Dilute phase waste incinerator

Claim 2

In an incineration process conducted in a fluid bed reactor to destroy organic waste material, the steps of fluidizing a bed of inert particulate solids at a space rate of at least about 4 ft./sec. to entirely fill said reactor with a dilute phase fluidized bed, maintaining said fluidized bed at a temperature of at least about 1200° F., introducing said organic waste material into said fluidized bed to burn the organics, essentially completely burning said organic waste material within said reactor, elutriating a substantial amount of bed fines and ash with the exhaust gases from said reactor, separating the solids from the gases in said exhaust gases while minimizing heat loss and returning said hot separated solids directly to the bed thereby conserving the heat generated in said reactor.

Claim 3

A process for the incineration of organic waste matter comprising establishing a fluidized bed of inert particles in a suitable combustion chamber, supplying a flow of combustion air through said fluidized bed at a space rate sufficiently high to entirely fill said combustion chamber with a dilute phase fluidized bed, said dilute phase fluidized bed ranging in density from about 20 lbs./cu. ft. in the upper region thereof up to about 60 lbs./cu. ft. in the lower region thereof, maintaining said fluidized bed at a temperature of at least about 1200° F., feeding said organic waste material into said dilute phase fluidized bed to subject the organic material to combustion, elutriating substantial amounts of hot solids comprised of bed material and ash with the exhaust combustion gases, separating hot solids from said exhaust gases and promptly returning said separated solids to the dilute phase fluidized bed thereby conserving the heat contained in said solids.

Claim 4

A process for the incineration of organic waste matter comprising establishing a fluidized bed of inert particles in a suitable combustion chamber, supplying a flow of combustion air through said fluidized bed at a space rate sufficiently high to entirely fill said combustion chamber with a dilute phase fluidized bed, said dilute phase fluidized bed ranging in density from about 20 lbs./cu. ft. in the upper region thereof up to about 60 lbs./cu. ft. in the lower region thereof, maintaining said fluidized bed at a temperature of at least about 1200° F., feeding said organic waste material into said dilute phase fluidized bed to subject the organic material to combustion, elutriating substantial amounts of hot solids comprised of bed material and ash with the exhaust combustion gases, separating hot solids from said exhaust gases and promptly returning said separated solids to the dilute phase fluidized bed thereby conserving the heat contained in said solids.

Claim 5

The incineration process of claim 2 wherein said space rate is in the range from about 4 ft./sec. up to about 20 ft./sec.

Claim 6

In an incineration process conducted in a fluid bed reactor to destroy organic waste material, the steps of fluidizing a bed of inert particulate solids at a space rate in the range from about 4 ft./sec. up to about 20 ft./sec. to substantially entirely fill said reactor with a dilute phase fluidized bed, maintaining said fluidized bed at a temperature in the range from about 1200° F. up to about 1400° F., introducing said organic waste material into said fluidized bed to burn the organics, elutriating a substantial amount of bed fines and ash with the exhaust gases from said reactor, separating the solids from the gases in said exhaust gases while minimizing heat loss and returning said hot separated solids to the bed thereby conserving the heat generated in said reactor.

Claim 7

In an incineration process conducted in a fluid bed reactor to destroy organic waste material, the steps of fluidizing a bed of inert particulate solids at a space rate in the range from about 4 ft./sec. up to about 20 ft./sec. to substantially entirely fill said reactor with a dilute phase fluidized bed, maintaining said fluidized bed at a temperature in the range from about 1200° F. up to about 1400° F., introducing said organic waste material into said fluidized bed to burn the organics, elutriating a substantial amount of bed fines and ash with the exhaust gases from said reactor, separating the solids from the gases in said exhaust gases while minimizing heat loss and returning said hot separated solids to the bed thereby conserving the heat generated in said reactor.

Claim 8

The incineration process of claim 4 wherein the density of said dilute phase fluidized bed is at least about 20 lbs./cu.ft.

Claim 9

The incineration process of claim 5 wherein the density of said dilute phase fluidized bed varies from about 20 lbs./cu.ft. in an upper region of said fluidized bed to about 60 lbs./cu.ft. in a lower region of said fluidized bed.