Activated sludge system with staggered partition basin

Claim 1

The method of reducing the oxygen demand of mixed liquor in an aeration basin of an activated sludge purification system comprising: a. flowing said mixed liquor through said aeration basin from an inlet end to an outlet end, b. partitioning said aeration basin into a plurality of liquid passes formed by a plurality of staggered partitions extending partially across the width of said basin and extending throughout the depth of the mixed liquor, c. flowing said mixed liquor through said plurality of liquid passes in a non-restricted serpentine manner by maintaining an open cross-sectional flowpath area between adjacent liquid passes within the range of 30% to 80% of the wetted cross-sectional area of said basin, d. aerating said mixed liquor as it flows through said liquid passes with a plurality of aerators, e. operating each of said liquid passes in a non-completely mixed mode so as to have a non-uniform oxygen demand throughout each liquid pass, f. maintaining intra-zone and inter-zone backflow within and between each of said liquid passes, g. maintaining the aerator mixing factor of each of said aerators within the range of 20 to 450, and h. maintaining the effective liquid staging greater than one effective liquid stage per actual liquid pass.

Claim 2

The method of reducing the oxygen demand of mixed liquor in an aeration basin of an activated sludge purification system comprising: a. flowing said mixed liquor through said aeration basin from an inlet end to an outlet end, b. partitioning said aeration basin into a plurality of liquid passes formed by a plurality of staggered partitions extending partially across the width of said basin and extending throughout the depth of the mixed liquor, c. flowing said mixed liquor through said plurality of liquid passes in a non-restricted serpentine manner by maintaining an open cross-sectional flowpath area between adjacent liquid passes within the range of 30% to 80% of the wetted cross-sectional area of said basin, d. aerating said mixed liquor as it flows through said liquid passes with a plurality of aerators, e. operating each of said liquid passes in a non-completely mixed mode so as to have a non-uniform oxygen demand throughout each liquid pass, f. maintaining intra-zone and inter-zone backflow within and between each of said liquid passes, g. maintaining the aerator mixing factor of each of said aerators within the range of 20 to 450, and h. maintaining the effective liquid staging greater than one effective liquid stage per actual liquid pass.

Claim 5

The method of reducing the oxygen demand of mixed liquor in an elongated, rectangular aeration basin of an activated sludge purification system comprising: a. flowing said mixed liquor through said aeration basin from an inlet end to an outlet end, b. partitioning said aeration basin into a plurality of liquid passes formed by a plurality of staggered partitions extending from alternate side walls for a distance in the order of one half the width of said basin and extending throughout the depth of the mixed liquor, c. maintaining the length to width ratios of said liquid passes in the order of 0.60 to 1.00, d. flowing said mixed liquor through said plurality of liquid passes in a non-restricted serpentine manner by maintaining open cross-sectional flowpath areas between adjacent liquid passes in the range of 40% to 60% of the wetted cross-sectional area of said basin, e. aerating said mixed liquor as it flows through said liquid passes with a plurality of rotary aerators, f. maintaining intra-zone and inter-zone backflow within and between each of said liquid passes, and g. maintaining the aerator mixing factor of each of said aerators within the range of 20 to 450 to obtain a high degree of effective liquid staging.

Claim 6

The method of reducing the oxygen demand of mixed liquor in an elongated, rectangular aeration basin of an activated sludge purification system comprising: a. flowing said mixed liquor through said aeration basin from an inlet end to an outlet end, b. partitioning said aeration basin into a plurality of liquid passes formed by a plurality of staggered partitions extending from alternate side walls for a distance in the order of one half the width of said basin and extending throughout the depth of the mixed liquor, c. maintaining the length to width ratios of said liquid passes in the order of 0.60 to 1.00, d. flowing said mixed liquor through said plurality of liquid passes in a non-restricted serpentine manner by maintaining open cross-sectional flowpath areas between adjacent liquid passes in the range of 40% to 60% of the wetted cross-sectional area of said basin, e. aerating said mixed liquor as it flows through said liquid passes with a plurality of rotary aerators, f. maintaining intra-zone and inter-zone backflow within and between each of said liquid passes, and g. maintaining the aerator mixing factor of each of said aerators within the range of 20 to 450 to obtain a high degree of effective liquid staging.