedstock procurement, feedstock refining, processing, or transformation, and hydrogen distribution pathways to end users. Such options are selected to maintain the total CI (carbon emissions per unit energy) of the hydrogen below a pre-selected threshold that defines an upper limit of CI for the hydrogen.

Systems and methods to provide low carbon intensity (CI) transportation fuels through one or more targeted reductions of carbon emissions based upon an analysis of carbon emissions associated with a combination of various options for feedstock procurement, feedstock refining, processing, or transformation, and fuel product distribution pathways to end users. Such options are selected to maintain the total CI (carbon emissions per unit energy) of the transportation fuel below a pre-selected threshold that defines an upper limit of CI for the transportation fuel.

Systems and methods to provide low carbon intensity (CI) transportation fuels through one or more targeted reductions of carbon emissions based upon an analysis of carbon emissions associated with a combination of various options for feedstock procurement, feedstock refining, processing, or transformation, and fuel product distribution pathways to end users. Such options are selected to maintain the total CI (carbon emissions per unit energy) of the transportation fuel below a pre-selected threshold that defines an upper limit of CI for the transportation fuel.

A method of and a system for processing a slurry containing organic components, such as biomass, having a water contents of at least 50%, comprises a pump and heater or heat exchanger to bring the liquid in the slurry in a supercritical state. A reactor converts at least a part of the organic components in the slurry. A separator removes gaseous products from the converted slurry. A mixer adds fluid from the converted slurry to the slurry upstream from the reactor.

A method of and a system for processing a slurry containing organic components, such as biomass, having a water contents of at least 50%, comprises a pump and heater or heat exchanger to bring the liquid in the slurry in a supercritical state. A reactor converts at least a part of the organic components in the slurry. A separator removes gaseous products from the converted slurry. A mixer adds fluid from the converted slurry to the slurry upstream from the reactor.