US2007017581A1PendingUtilityA1
Apparatus For Mixing Two Fluids Or Keeping Them Separate
Est. expiryJun 21, 2022(expired)· nominal 20-yr term from priority
Y10T137/87676B01F 23/451Y10T137/8766Y10T137/87652B01F 2101/305B01F 25/105B01F 35/71805B01F 35/833B01F 35/7547B01F 35/712B01F 35/714
47
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Claims
Abstract
A mixing apparatus for mixing two fluids immediately following contact with each other is disclosed. The mixing apparatus includes a spring-loaded ball valve separating a first fluid from a second fluid. The ball valve closes as a result of at least spring force. The ball valve opens as a result of hydraulic pressure of one of the fluids operating against the spring force. Mixing is accomplished instantaneously by dispersing one fluid in a thin pattern around the open ball valve into a stream of the other fluid.
Claims
exact text as granted — not AI-modified1 .- 9 . (canceled)
10 . A method of forming a mixture of an aqueous fluid and a reactive polymer composition comprising:
passing an aqueous fluid into a mixing assembly through a first inlet port in a first direction; passing a reactive polymer composition into the mixing assembly through a second inlet port in a second direction, the second direction being orthogonal to the first direction, with a force sufficient to open a pressure-actuated valve located at an intersection of the first inlet port and the second inlet port; forming a mixture of the aqueous fluid and the reactive polymer composition at the intersection without forming a coagulation on the pressure-actuated valve; and passing the mixture out of the mixing assembly through an outlet port axially aligned with the first inlet port.
11 . The method of claim 10 , wherein the first direction is substantially horizontal and the second direction is substantially vertical.
12 . The method of claim 10 , wherein the reactive polymer composition flows at a rate in the range of from about a fraction of a gallon per hour to about several hundred gallons per hour.
13 . The method of claim 10 , wherein the aqueous fluid flows at a rate in the range of from about a fraction of a gallon per minute to about several hundred gallons per minute.
14 . The method of claim 10 , wherein a pressure of about 30 pounds per square inch is applied to the pressure-actuated valve.
15 . The method of claim 11 , wherein the reactive polymer composition flows at a rate in the range of from about a fraction of a gallon per hour to about several hundred gallons per hour.
16 . The method of claim 11 , wherein the aqueous fluid flows at a rate in the range of from about a fraction of a gallon per minute to about several hundred gallons per minute.
17 . The method of claim 11 , wherein a pressure of about 30 pounds per square inch is applied to the pressure-actuated valve.
18 . The method of claim 10 , wherein the reactive polymer composition flows at a rate in the range of from about a fraction of a gallon per hour to about several hundred gallons per hour, the aqueous fluid flows at a rate in the range of from about a fraction of a gallon per minute to about several hundred gallons per minute and a pressure of about 30 pounds per square inch is applied to the pressure-actuated valve.
19 . The method of claim 18 , wherein the first direction is substantially horizontal and the second direction is substantially vertical.Cited by (0)
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