Abstract:
A system for digesting biodigestible feed that preferably includes the steps of comminuting the feed, introducing feed, an oxygen-containing gas, an accelerant, and bacteria into a digestion zone, the bacteria being suitable for digesting the feed under aerobic, anaerobic, and anoxic conditions. The contents of the digestion zone can be changed from aerobic operation to either anoxic or anaerobic operation, or vice versa, without changing the bacteria in the digestion zone.
Abstract:
A system for digesting biodigestible feed that preferably includes the steps of comminuting the feed, introducing feed, an oxygen-containing gas, an accelerant, and bacteria into a digestion zone, the bacteria being suitable for digesting the feed under aerobic, anaerobic, and anoxic conditions. The contents of the digestion zone can be changed from aerobic operation to either anoxic or anaerobic operation, or vice versa, without changing the bacteria in the digestion zone.
Abstract:
A method for disposing of solid refinery waste is disclosed. The method includes removing solid waste constituents from inside a refinery tank using excavating machinery, delumping the solid waste constituents, and conveying the delumped solid waste constituents into a mobile tank. The method further includes transporting the delumped solid waste constituents in the mobile tank to a burning facility, adding at least one diluent, mixing, and pumping from the mobile tank a flowable mixture of refinery waste and the at least one diluent at the burning facility.
Abstract:
A method and system for cost effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into to a feedwater energy transfer system. The feedstock can be any organic material, or fossil fuel. The energy transferred in the feedwater is converted into steam which is then injected into the low turbine of a combined cycle power plant. Heat is extracted from gas product issued by a gassifier and delivered to a power plant via its feedwater system. The gassifier is a plasma gassifier and the gas product is syngas. In a further embodiment, prior to performing the step of extracting heat energy, there is provided the further step of combusting the syngas in an afterburner. An air flow, and/or EGR flow is provided to the afterburner at a rate that is varied in response to an operating characteristic of the afterburner. The air flow to the afterburner is heated.
Abstract:
A waste-to-energy conversion apparatus comprising a primary combustion chamber capable of holding a load of waste, and the primary combustion chamber further comprises a heat source to heat the waste and generate a syn gas stream, grates, within the primary chamber, capable of supporting the load of waste during heating, a mixing chamber wherein the syn gas is mixed with additional combustion gas, a multi-chambered secondary combustion chamber for combusting the mixture of syn gas and additional combustion gas, and an energy extraction system for extracting the heat energy generated by the combustion of the mixture of syn gas and additional combustion gas.
Abstract:
Oxycombustion process wherein a combustor is fed with a fuel, a comburent and compounds under the form of coherent aggregates having Young modulus ≧104 MPa, the combustor being isothermal and flameless.
Abstract:
An apparatus for disposing of solid refinery waste is disclosed. The apparatus includes a mixing apparatus for mixing refinery solid waste in a mobile tank. The mixing apparatus may include an agitator, an external support, and an actuator connectable to the external support. The external support may be configured for disposition adjacent to a manhole opening in a top of the mobile tank for supporting the agitator in the mobile tank.
Abstract:
An automated system and method are provided for conveying plant material bales. The system and method retrieves stacked bales from a storage site and places the bales on a conveyor assembly line, wherein the bales are indexed, accumulated, and metered for discharge into a bale shredder. Once the bales are on the conveyor assembly, the bales are automatically moved and arranged without manual intervention.
Abstract:
A vehicle configured to carry solid refinery waste is disclosed. The vehicle includes a mobile tank including a plurality of compartments and at least one buffer disposed between each of the plurality of compartments. The vehicle further includes a plurality of manhole openings on a top wall of the tank, each manhole opening being associated with one of the plurality of compartments and being sized to enable an agitator to pass therethrough. The vehicle also includes a plurality of connectors, each connector being affixed to the mobile tank for movement therewith to selectively secure the agitator and a plurality of fluid valves sized to permit an emulsion of the solid refinery waste and at least one diluent to pass therethrough in flowable form.
Abstract:
A method for disposing of solid refinery waste is disclosed. The method includes removing solid waste constituents from inside a refinery tank using excavating machinery, delumping the solid waste constituents, and conveying the delumped solid waste constituents into a mobile tank. The method further includes transporting the delumped solid waste constituents in the mobile tank to a burning facility, adding at least one diluent, mixing, and pumping from the mobile tank a flowable mixture of refinery waste and the at least one diluent at the burning facility.