Super-oxygenation method

Claim 1

A method for continuously super-oxygenating a portion of the bio-oxidizable fluid from a bio-oxidation reactor to increase the concentration of oxygen dissolved in such fluid and reduce the energy required to effect the dissolution of such oxygen in such fluid comprising the steps of: a. continuously transferring a stream of said fluid in said reactor from a point near the top of the column of said fluid to a point near the bottom of an oxidator vessel equipped with a high shear agitator, said vessel having a capacity of from about one-tenth to one-two hundreth of the capacity of said reactor and having a diameter to height ratio of from about 1:2 to about 1:10 and said agitator having a diameter of from about 1:3 to 2:3 of the diameter of said vessel and impellers thereon having an effective surface area about the same as the cross-sectional area of said vessel, said reactor and said vessel being connected in a closed system; b. filling said vessel with a column of said fluid from said reactor to a point near the top of said vessel where there is disposed a return conduit from said vessel to a point near the bottom of said vessel to a point near the bottom of said reactor; c. introducing an oxygen containing gas into said fluid in said vessel at a point near the bottom of said vessel, at a pressure of from about 1.0 to about 40 psig; d. revolving said agitator in said fluid in said vessel while said gas is being introduced thereinto; e. operating said agitator at from about 150 to about 1,800 rpm wherein the energy utilization is from about 5 to about 15 horsepower per 1,000 gallons of said fluid in said vessel; f. shearing said oxygen containing gas into submillimeter bubbles of the order of from about 10.sup. -1 to about 10.sup. -4 centimeters in said fluid; and g. continuously transferring a stream of the bio-oxidizable fluid containing the sub-millimeter bubbles of oxygen containing gas from said vessel to a point near the bottom of said reactor, said stream being taken from a point near the top of said column of said fluid in said vessel, said transferring being conducted at a rate such that the volume of said fluid in said vessel is renewed every 30 to 240 seconds.

Claim 2

A method for continuously super-oxygenating a portion of the bio-oxidizable fluid from a bio-oxidation reactor to increase the concentration of oxygen dissolved in such fluid and reduce the energy required to effect the dissolution of such oxygen in such fluid comprising the steps of: a. continuously transferring a stream of said fluid in said reactor from a point near the top of the column of said fluid to a point near the bottom of an oxidator vessel equipped with a high shear agitator, said vessel having a capacity of from about one-tenth to one-two hundreth of the capacity of said reactor and having a diameter to height ratio of from about 1:2 to about 1:10 and said agitator having a diameter of from about 1:3 to 2:3 of the diameter of said vessel and impellers thereon having an effective surface area about the same as the cross-sectional area of said vessel, said reactor and said vessel being connected in a closed system; b. filling said vessel with a column of said fluid from said reactor to a point near the top of said vessel where there is disposed a return conduit from said vessel to a point near the bottom of said vessel to a point near the bottom of said reactor; c. introducing an oxygen containing gas into said fluid in said vessel at a point near the bottom of said vessel, at a pressure of from about 1.0 to about 40 psig; d. revolving said agitator in said fluid in said vessel while said gas is being introduced thereinto; e. operating said agitator at from about 150 to about 1,800 rpm wherein the energy utilization is from about 5 to about 15 horsepower per 1,000 gallons of said fluid in said vessel; f. shearing said oxygen containing gas into submillimeter bubbles of the order of from about 10.sup. -1 to about 10.sup. -4 centimeters in said fluid; and g. continuously transferring a stream of the bio-oxidizable fluid containing the sub-millimeter bubbles of oxygen containing gas from said vessel to a point near the bottom of said reactor, said stream being taken from a point near the top of said column of said fluid in said vessel, said transferring being conducted at a rate such that the volume of said fluid in said vessel is renewed every 30 to 240 seconds.