Fluidized bed process for retorting oil shale

Claim 1

A method for recovery of values from oil shale comprising the steps of: (a) introducing particulate oil shale feed containing carbonaceous material to a retorting zone fluidized bed wherein the retorting zone fluidized bed is fluidized at least partly by an upward flow therethrough of combustion gases substantially free of free oxygen and which do not react with products of retorting in a deleterious manner, the combustion gases maintaining the retorting zone fluidized bed at a temperature sufficient to retort oil shale to yield, as products of retorting, retorted oil shale containing residual carbonaceous material and retorting vapors comprising volatilized hydrocarbons; (b) passing retorted oil shale particles containing residual carbonaceous material from the bottom of the retorting zone fluidized bed downwardly to the top of a combustion zone fluidized bed by means of a rotary vane feeder; (c) introducing a gaseous source of oxygen into the combustion zone fluidized bed for fluidizing the combustion zone fluidized bed and for oxidizing residual carbonaceous material contained in retorted oil shale particles present in the combustion zone fluidized bed to yield combusted oil shale and combustion gases; (d) passing such combustion gases upwardly from the combustion zone fluidized bed to the retorting zone fluidized bed for fluidizing the retorting zone fluidized bed and for maintaining the retorting zone fluidized bed at a temperature sufficient to retort oil shale, wherein the combustion zone and retorting zone fluidized beds are contained in separate vessels, with the vessel containing the retorting zone fluidized bed being directly above the vessel containing the combustion zone fluidized bed, the upper portion of each vessel being expanded for disengagement of oil shale particles from fluidizing gas; (e) withdrawing a vapor mixture of combustion gases and retorting vapors comprising hydrocarbons and entrained retorted oil shale particles from the retorting zone fluidized bed; (f) separating entrained retorted oil shale particles from the vapor mixture; (g) recycling separated retorted oil shale particles to one of said fluidized beds; (h) condensing hydrocarbons from the vapor mixture; and (i) withdrawing combusted oil shale particles from the combustion zone fluidized bed.

Claim 2

A method for recovery of values from oil shale comprising the steps of: (a) introducing particulate oil shale feed containing carbonaceous material to a retorting zone fluidized bed wherein the retorting zone fluidized bed is fluidized at least partly by an upward flow therethrough of combustion gases substantially free of free oxygen and which do not react with products of retorting in a deleterious manner, the combustion gases maintaining the retorting zone fluidized bed at a temperature sufficient to retort oil shale to yield, as products of retorting, retorted oil shale containing residual carbonaceous material and retorting vapors comprising volatilized hydrocarbons; (b) passing retorted oil shale particles containing residual carbonaceous material from the bottom of the retorting zone fluidized bed downwardly to the top of a combustion zone fluidized bed by means of a rotary vane feeder; (c) introducing a gaseous source of oxygen into the combustion zone fluidized bed for fluidizing the combustion zone fluidized bed and for oxidizing residual carbonaceous material contained in retorted oil shale particles present in the combustion zone fluidized bed to yield combusted oil shale and combustion gases; (d) passing such combustion gases upwardly from the combustion zone fluidized bed to the retorting zone fluidized bed for fluidizing the retorting zone fluidized bed and for maintaining the retorting zone fluidized bed at a temperature sufficient to retort oil shale, wherein the combustion zone and retorting zone fluidized beds are contained in separate vessels, with the vessel containing the retorting zone fluidized bed being directly above the vessel containing the combustion zone fluidized bed, the upper portion of each vessel being expanded for disengagement of oil shale particles from fluidizing gas; (e) withdrawing a vapor mixture of combustion gases and retorting vapors comprising hydrocarbons and entrained retorted oil shale particles from the retorting zone fluidized bed; (f) separating entrained retorted oil shale particles from the vapor mixture; (g) recycling separated retorted oil shale particles to one of said fluidized beds; (h) condensing hydrocarbons from the vapor mixture; and (i) withdrawing combusted oil shale particles from the combustion zone fluidized bed.