A portable, yard waste incinerator system that includes a transport vehicle with a large burn tank configured for burning yard waste. Located inside the burn tank is a primary burner that forms an inner primary combustion chamber and an outer secondary chamber. Propane fuel is connected to an external propane gas source which delivers propane to the primary combustion chamber. The primary burner includes a plurality of holes that allows flames and hot gases from the fire and heat from the primary combustion chamber to extend into a secondary combustion chamber. The system also includes a vacuum system connected to the burn tank which picks up small, loose combustible debris from the yard and delivers the debris and oxygen to the secondary combustion chamber. The system also includes an optional electric generator that energizes the vacuum system and an optional shredder that delivers shredded yard waste to the secondary burning chamber.

A process of making a fuel product from a non-combustible high protein organic material such as a biological by-product or waste material. The moisture content of the high protein organic material is mechanically reduced and dried to reduce the moisture content to less than ten percent (10%). The high protein organic material is pulverized to a particle size of less than about 2 mm. The high protein organic waste material is fed into a combustion chamber and separated during combustion such as by spraying of the high protein organic waste material within the combustion chamber. Temperature and nitrogenous hydrocarbon combustion reactions within the combustion chamber are also controlled by injection of steam within the combustion chamber.

The present invention provides a biomass combustion burner applied to a pulverized coal-fired boiler to burn biomass fuel, a biomass-mixed fired boiler that reduces an amount of CO2 derived from fossil fuels, and a method for burning biomass fuel using the foregoing. The biomass combustion burner includes a biomass fuel jet nozzle having a fuel jet port that jets biomass fuel conveyed by primary air; a secondary air nozzle having a secondary air jet port that surrounds the fuel jet port; and a tertiary air nozzle having a tertiary air jet port that surrounds the secondary air jet port. The biomass fuel jet nozzle includes a fuel concentration adjusting section that changes a biomass fuel stream into a swirl flow to thereby make a fuel concentration higher on an outer circumferential portion side; and a degree-of-swirl adjusting plate that reduces a degree of swirl of a jetting fuel stream.

An apparatus for waste recycling that is suitable for residence building level in both volume and rate of supply of waste with a waste disposal and treatment container having the following parts: waste eliminator comprising a thermally and acoustically insulating casing with odour insulating raw waste receiving space; all-purpose shredder and crusher; crushed and/or shredded waste conveyor; liquid waste purifier; gasification plasma reactor; gas conveyor and purifier; slag collector; re-hydration means for re-hydrating solid waste in the gasification plasma reactor; and safety means. Each one of these parts is organized in fluid communication with its neighbor parts.

A process is described for treating waste plastics material to provide at least one on-specification fuel product. Plastics material is melted and then pyrolyzed in an oxygen-free atmosphere to provide pyrolysis gases. The pyrolysis gases are brought into contact with plates in a contactor vessel so that some long chain gas components condense and return to be further pyrolyzed to achieve thermal degradation. Short chain gas components exit the contactor in gaseous form and proceed to distillation to provide one or more on-specification fuel products. A pipe directly links the pyrolysis chamber to the contactor, suitable for conveying upwardly-moving pyrolysis gases and downwardly-flowing long-chain liquid for thermal degradation.

This present invention relates to a eco-friendly ultra-high temperature thermal decomposition system for waste-to-energy, where its thermal decomposition chamber made with special castable mixture maintains the ultra-high temperature above 850? C. and ten (10) layers of air curtains made by a double-layered air-curtain maker installed at the center of the thermal decomposition chamber allows the input materials to be completely decomposed without any auxiliary fuel and air pollutants to be completely decomposed by trapping them inside the thermal decomposition chamber with ultra-high temperature above 850? C. for more than two (2) seconds of residence time, as well as its two (2) layers of oil nozzles, central oil nozzles and lower oil nozzles, installed on the inner wall of the thermal decomposition chamber, each installed to aim the central part and the bottom part of the thermal decomposition chamber, evenly spraying the auxiliary fuel when necessary so the input materials with different conditions, sizes, and hydration level, are completely decomposed; furthermore, its outer shredder, installed at the left side of the thermal decomposition chamber, improves its treatment efficacy by homogenizing the input materials with different conditions, sizes, and hydration level, prior to being fed into the thermal decomposition chamber, with a screw conveyor connecting the outer shredder and the thermal decomposition chamber automatically feeding the input materials, as well as its inner shredder installed at the bottom part of the thermal decomposition chamber shreds the ash and the input materials that are not being decomposed yet piled up at the bottom of the thermal decomposition chamber so the screw conveyor connecting the inner shredder and the thermal decomposition chamber can re-input such materials back to the thermal decomposition chamber, thus even the ash is also completely decomposed; moreover, its thermal generation modules, installed in the thermal generation chamber around the thermal decomposition chamber and on the upper cover of the thermal decomposition chamber, effectively collect the waste heat generated from thermal decomposition process to generate electricity while the waste heat is also used to generate steam via the steam chamber installed on the upper cover of the thermal decomposition chamber, where such steam is sent to separately composed boiler and steam turbine via steam pipe to generate further electricity; and lastly, its dust collector and the monitoring device are located at the right side of the thermal decomposition chamber with their collecting holes at the top part of inner wall of the thermal decomposition chamber to col

A method and system for cost effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into 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.

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.

A garbage supply device, which supplies waste to a gasification furnace that gasifies waste, includes a casing, two feed screws provided in the casing, and a middle shaft that is provided between the two supply screws, has a plurality of protrusions, and is repeatedly rotated forward or backward.

A method and system for cost effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into 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 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.