Abstract: A method for treating contaminated solids such as contaminated soil or sludge includes feeding the solids into a preheater and pneumatically conveying the solids through the preheater by preheated primary air into and through an oxidation chamber by cocurrent flow. Secondary air is directed into the oxidation chamber through a plurality of perforations in the wall of the oxidation chamber to combine with and sustain the fluidized state of the solid-gas mixture. The primary air is preferably produced by an air blower which blows the air through a preheater to produce hot air. The temperature of the fluidized bed is controlled by the temperature of the primary air. The temperature should be hot enough that the lighter hydrocarbons spontaneously ignite in the oxidation chamber. The exothermic combustion causes the remaining organic material present in the contaminated solids to then vaporize and burn.

Abstract: A method for treating an emulsion of hydrocarbons and solids such as sludge includes spraying the sludge into a preheater and pneumatically conveying it by primary air into an oxidation chamber. Secondary air is directed into the oxidation chamber through a plurality of perforations in the wall of the oxidation chamber to combine with and sustain the fluidized state of the solid-gas mixture. The primary air is preferably produced by passing the proceeds of an air blower through a preheater to produce hot air. The oxidizer is arranged at an incline so that the gas solid mixture of hot air and contaminated soil flows upwardly. The temperature of the fluidized bed is controlled by the temperature of the primary air so that lighter hydrocarbons spontaneously ignite in the oxidation chamber. The exothermic combustion causes the remaining organic material present in the contaminated solids to vaporize and burn.

Abstract: A method for treating soil that has become contaminated with hydrocarbons or other organic material includes straining the contaminated material through a rotary air lock into a preheater and pneumatic conveying by primary air into an oxidation chamber. Secondary air is directed into the oxidation chamber through a plurality of perforations in the wall of the oxidation chamber to combine with and sustain the fluidized state of the soil-gas mixture. The primary and secondary air is preferably produced by passing the proceeds of an air blower through a pre-heating assembly to produce hot air. The oxidizer is arranged at an incline so that the gas solid mixture of hot air and contaminated soil flows upwardly. The temperature of the fluidized bed is controlled by the temperature of primary air so that lighter hydrocarbons spontaneously ignite in the oxidation chamber. The exothermic combustion causes the remaining organic material present in the contaminated soil to vaporize and burn.