US5061406A — In-line gas/liquid dispersion

Claim 1

Independent Claim 410 words

An improved system for the dispersion of a gas in a liquid comprising: (a) a flow line in which said gas and liquid are mixed; (b) flow means for passing one of the fluids to be mixed through said flow line; (c) injection means for injecting the other fluid for the desired mixture of gas and liquid into said flow line to form a gas bubble/liquid mixture; (d) a venturi device positioned in said flow line downstream of the point at which said gas bubble/liquid mixture is formed, said venturi device comprising a converging diameter section, a neck section of smallest diameter, and a diverging diameter section expanding in diameter in the downstream direction; (e) a conical in-line mixer positioned in said flow line downstream of the point at which said gas bubble/liquid mixture is formed, said conical mixer comprising a first cone portion having its enlarged section positioned in the downstream direction and a second cone portion having its enlarged section adjacent that of the first cone portion and its pointed end section positioned downstream thereof in the converging diameter section of the venturi device, the enlarged sections of said cone portions of the mixer being of essentially the same diameter, said second cone portion being positioned such as to form, together with the walls of the converging diameter section of the venturi device, an annular opening for the passage of the gas bubble/liquid mixture to the neck section of the venturi device, said annular passage being adapted to accelerate a high portion of the flow velocity of said mixture to supersonic velocity, with subsequent deacceleration of the flow velocity to subsonic range in the diverging diameter section and/or the neck section of the venturi device, such acceleration-deacceleration action of the venturi device-conical in-line mixer serving to create a sonic shock wave effect resulting in the fine dispersion of the gas bubbles in the liquid, said conical in-line mixer being adjustable so as to enable said conical mixer to be positioned at any desired distance from its closing position in the venturi device so as to adjust the annular opening between the converging diameter section of the venturi and the second cone portion of the conical mixer; and (f) means for adjusting the position of said conical mixer in the flow line, whereby said system can be used to provide enhanced gas bubble/liquid dispersions under a wide range of operating conditions for a wide variety of gas/liquid dispersion operations.

Claim 2

Dependent Claim 410 words

An improved system for the dispersion of a gas in a liquid comprising: (a) a flow line in which said gas and liquid are mixed; (b) flow means for passing one of the fluids to be mixed through said flow line; (c) injection means for injecting the other fluid for the desired mixture of gas and liquid into said flow line to form a gas bubble/liquid mixture; (d) a venturi device positioned in said flow line downstream of the point at which said gas bubble/liquid mixture is formed, said venturi device comprising a converging diameter section, a neck section of smallest diameter, and a diverging diameter section expanding in diameter in the downstream direction; (e) a conical in-line mixer positioned in said flow line downstream of the point at which said gas bubble/liquid mixture is formed, said conical mixer comprising a first cone portion having its enlarged section positioned in the downstream direction and a second cone portion having its enlarged section adjacent that of the first cone portion and its pointed end section positioned downstream thereof in the converging diameter section of the venturi device, the enlarged sections of said cone portions of the mixer being of essentially the same diameter, said second cone portion being positioned such as to form, together with the walls of the converging diameter section of the venturi device, an annular opening for the passage of the gas bubble/liquid mixture to the neck section of the venturi device, said annular passage being adapted to accelerate a high portion of the flow velocity of said mixture to supersonic velocity, with subsequent deacceleration of the flow velocity to subsonic range in the diverging diameter section and/or the neck section of the venturi device, such acceleration-deacceleration action of the venturi device-conical in-line mixer serving to create a sonic shock wave effect resulting in the fine dispersion of the gas bubbles in the liquid, said conical in-line mixer being adjustable so as to enable said conical mixer to be positioned at any desired distance from its closing position in the venturi device so as to adjust the annular opening between the converging diameter section of the venturi and the second cone portion of the conical mixer; and (f) means for adjusting the position of said conical mixer in the flow line, whereby said system can be used to provide enhanced gas bubble/liquid dispersions under a wide range of operating conditions for a wide variety of gas/liquid dispersion operations.

Claim 3

Dependent Claim 85 words

The system of claim 1 in which said injection means comprise means for injecting said other fluid at a sonic velocity in said gas/liquid mixture so as to create an initial sonic shock wave, said initial shock wave and the sonic shock wave produced in the venturi device-conical mixer, resulting in very fine dispersion of the gas bubbles in the liquid, with an extremely high mass transfer surface area being produced as a result of the consecutive sonic shock waves in the gas bubble/liquid mixture.

Claim 4

Dependent Claim 49 words

The system of claim 1 in which said flow means comprise means for passing liquid through the flow line, and said injection means comprise means for injecting gas into the liquid passing through said flow line in the direction of said conical mixer and the venturi device downstream thereof.

Claim 5

Dependent Claim 50 words

The system of claim 1 in which said flow means comprise means for passing liquid through the flow line, and said injection means comprise means for injecting gas into the liquid passing through said low line in the direction of said conical in-line mixer and the venturi device downstream thereof.

Claim 6

Dependent Claim 34 words

The process of claim 4 in which the liquid is passed through the flow line in the direction of the conical in-line mixer and said venturi device, and gas is injected into said liquid.

Claim 7

Dependent Claim 388 words

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 in a flow line, said mixture having a velocity of less than the velocity of sound in said gas bubble/liquid mixture; (b) passing said gas bubble/liquid mixture into contact with a venturi device-conical in-line mixer combination positioned in said flow line, said venturi device comprising a converging diameter section, a neck section of smallest diameter, and a diverging diameter section expanding in diameter in the downstream direction, said conical in-line mixer positioned in the flow line downstream of the point at which said gas bubble/liquid mixture is formed, said conical mixer comprising a first cone portion having an enlarged section positioned in the downstream direction and a second cone portion having its enlarged diameter section adjacent that of the first cone portion and its pointed end section positioned downstream thereof in the converging diameter section of the venturi device, the enlarged section of said cone portions being of essentially the same diameter, said second cone portion being positioned such as to form, together with the walls of the converging diameter section of the venturi device, an annular opening for the passage of the gas bubble/liquid mixture to the neck section of the venturi device, said annular passage being adapted to accelerate a high portion of the flow velocity of said mixture to supersonic velocity, with subsequent deacceleration of the flow velocity to subsonic range in the diverging diameter section and/or the neck section of the venturi device, such acceleration-deacceleration action of the venturi device-conical in-line mixer serving to create a sonic shock wave effect resulting in the fine dispersion of the gas bubbles in the liquid, said conical in-line mixer being adjustable so as to enable said conical mixer to be positioned at any desired distance from its closing position in the venturi device so as to adjust the annular opening between the converging diameter section of the venturi and the second cone portion of the conical mixer; and (c) passing the gas bubble/liquid dispersion through the flow line downstream of the diverging diameter section of the venturi device, whereby an enhanced gas bubble/liquid dispersion can be provided under a wide variety of operating conditions for a wide variety of gas/liquid dispersion operations.

Claim 8

Dependent Claim 388 words

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 in a flow line, said mixture having a velocity of less than the velocity of sound in said gas bubble/liquid mixture; (b) passing said gas bubble/liquid mixture into contact with a venturi device-conical in-line mixer combination positioned in said flow line, said venturi device comprising a converging diameter section, a neck section of smallest diameter, and a diverging diameter section expanding in diameter in the downstream direction, said conical in-line mixer positioned in the flow line downstream of the point at which said gas bubble/liquid mixture is formed, said conical mixer comprising a first cone portion having an enlarged section positioned in the downstream direction and a second cone portion having its enlarged diameter section adjacent that of the first cone portion and its pointed end section positioned downstream thereof in the converging diameter section of the venturi device, the enlarged section of said cone portions being of essentially the same diameter, said second cone portion being positioned such as to form, together with the walls of the converging diameter section of the venturi device, an annular opening for the passage of the gas bubble/liquid mixture to the neck section of the venturi device, said annular passage being adapted to accelerate a high portion of the flow velocity of said mixture to supersonic velocity, with subsequent deacceleration of the flow velocity to subsonic range in the diverging diameter section and/or the neck section of the venturi device, such acceleration-deacceleration action of the venturi device-conical in-line mixer serving to create a sonic shock wave effect resulting in the fine dispersion of the gas bubbles in the liquid, said conical in-line mixer being adjustable so as to enable said conical mixer to be positioned at any desired distance from its closing position in the venturi device so as to adjust the annular opening between the converging diameter section of the venturi and the second cone portion of the conical mixer; and (c) passing the gas bubble/liquid dispersion through the flow line downstream of the diverging diameter section of the venturi device, whereby an enhanced gas bubble/liquid dispersion can be provided under a wide variety of operating conditions for a wide variety of gas/liquid dispersion operations.

Claim 9

Dependent Claim 33 words

The process of claim 6 in which the liquid is passed through the flow line in the direction of the conical mixer and the venturi device, and gas is injected into said liquid.

Claim 10

Dependent Claim 76 words

The process of claim 6 and including injecting one fluid into the other at a sonic velocity so as to create an initial sonic shock wave, said initial shock wave and said sonic shock wave produced in the venturi device-conical mixer resulting in very fine dispersion of the gas bubbles in the liquid, with very high mass transfer surface area being produced as a result of the consecutive sonic shock waves in the gas bubble/liquid mixture.

Claim 11

Dependent Claim 30 words

The process of claim 6 in which said gas/liquid dispersion comprises a process in which the gas is used to strip a gas or a volatile component from a liquid.

Claim 12

Dependent Claim 21 words

The process of claim 6 in which said gas/liquid dispersion comprises a process for the reaction of the gas and liquid.

Claim 13

Dependent Claim 22 words

The process of claim 6 in which said gas/liquid dispersion comprises a process for the dissolving of the gas in the liquid.

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1994-10-28	1995-04-29	1995-10-29	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1998-10-28	1999-04-29	1999-10-29	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	2002-10-28	2003-04-29	2003-10-29	$7700.00	Window Closed / Lapsed

In-line gas/liquid dispersion

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