Method and apparatus for continuous mixing of small, precise quantities of bulk materials with a liquid stream

• US 4,801,210 A
• Filed: 03/14/1988
• Issued: 01/31/1989
• Est. Priority Date: 03/14/1988
• Status: Expired due to Term

• Current Assignee: Michael Gian
• Original Assignee: Michael Gian
• Inventors: Gian, Michael
• Primary Examiner(s): Jenkins, Robert W.
• Application Number:
  US07/167,369
• Time in Patent Office: 323 Days
• Field of Search: 366/3, 366/5, 366/10, 366/11, 366/101, 366/102, 366/103, 366/150, 366/154, 366/156, 366/157, 366/107, 366/349, 406/46, 406/47, 406/61, 222/630
• US Class Current: 366/156.2
• CPC Class Codes: B01F 33/80 Mixing plants; Combinations of mixers
• CPC Class Codes: B01F 35/71 Feed mechanisms with proportioning B01F35/80
• CPC Class Codes: B01F 35/712 for feeding fluids
• CPC Class Codes: B01F 35/714 for feeding predetermined amounts B01F35/88 takes precedence
• CPC Class Codes: B01F 35/7173 using gravity, e.g. from a hopper
• CPC Class Codes: B01F 35/7176 using pumps
• CPC Class Codes: B01F 35/71805 using valves, gates, orifices or openings

Abstract

A continuous mixer is provided for combining bulk materials metered at a relatively slow rate into a liquid stream and is particularly useful for preparing an innoculant solution for treating feed pellets, seed or the like. The mixer has a vertical separation tube extending between a screw feeder and a mixing zone in a liquid conduit therebelow, and the tube is independently pressurized with air to substantially preclude ascent of liquids within the tube to ensure that all of the mixing occurs within the liquid line and to prevent the liquid from rising to a level sufficient for wetting the innoculants stored within a hopper adjacent the screw feeder. Air pressure within the tube is selectively adjustable in order to vary the spray produced by a nozzle at the end of the fluid conduit from a liquid stream essentially free of air to a finely dispersed fog which includes substantial quantities of air.

Claims

1. Apparatus for mixing precise quantities of bulk materials with a stream of liquid comprising:

means defining a hopper presenting an enclosed chamber for receiving bulk materials,

said enclosed chamber having a lower outlet and being pressurizable to a value above atmospheric pressure;

means for pressurizing said chamber to a first, certain pressure;

an elongated, axially rotatable screw feeder extending through said outlet of said chamber for carrying away metered portions of said bulk materials from said chamber,

said screw feeder presenting a discharge end portion remote from said outlet of said chamber;

a vessel for receiving and storing liquid;

conduit means coupled to said vessel and having an outlet opening remote from the latter;

means for pumping liquid from said vessel and along the length of said conduit means under pressure for discharge through said outlet opening,

said conduit means including structure defining a mixing zone having an upwardly facing inlet opening;

an upright separation tube having an upper section for receiving bulk materials discharged from said end portion of said screw feeder,

said tube including a lower section directly connected to said structure defining said mixing zone of said conduit means in surrounding relationship to said inlet opening; and

air conveying means for accelerating bulk materials along substantially the length of said upright separation tube in cooperation with the effects of gravity and for directing said bulk materials through said inlet opening and into said mixing zone,

said conveying means including means for pressurizing the tube at a pressure equal to or less than the pressure of said chamber and at a pressure which is greater than the pressure of said liquid passing through said mixing zone of said conduit means in order to substantially preclude ascent of said liquid through said inlet opening adjacent said mixing zone and into said upright tube,

said means for pressurizing said tube including structure defining an air inlet disposed adjacent said discharge end portion of said screw in order to facilitate acceleration and descent of bulk materials along said separation tube.

2. The invention as set forth in claim 1, wherein said lower section of said tube presents a transverse, free cross-sectional internal area substantially equal to the internal, free cross-sectional area of said conduit means in said mixing zone.

3. The invention as set forth in claim 1, wherein said means for pressurizing said tube includes an air inlet disposed above said discharge end portion of said screw feeder for facilitating disengagement of bulk materials from the latter.

4. The invention as set forth in claim 1, wherein said screw feeder extends in a generally horizontal direction, and wherein said means for pressurizing said tube includes an air inlet disposed directly above said discharge end portion of said screw feeder.

5. The invention as set forth in claim 1;

and including a second, elongated, axially rotatable screw feeder having a discharge end portion extending into said tube for metering additional quantities of said bulk materials into said tube.

6. The invention as set forth in claim 1, wherein said screw feeder includes a variable feed motor.

7. The invention as set forth in claim 1;

and including means for inducing a vortex in said liquid stream passing through said fluid conduit at at least one location downstream of said mixing zone.

8. A method of mixing precise quantities of bulk materials with a liquid stream comprising the steps of:

loading a quantity of bulk materials into an enclosed, pressurized chamber;

metering a portion of said bulk materials out of said chamber with an elongated, axially rotatable screw feeder;

discharging the metered bulk materials from said screw feeder into an upper section of an upright tube;

p1 pumping under pressure a volume of liquid through an elongated fluid conduit presenting a mixing zone with an upwardly facing inlet opening connected to a bottom section of said upright tube; and

admitting pressurized air into said upper section of said upright tube adjacent a discharge end portion of said screw feeder to pressurize said tube to a value equal to or smaller than the pressure within said chamber and greater than the pressure within said fluid conduit of said mixing zone in order to facilitate advancement of said bulk materials along said screw feeder and descent of said materials along said tube while substantially precluding ascent of liquid within the latter.

9. The method as set forth in claim 8, wherein said step of admitting air to said upright tube includes the step of directing pressurized air in a direction generally toward said discharge end portion of said screw feeder.

10. The method as set forth in claim 8;

and including the step of introducing bulk materials into said upright tube with another screw feeder presenting a discharge end portion disposed generally beneath the location where said air is admitted into said tube.