Method and apparatus for treating waste containing organic contaminants

Claim 1

The method of removing unwanted organic materials from a matrix in a countercurrent, direct fired, rotary kiln having a burner which is selectively positionable along the length of said kiln, comprising the steps of feeding the matrix into one end of said kiln and discharging the treated matrix from the other end of said kiln, delivering hydrocarbon fuel to the burner together with sufficient air at the point of combustion to essentially only effect combustion of the fuel to maintain the kiln at a temperature at from about 1300°-1800° F. and develop a substantially non-oxidizing material treatment environment between said burner and the point of entry of said matrix into said kiln, conducting off-gas from the kiln at its matrix feed end to a subsequent treatment means, positioning the burner at a selectable location along the length of said kiln spaced from the feed end a sufficient distance to dry, desorb, and pyrolyze substantially all of said unwanted organic materials by the time they reach the position of said burner and further defining a second material treatment zone between said burner and said discharge end, and admitting auxiliary air to said second material treatment zone thereby maintaining an oxidizing atmosphere in the area of said kiln between said burner and the discharge end of said kiln whereby the volume of combustion air and auxiliary air is less than enough to completely oxidize said unwanted organic materials that have been evaporated, desorbed or pyrolyzed and retaining the matrix in said material treatment zone a sufficient period of time to oxidize any remaining organic materials prior to discharge from said kiln.

Claim 2

The method of removing unwanted organic materials from a matrix in a countercurrent, direct fired, rotary kiln having a burner which is selectively positionable along the length of said kiln, comprising the steps of feeding the matrix into one end of said kiln and discharging the treated matrix from the other end of said kiln, delivering hydrocarbon fuel to the burner together with sufficient air at the point of combustion to essentially only effect combustion of the fuel to maintain the kiln at a temperature at from about 1300°-1800° F. and develop a substantially non-oxidizing material treatment environment between said burner and the point of entry of said matrix into said kiln, conducting off-gas from the kiln at its matrix feed end to a subsequent treatment means, positioning the burner at a selectable location along the length of said kiln spaced from the feed end a sufficient distance to dry, desorb, and pyrolyze substantially all of said unwanted organic materials by the time they reach the position of said burner and further defining a second material treatment zone between said burner and said discharge end, and admitting auxiliary air to said second material treatment zone thereby maintaining an oxidizing atmosphere in the area of said kiln between said burner and the discharge end of said kiln whereby the volume of combustion air and auxiliary air is less than enough to completely oxidize said unwanted organic materials that have been evaporated, desorbed or pyrolyzed and retaining the matrix in said material treatment zone a sufficient period of time to oxidize any remaining organic materials prior to discharge from said kiln.