An oil-water emulsion breakup system. In one embodiment, the system includes an oil-water mixture inlet line configured to receive an oil and water liquid mixture, which may be stabilized by hydrophobic nanoparticles, surfactants of low HLB value, or both. A water injection inlet in communication with the oil-water mixture inlet is configured to direct water into the oil-water mixture inlet. A water sensor is in communication with the oil-water mixture inlet to sense percentage of water in the mixture. A water injection valve in the water injection inlet is in communication with the water sensor. A liquid-liquid separator has an inlet configured to receive a combination of the oil and water mixture and the water, with the separator separating liquid into an oil phase and a water phase. An upper leg in communication with the liquid-liquid separator receives oil separated from the separator. A lower leg in communication with the liquid-liquid separator receives water separated in the liquid-liquid separator.

An oil-water emulsion breakup system. In one embodiment, the system includes an oil-water mixture inlet line configured to receive an oil and water liquid mixture, which may be stabilized by hydrophobic nanoparticles, surfactants of low HLB value, or both. A water injection inlet in communication with the oil-water mixture inlet is configured to direct water into the oil-water mixture inlet. A water sensor is in communication with the oil-water mixture inlet to sense percentage of water in the mixture. A water injection valve in the water injection inlet is in communication with the water sensor. A liquid-liquid separator has an inlet configured to receive a combination of the oil and water mixture and the water, with the separator separating liquid into an oil phase and a water phase. An upper leg in communication with the liquid-liquid separator receives oil separated from the separator. A lower leg in communication with the liquid-liquid separator receives water separated in the liquid-liquid separator.

Disclosed herein is an integrated plant including, in some embodiments, an interconnected set of two or more stages of reactors forming a bio-reforming reactor configured to generate syngas from wood-containing biomass. A first stage of the bio-reforming reactor is configured to cause a set of chemical reactions in the biomass to produce reaction products of constituent gases, tars, chars, and other components. The first stage includes a fluidized-bed gasifier, a fluidized-bed combustor, and a moving-bed filtration system, each of which includes media inputs and outputs to respectively receive and supply heat-absorbing media to another operation unit for recirculation in a media recirculation loop. The moving-bed filtration system includes a tar pre-reformer configured to capture and reform heavier tars into lighter tars for subsequent processing in one or more fuel-producing reactor trains. Fuel products produced by the one or more reactor trains have a biogenic content of between 50% and 100%.

Disclosed herein is an integrated plant including, in some embodiments, an interconnected set of two or more stages of reactors forming a bio-reforming reactor configured to generate syngas from wood-containing biomass. A first stage of the bio-reforming reactor is configured to cause a set of chemical reactions in the biomass to produce reaction products of constituent gases, tars, chars, and other components. The first stage includes a fluidized-bed gasifier, a fluidized-bed combustor, and a moving-bed filtration system, each of which includes media inputs and outputs to respectively receive and supply heat-absorbing media to another operation unit for recirculation in a media recirculation loop. The moving-bed filtration system includes a tar pre-reformer configured to capture and reform heavier tars into lighter tars for subsequent processing in one or more fuel-producing reactor trains. Fuel products produced by the one or more reactor trains have a biogenic content of between 50% and 100%.

A cyclonic separator is taught, comprising at least two cyclonic chambers in the form of cylindrical tubes, having an upper inlet end and a lower liquid outlet end, a common tangential inlet in fluid communication with the upper end of each of the at least two cyclonic chambers, a gas outlet proximal to and extending upwardly from the upper ends of each of the at least two cyclonic chambers and a common outer shell surrounding the at least two cyclonic chambers, wherein said common tangential inlet extends through said common outer shell and into each of said at least two cyclonic chambers. A method for separation of a mixed heavy phase/light phase process stream is also taught.

A system for treatment of contaminated sediments and soils using free radical chemical reaction and phase separation processes comprises a sediment or soil inlet system, a slurry tank, wherein the inlet system feeds the slurry tank, a water make-up tank, an optional acid storage tank, wherein the water make-up tank and the acid storage tank are connected to the slurry tank, a reaction vessel, wherein the slurry tank is connected to the reaction vessel, an oxidant agent storage tank, an optional catalyst storage tank, wherein the oxidant agent storage tank and the catalyst storage tank are connected to the reaction vessel, a first particle separator, wherein the reaction vessel is connected to the first particle separator, and an oil/water separator, wherein the first particle separator is connected to the oil/water separator is disclosed. A method for treatment of contaminated sediments and soils is also disclosed.

A system for treatment of contaminated sediments and soils using free radical chemical reaction and phase separation processes comprises a sediment or soil inlet system, a slurry tank, wherein the inlet system feeds the slurry tank, a water make-up tank, an optional acid storage tank, wherein the water make-up tank and the acid storage tank are connected to the slurry tank, a reaction vessel, wherein the slurry tank is connected to the reaction vessel, an oxidant agent storage tank, an optional catalyst storage tank, wherein the oxidant agent storage tank and the catalyst storage tank are connected to the reaction vessel, a first particle separator, wherein the reaction vessel is connected to the first particle separator, and an oil/water separator, wherein the first particle separator is connected to the oil/water separator is disclosed. A method for treatment of contaminated sediments and soils is also disclosed.