A solid-fuel burning and drying unit capable of carbonized drying and burning of toxic gases, having a main body with a fuel cell configured in the main body, a barrier surface which closes the fuel cell from the upper region and enables combustion of toxic and volatile gases in the combustion zone without mixing with the atmosphere, fuel supply elements and fuel discharge elements that deliver fuels to be burned into the fuel cell, wherein the said main body contains a drying unit in which the damp fuel is dried by heat from the combustion zone by generating frictional energy by rotating through the configured drive element and coils on the axis of rotation (z).

A method for drying biomass fuel using waste heat of flue gas from a power plant. The method includes: 1) stepwise recovering, by multi-stage condensation, sensible heat of flue gas; stepwise heating air using the sensible heat, to yield first-stage dry air and second-stage dry air; 2) convectively drying and dehydrating biomass fuel using the first-stage dry air having a temperature of between 150 and 180° C.; 3) further convectively drying and dehydrating the biomass fuel using the second-stage dry air having a temperature of between 80 and 100° C.; and 4) drying and dehydrating the biomass fuel using the third-stage dry air having a temperature of less than or equal to 25° C.

The present invention relates to a waste feed device for feeding waste into a combustion space of a waste incineration plant, including a waste feed shaft wall surrounding a waste feed shaft. In this case, at least part of the waste feed shaft wall is formed from a multiplicity of separate panels which are connected releasably to one another and which comprise, on their side facing the waste feed shaft, a panel inner wall and, on their side facing away from the waste feed shaft, a panel outer wall which is spaced apart from the panel inner wall and which with the panel inner wall surrounds a panel cavity.

Provided is a plastic waste solid fuel incinerator comprising: an incinerator housing which has, on the upper portion thereof, a gas outlet through which combustion gas is discharged; a fuel supply unit which transfers and supplies a plastic waste solid fuel; a first combustion unit which continuously transfers and burns the supplied plastic waste solid fuel; a first air supply unit which supplies air needed for combustion to the first combustion unit; a combustion gas induction unit which induces the combustion gas generated from the first combustion unit toward the lower portion of a first combustion chamber; a second combustion unit which is arranged in the lower portion of the first combustion unit and comprises a downward injection nozzle unit which downwardly injects the combustion gas supplied through the combustion gas induction unit in order to reburn the combustion gas; and a second air supply unit which is arranged in the lower portion of the second combustion unit and supplies the air needed for combustion to the second combustion unit by downwardly injecting the air. Accordingly, there is an advantage of allowing continuous combustion using combustion gas generated during the combustion of the plastic waste solid fuel without using a separate auxiliary fuel, thereby reducing incineration costs.

There is provided a combustible waste injection device and a method for operating the same which can suppress a landing combustion of a combustible waste and suppress excessive change of a flame state from a cement kiln burner even if a rate of using the combustible waste fluctuates. The combustible waste injection device according to the present invention is provided with a combustible waste flow channel which is arranged in an inner side of the air flow channel in an innermost shell, is installed in parallel to an axial direction of the cement kiln burner device and is provided for flow feeding a combustible waste flow, and an assist air inflow port which can flow an assist air flow into the combustible waste flow channel toward an axis center of the combustible waste flow channel in the vicinity of an injection port of the combustible waste flow channel, and the assist air inflow port is arranged at a plurality of positions in relation to a circumferential direction.

An apparatus for recycling fly ash has a quantum energy generator therein. The apparatus recycles fly ash generated as the combustion waste from the burning of coal in thermal power plants, into construction materials such as cement substitutes, environment-friendly cover materials, etc. Unburned pulverized coal is removed while generating carbon monoxide (CO) or carbon dioxide (CO.sub.2) through a combustion reaction, in which the unburned pulverized coal of the fly ash contacts the thermal electrons discharged during a thermal decomposition process at a high temperature, the negative electrodes of the thermal decomposition part, which are heated at a high temperature of 500° C., which is an ignition point of the unburned pulverized coal, or higher, and a high-voltage discharge electrode of an electrochemical reaction part, then heated at 500° C. or higher, and then naturally burned under an oxygen atmosphere (oxygen or ionized oxygen ions in air contained in the fly ash).

A biochar apparatus and a related biochar module may have a horizontal table-shaking mechanism and a tapered channel for causing biochar pieces generated in a firebox to fall through openings in the table to a conveyor system below. The table may be configured with replaceable grate panels. A quenching reservoir pan for holding quenching liquid receives a drainage basket at a discharge end of the conveyor system for quenching hot pieces of biochar and allowing easy retrieval of the quenched pieces.

A kinetic feed plug screw apparatus and process for creating the same, where organic raw material or feedstock is transported to a combustion or pyrolysis chamber, and a dynamic seal is concurrently and continuously created between the inlet and outlet to prevent immediate material blowback.

A vacuum cracking method and a cracking apparatus for a power battery are disclosed. The vacuum cracking method includes the following steps that: waste power batteries are fed from a feed hopper and then enter a rolling unit for rolling treatment to obtain a crushed material; the crushed material is transported to a cracking unit for preheating, then heated and cracked under an inert atmosphere or vacuum to obtain cracked gas, solid cracked products and non-crackable products; and the solid cracked products and the non-crackable products are transported to a pyrolysis unit for pyrolysis at an aerobic atmosphere to obtain pyrolysis gas and non-pyrolysis products.

A bale boiler incinerates bales of material, and particularly bales made from waste, garbage and other refuse, in order to provide heat for a steam turbine generator, and includes a conveyor for transporting bales of waste material through a three-stage boiler. The boiler is preferably divided into three stages: 1) the warming stage, 2) the main incineration stage, and 3) the supplemental incineration stage. In the warming stage, the bale is warmed and dried. In the main incineration stage, the bale is burned to create heat that is then used to power a steam turbine electrical generator or the like. In the third, supplemental incineration stage, the remnants of the bale burn down to ash, and the remaining ash and non-combustible waste are then transported out of the boiler by the conveyor and dumped into a receptacle or container for transport and disposal.