Abstract There is disclosed an improved process for activating carbon in a fluidized bed which includes continuous activation at a temperature between 1,000 DEG F. and 2,200 DEG F., preferably 1,700 DEG F. to 1,950 DEG F. in the bed. The activation step includes heat transfer by conduction through a distributor plate to the bed and means to achieve a high degree of particle agitation, thus allowing a continuous activation of carbon without the formation of sintered coal ash. The prevention of coal ash sintering allows the process to continue over long periods of time without frequent shutdowns. Carbonaceous material is fed into an initial compartment and a bed is formed on the floor of the compartment. The floor is a gas permeable distributor plate. Fluidizing gases are introduced through the plate into this compartment. As the carbonaceous material is added, some carbonaceous material overflows the initial compartment and forms a bed in another compartment. The second compartment is like the first compartment. By overflowing, the carbonaceous material moves through a plurality of similar compartments until it exits the activator as activated carbon. The thermal energy required to activate the carbonaceous material and to maintain the bed temperature is generated by combustion of fuel in a combustion chamber located beneath the plate. It is the purpose of this invention to provide a process whereby a substantial part of the thermal energy is transferred to the bed by conduction through the distributor plate.
A process for manufacturing activated carbon from granular coal particles that have been rendered non-agglomerative and carbonized which comprises: a. continuously feeding said non-agglomerative and carbonized coal particles into a fluidized bed supported on a horizontal gas distributor plate; b. and at the same time passing an activating gas from below through said gas distributor plate at a velocity at least sufficient to provide for fluidizing said coal particles, said gas distributor plate having tuyeres projecting above the upper surface of said plate whereby substantially all of said coal particles on the upper plate surface in said fluidized bed are in continuous motion; c. activating said coal particles by maintaining a constant level of thermal energy required for activation at maximum yield in said fluidized bed by supplying, 1. at least 10% of said thermal energy by conduction of heat from hot activating gas below said distributor plate through said plate to the fluidized bed, and 2. the remainder of said thermal energy being supplied by the sensible heat of the activating gas to thereby provide a temperature in said fluidized bed between 1,000°F. and 2,200°F. while maintaining the upper surface of said gas distributor plate below the sintering temperature of said coal particles; and d. separating the gases from the thus activated carbon and recovering said activated carbon.
Claim 2
Dependent Claim
219 words
A process for manufacturing activated carbon from granular coal particles that have been rendered non-agglomerative and carbonized which comprises: a. continuously feeding said non-agglomerative and carbonized coal particles into a fluidized bed supported on a horizontal gas distributor plate; b. and at the same time passing an activating gas from below through said gas distributor plate at a velocity at least sufficient to provide for fluidizing said coal particles, said gas distributor plate having tuyeres projecting above the upper surface of said plate whereby substantially all of said coal particles on the upper plate surface in said fluidized bed are in continuous motion; c. activating said coal particles by maintaining a constant level of thermal energy required for activation at maximum yield in said fluidized bed by supplying, 1. at least 10% of said thermal energy by conduction of heat from hot activating gas below said distributor plate through said plate to the fluidized bed, and 2. the remainder of said thermal energy being supplied by the sensible heat of the activating gas to thereby provide a temperature in said fluidized bed between 1,000°F. and 2,200°F. while maintaining the upper surface of said gas distributor plate below the sintering temperature of said coal particles; and d. separating the gases from the thus activated carbon and recovering said activated carbon.
Claim 3
Dependent Claim
19 words
The process according to claim 1 wherein said activation is carried out in a plurality of interconnected fluidized beds.
Claim 4
Dependent Claim
23 words
The process according to claim 2 wherein the temperature in said fluidized beds is maintained constant at a temperature between 1,700°F. and 1,950°F.
Claim 5
Dependent Claim
25 words
The process according to claim 2 wherein the activating gas is a mixture of steam and the gas formed by the combustion of a hydrocarbon.
Claim 6
Dependent Claim
27 words
The process according to claim 1 wherein at least a majority of the thermal energy required for activation is supplied by conduction through said gas distributor plate.