Gas dispersion process and system

Claim 2

An improved process for the dispersion of a gas in a liquid comprising: (a) combining said gas and liquid to form a gas bubble-liquid mixture under non-turbulent flow conditions such that a uniform dispersion of gas bubbles and liquid is not formed, said mixture having a flow velocity of less than the velocity of sound in said gas bubble-liquid mixture; (b) passing said nonuniformly dispersed gas bubble-liquid mixture under non-turbulent flow conditions into contact with flow constriction means positioned downstream of, but in close proximity to, the point at which said gas and liquid are mixed; (c) accelerating the flow velocity of said gas bubble-liquid mixture to a supersonic velocity, by passage through said flow constriction means; (d) subsequently deaccelerating said flow velocity from supersonic velocity to sub-sonic range, the acceleration-deacceleration of the pre-formed gas bubble-liquid mixture upon passage through said flow constriction means serving to create a sonic shock wave resulting in an extremely fine dispersion of gas bubbles in the liquid, the close proximity of the flow constriction means to the point of initial formation of the gas bubble-liquid mixture under non-turbulent conditions precluding the uniform dispersion of gas and liquid prior to the acceleration of the gas bubble-liquid mixture to a supersonic velocity and subsequent deacceleration thereof, whereby the mass transfer characteristics of the gas bubble-liquid dispersion, and the mass transfer-power consumption balance, are enhanced by this subjecting of the gas-liquid mixture, initially in nonuniformly dispersed form, to the sonic shock wave effect of said flow constriction means.

Claim 3

The process of claim 1 in which said flow constriction means comprises an orifice plate.

Claim 4

The process of claim 1 in which said flow constriction means comprises a reduced diameter section of a flow conduit through which said gas and liquid are being passed.

Claim 5

The process of claim 1 in which said flow constriction means comprises a venturi.

Claim 6

The process of claim 1 in which said gas is oxygen, and said liquid is water.

Claim 7

The process of claim 1 in which said gas-liquid dispersion comprises a process for the reaction of the gas and liquid.

Claim 8

The process of claim 1 in which said gas-liquid dispersion comprises a process in which the gas is used to strip dissolved gas from the liquid.

Claim 9

The process of claim 1 in which said flow constriction means is positioned in the flow conduit through which one of the fluids to be mixed is passed, the other fluid being added thereto upstream of said flow constriction means at a distance therefrom not exceeding about one diameter in length, based on the diameter of said flow conduit through which said fluid is passed upstream of said flow constriction means.

Claim 10

The process of claim 5 in which said liquid is passed through the flow conduit and said gas is injected therein to form a gas bubble-liquid mixture.

Claim 11

The process of claim 9 in which said gas is injected into a stream of liquid at an injection point positioned within the converging section of the venturi.

Claim 12

The process of claim 10 in which said gas injection point is positioned at about one half of the distance from the throat of the venturi to the upstream end of the converging section thereof.

Claim 13

The process of claim 10 in which said gas injection point is close to the throat of the venturi.

Claim 14

The process of claim 10 in which said gas injection point is positioned in the flow conduit upstream of the converging section of the venturi.

Claim 15

An improved system for the dispersion of a gas in a liquid comprising: (a) a flow conduit in which said gas and liquid are to be combined; (b) flow means for passing one of the fluids to be combined through said flow conduit under non-turbulent conditions; (c) injection means for injecting the other fluid for the desired combination of gas and liquid into said flow conduit to form a gas bubble-liquid mixture under said non-turbulent conditions such that a uniform dispersion of gas bubbles and liquid is not formed; and (d) flow constriction means positioned in said flow conduit downstream of said injection means but in close proximity thereto, said flow constriction means being adapted to accelerate the flow velocity of said nonuniformly dispersed gas bubble-liquid mixture from said non-turbulent flow conditions to a supersonic velocity, with subsequent deacceleration of the flow velocity to sub-sonic range, such acceleration-deacceleration action of the flow constriction means serving to create a sonic shock wave effect resulting in an extremely fine dispersion of the gas bubbles in the liquid, the close proximity of the flow constriction means in the flow conduit to the position of said injection means precluding the uniform dispersion of gas bubbles and liquid prior to the acceleration of the gas bubble-liquid mixture to a supersonic velocity, and subsequent deacceleration to sub-sonic velocity, whereby the mass-transfer characteristics of the gas bubble-liquid dispersion, and the mass transfer-power consumption balance, can be enhanced by thus subjecting the gas bubble-liquid mixture, initially in nonuniformly dispersed form, to the sonic shock wave effect of said flow constriction means.

Claim 16

An improved system for the dispersion of a gas in a liquid comprising: (a) a flow conduit in which said gas and liquid are to be combined; (b) flow means for passing one of the fluids to be combined through said flow conduit under non-turbulent conditions; (c) injection means for injecting the other fluid for the desired combination of gas and liquid into said flow conduit to form a gas bubble-liquid mixture under said non-turbulent conditions such that a uniform dispersion of gas bubbles and liquid is not formed; and (d) flow constriction means positioned in said flow conduit downstream of said injection means but in close proximity thereto, said flow constriction means being adapted to accelerate the flow velocity of said nonuniformly dispersed gas bubble-liquid mixture from said non-turbulent flow conditions to a supersonic velocity, with subsequent deacceleration of the flow velocity to sub-sonic range, such acceleration-deacceleration action of the flow constriction means serving to create a sonic shock wave effect resulting in an extremely fine dispersion of the gas bubbles in the liquid, the close proximity of the flow constriction means in the flow conduit to the position of said injection means precluding the uniform dispersion of gas bubbles and liquid prior to the acceleration of the gas bubble-liquid mixture to a supersonic velocity, and subsequent deacceleration to sub-sonic velocity, whereby the mass-transfer characteristics of the gas bubble-liquid dispersion, and the mass transfer-power consumption balance, can be enhanced by thus subjecting the gas bubble-liquid mixture, initially in nonuniformly dispersed form, to the sonic shock wave effect of said flow constriction means.

Claim 17

The system of claim 14 in which said flow constriction means comprises an orifice plate.

Claim 18

The system of claim 14 in which said flow constriction means comprises a reduced diameter section of said flow conduit.

Claim 19

The system of claim 14 in which said flow constriction means comprises a venturi.

Claim 20

The system of claim 14 in which said injection means is positioned upstream of said flow constriction means at a distance therefrom not exceeding about one diameter in length, based on the diameter of said flow conduit through which said fluid is passed upstream of said flow constriction means.

Claim 21

The system of claim 18 in which said flow means comprises means for passing liquid through said flow conduit, and said injection means comprises means for injecting gas into the liquid passing through said flow conduit.

Claim 22

The system of claim 19 in which said gas injection means is positioned within the converging section of the venturi.