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An apparatus and process for preparing activated carbon from a wood or wood residue feedstock using fluidized bed technology. The fluidized bed apparatus has a number of wood residue inlets that allow differing residence times in the fluidized bed apparatus appropriate for the wood or wood residue f

An apparatus and process for preparing activated carbon from a wood or wood residue feedstock using fluidized bed technology. The fluidized bed apparatus has a number of wood residue inlets that allow differing residence times in the fluidized bed apparatus appropriate for the wood or wood residue feedstock to be carbonized. The carbonized material may then be activated to form activated carbon.

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1. A process for carbonizing wood residues to produce charcoal, said wood residues including wood or woody-type particles of varying size and/or moisture content, the process including the steps of feeding the wood residue to a fluidized bed having a plurality of wood residue inlets, the wood or woo

1. A process for carbonizing wood residues to produce charcoal, said wood residues including wood or woody-type particles of varying size and/or moisture content, the process including the steps of feeding the wood residue to a fluidized bed having a plurality of wood residue inlets, the wood or woody-type particles of varying size and/or dryness being fed to differing ones of the plurality of wood residue inlets according to an expected time for carbonization for said wood or woody-type particles, the fluidized bed including a bed of inert particulate material fluidized with or having injected therein a gas or gas mixture containing an oxidizing gas, carbonizing the wood residues in the fluidized bed under reaction conditions selected such that volatile components in the wood residues are removed during carbonization and are burned in or above the bed or in an afterburner to thereby supply the heat requirements for carbonization and separating charcoal from the inert particulate material. 2. An apparatus for carbonizing wood residues to produce charcoal including a fluidized bed reactor having a plurality of wood residue inlets for supplying wood residues including wood or woody-type particles of varying size and/or moisture content, a discharge outlet for removing fluidized bed contents from the fluidized bed and at least one fluidizing gas inlet, characterized in that each one of said plurality of wood residue inlets is positioned at different locations with respect to said discharge outlet and that residence time of or woody type particle in the fluidize bed reactor is dependent upon the inlet through which the wood or woody type particle is fed to the fluidized bed reactor. 3. The apparatus of claim 2 further including a separating means for separating charcoal from the fluidized bed contents removed from the discharge outlet and return means for returning inert particulate material to the fluidized bed reactor. 4. The apparatus of claim 3, wherein the return means comprises a conduit connected to an inlet. 5. The apparatus of claim 4 wherein the conduit is provided with particulate material transport means selected from a group consisting of a conveyor, a screw conveyor, an augur, pneumatic conveying means and gaseous conveying means. 6. The apparatus of any one of claims 3 to 5 wherein the separating means is a screen means. 7. The apparatus of claim 6 wherein said screen means is a vibratory screen means. 8. The apparatus of claim 2 wherein the apparatus further includes an afterburner for burning any uncombusted volatiles in the exhaust gas. 9. An apparatus for producing activated carbon including:a furnace;a reactor positioned inside the furnace, the reactor including solids inlet means for supplying solids to the reactor and gas inlet means for supplying gas to the reactor, at least one pipe connected to the gas inlet means of the reactor, said at least one pipe having at least a portion of its length extending within the furnace whereby gas flowing through said at least one pipe to the reactor is heated to an elevated temperature by the furnace; anda gas manifold inside the furnace, the gas manifold having an inlet and a plurality of outlets, each of the plurality of manifold outlets having respective ones of a plurality of pipes extending therefrom, the plurality of pipes being connected at their other ends to the gas inlet means of the reactor. 10. The apparatus of claim 9 wherein the reactor is a fluidized bed reactor. 11. The apparatus of claim 9 or 10 wherein at least one pipe has a substantial portion of its length extending within the furnace. 12. The apparatus of claim 4 wherein at least one pipe is positioned within the furnace and external to the reactor. 13. A process for carbonizing wood residues to produce activated carbon, said wood residues including wood or woody-type particles of varying size and/or moisture consent, the process including the steps of:feeding the wood residue to a first fluidized bed having a plurality of wood residue inlets, the wood or woody-type particles of varying size and/or dryness being fed to differing ones of the plurality of wood residue inlets according to an expected time for carbonization for said wood or woody-type particles, the first fluidized bed including a bed of inert particulate material fluidized with or having injected therein a gas or gas mixture containing an oxidizing gas;carbonizing the wood residues in the fluidized bed under reaction conditions selected such that volatile components in the wood residues are removed during carbonization and are burned in or above the bed or in an afterburner to thereby supply the heat requirements for carbonization;separating charcoal from the inert particulate material of the first fluidized bed;adding particulate material to a second fluidized bed reactor to form a bed of particulate material;adding said charcoal to said second fluidized bed reactor and fluidizing the bed;activating the carbon feedstock by adding superheated steam to the fluidized bed to produce activated carbon; andrecovering activated carbon from the bed. 14. A process according to claim 13 wherein the step of activating the carbon feedstock includes adding steam to the fluidized bed. 15. A process according to claim 14 wherein steam is used as the fluidizing gas in the fluidised bed. 16. A process according to claim 13 or claim 14 wherein the steam is super heated steam.