US2190896A - Revolving cone mixer - Google Patents

Revolving cone mixer Download PDF

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Publication number
US2190896A
US2190896A US186717A US18671738A US2190896A US 2190896 A US2190896 A US 2190896A US 186717 A US186717 A US 186717A US 18671738 A US18671738 A US 18671738A US 2190896 A US2190896 A US 2190896A
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United States
Prior art keywords
cones
cone
cone mixer
shaft
revolving
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Expired - Lifetime
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US186717A
Inventor
Elvin M Underwood
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Patterson Foundry & Machine Co
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Patterson Foundry & Machine Co
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Publication date
Application filed by Patterson Foundry & Machine Co filed Critical Patterson Foundry & Machine Co
Priority to US186717A priority Critical patent/US2190896A/en
Application granted granted Critical
Publication of US2190896A publication Critical patent/US2190896A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/116Stirrers shaped as cylinders, balls or rollers

Definitions

  • My invention relates to an improvement in revolving cone mixers.
  • This invention is of the nature of thevarious forms of cones disclosed in my application, Serial No. 157,191, filed in the U. S. Patent Office, April 3, 1937, and embodies a development of the several forms of mixers disclosed in that application.
  • the primary object of the present invention is to provide complete and uniform mixing of various liquid and semi-liquid solutions by creating a differential in speeds of discharge of the liquid from the cones, with the result that the same material will not repeatedly meet at the discharge ends of the cones, but the discharging flow will constantly meet different materials, all of which is accomplished as has been fully demonstrated by.
  • experimentation in a very simple way by differential proportioning of the cones and this might be accomplished by either a difference in diameters of cooperating cones, or a difference in length of these cones, the result of which is that the flow from one cone is at a greater speed than from the other.
  • Fig. l is a vertical sectional view of a form of the invention.
  • Fig. 2 shows the same disposed horizontally
  • A represents the usual tank; the numeral l, the rotary shaft; and 2 and 3 are the two cones secured to the shaft l.
  • Cones 2 and t are shown opposed to each other, andthe cone 2 is of greater diameter than the diameter of cone 3, thus providing a difference end of the cone, with the result that the liquid issuing from the cone 2 exceeds the speed of the discharge from the cone 3, because of the faster travel of cone 2 at its periphery.
  • the differential in relative speeds at the open. or discharge ends creates a faster discharge and circulation from the cone of greater pitch, and in consequence a return of the material to meet the material discharging from the other cone; at a different point or area in its flow, thereby accomplishing greatly improved mixing results as compared with former practices in which substantially the same material pumped through the cones repeatedly meets at the central discharge.
  • the material will have a diiferent pumping volume and speed of travel in the course of its repeated circuits, so that when the materials leave the cones on'the way to the outer end and return, the material in one cone will revolve faster than in the other, and consequently the same materials will not return to a given place at the same time and come in contact again when the two discharging currents meet.
  • a mixer including atanlr, a rotary shaft,
  • hollow cones secured on the shaft in pairs and discharging toward each other, one cone of greater diameter than the other.
  • a mixer including a tank, a rotary shaft,
  • cones secured on the shaft in pairs and discharging toward each other, one cone of greater length than the other.
  • a mixer includinga tank, a rotary shaft and cones of diiferentfpitchcarried by the shaft,
  • the cones having free interiors and discharging toward each other in opposite directions so that different particles of the contents constantly meet at the outlets of the cones.

Description

Feb 20, 1g4@n M UNDERWQQD ZJQQfiWi REVOLVING com: MIXER Filed Jan. 24, 1958 Patented F ch. 20, 1940 UNITED STATES REVOLVING OONE- MIXER Elvin M. Underwood, East Liverpool, Ohio, as-
signor to The Patterson Foundry & Machine 00., East Liverpool, Ohio Ohio, a corporation of Application January 24, 1938, Serial No. 186,717
3 Claims.
My invention relates to an improvement in revolving cone mixers.
This invention is of the nature of thevarious forms of cones disclosed in my application, Serial No. 157,191, filed in the U. S. Patent Office, April 3, 1937, and embodies a development of the several forms of mixers disclosed in that application.
The primary object of the present invention is to provide complete and uniform mixing of various liquid and semi-liquid solutions by creating a differential in speeds of discharge of the liquid from the cones, with the result that the same material will not repeatedly meet at the discharge ends of the cones, but the discharging flow will constantly meet different materials, all of which is accomplished as has been fully demonstrated by. experimentation in a very simple way by differential proportioning of the cones, and this might be accomplished by either a difference in diameters of cooperating cones, or a difference in length of these cones, the result of which is that the flow from one cone is at a greater speed than from the other.
in pitch and consequently speed at the discharge In the accompanying drawing:
Fig. l is a vertical sectional view of a form of the invention;
Fig. 2 shows the same disposed horizontally;
Fig. 3 is a modification; and i Fig. l is a plan view of the form illustrated in Fi 1. I
Referring to Fig. l, A represents the usual tank; the numeral l, the rotary shaft; and 2 and 3 are the two cones secured to the shaft l.
Cones 2 and t are shown opposed to each other, andthe cone 2 is of greater diameter than the diameter of cone 3, thus providing a difference end of the cone, with the result that the liquid issuing from the cone 2 exceeds the speed of the discharge from the cone 3, because of the faster travel of cone 2 at its periphery.
While this is illustrated in vertical form, the foregoing elements might be arranged horizontally or in any other position for that matter within the tank A.
Also, it is obvious that the relative difference in'diameters of the discharge ends of the cones On the form shown in Fig. 3, the differencein pitch between the cones is taken care of by making one cone, namely cone 5 in this instance, of greater length then. cone 5. Both are secured to the shaft 4.
Itwill be understood that the position of the cones 2 and 3, and 5 and 6, might be reversed by inverting the shafts i and t, or in some other way.
While I have shown one pair of cones only in the drawing, these might be arranged in series on the same shaft.
By reason of .the foregoing arrangement, the differential in relative speeds at the open. or discharge ends creates a faster discharge and circulation from the cone of greater pitch, and in consequence a return of the material to meet the material discharging from the other cone; at a different point or area in its flow, thereby accomplishing greatly improved mixing results as compared with former practices in which substantially the same material pumped through the cones repeatedly meets at the central discharge. In other words, if there is a difference in pitch between the two cones, the material will have a diiferent pumping volume and speed of travel in the course of its repeated circuits, so that when the materials leave the cones on'the way to the outer end and return, the material in one cone will revolve faster than in the other, and consequently the same materials will not return to a given place at the same time and come in contact again when the two discharging currents meet.
I claim:
1. A mixer including atanlr, a rotary shaft,
hollow cones secured on the shaft in pairs and discharging toward each other, one cone of greater diameter than the other.
2. A mixer including a tank, a rotary shaft,
. cones secured on the shaft in pairs and discharging toward each other, one cone of greater length than the other.
3. A mixer includinga tank, a rotary shaft and cones of diiferentfpitchcarried by the shaft,
the cones having free interiors and discharging toward each other in opposite directions so that different particles of the contents constantly meet at the outlets of the cones.
ELVIN M. UNDERWOOD.
US186717A 1938-01-24 1938-01-24 Revolving cone mixer Expired - Lifetime US2190896A (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3043570A (en) * 1957-08-15 1962-07-10 Du Pont Apparatus for mixing flowable materials
US3069144A (en) * 1959-02-06 1962-12-18 Sweden Freezer Mfg Co Agitator means for drink mixers
US4490049A (en) * 1983-06-02 1984-12-25 Cron Chemical Corporation Mixing arrangement
US5241992A (en) * 1992-07-14 1993-09-07 Eastman Kodak Company Apparatus and method for distributing fluids
WO1993017782A1 (en) * 1992-03-04 1993-09-16 Kamyr, Inc. Varying annular fluidization zone for increased mixing efficiency in a medium consistency mixer
US5261745A (en) * 1992-04-13 1993-11-16 Watkins James R Mixing apparatus with frusto-conically shaped impeller for mixing a liquid and a particulate solid
US5575559A (en) * 1994-09-19 1996-11-19 Goulds Pumps, Inc. Mixer for mixing multi-phase fluids
US6523995B2 (en) * 2001-03-23 2003-02-25 Chemineer, Inc. In-tank mixing system and associated radial impeller
US6543927B2 (en) * 1995-12-05 2003-04-08 David Marshall King Method of mixing viscous fluids
US6688764B2 (en) 1995-12-05 2004-02-10 Site-B Company Method of mixing using mixing device having vanes with sloping edges
US6971788B1 (en) 2000-08-11 2005-12-06 Site-B Company Fluid mixing device
US20120138276A1 (en) * 2009-07-30 2012-06-07 Aisin Seiki Kabushiki Kaisha Device for diluting viscous substance

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3043570A (en) * 1957-08-15 1962-07-10 Du Pont Apparatus for mixing flowable materials
US3069144A (en) * 1959-02-06 1962-12-18 Sweden Freezer Mfg Co Agitator means for drink mixers
US4490049A (en) * 1983-06-02 1984-12-25 Cron Chemical Corporation Mixing arrangement
WO1993017782A1 (en) * 1992-03-04 1993-09-16 Kamyr, Inc. Varying annular fluidization zone for increased mixing efficiency in a medium consistency mixer
US5263774A (en) * 1992-03-04 1993-11-23 Kamyr, Inc. Rotor for increasing mixing efficiency in a medium consistency mixer
US5378321A (en) * 1992-03-04 1995-01-03 Kamyr, Inc. Varying annular fluidization zone for increased mixing efficiency in a medium consistency mixer
US5261745A (en) * 1992-04-13 1993-11-16 Watkins James R Mixing apparatus with frusto-conically shaped impeller for mixing a liquid and a particulate solid
US5241992A (en) * 1992-07-14 1993-09-07 Eastman Kodak Company Apparatus and method for distributing fluids
US5575559A (en) * 1994-09-19 1996-11-19 Goulds Pumps, Inc. Mixer for mixing multi-phase fluids
US6688764B2 (en) 1995-12-05 2004-02-10 Site-B Company Method of mixing using mixing device having vanes with sloping edges
US7334936B2 (en) * 1995-12-05 2008-02-26 Site-B Company Mixing device and method of mixing
US20030112700A1 (en) * 1995-12-05 2003-06-19 King David Marshall Method of mixing viscous fluids
US20090268545A1 (en) * 1995-12-05 2009-10-29 King Ronnald B Mixing device and method of mixing
US20040160854A1 (en) * 1995-12-05 2004-08-19 King Ronnald B. Method of mixing using mixing device having vanes with sloping edges
US6848823B2 (en) * 1995-12-05 2005-02-01 Site-B Company Method of mixing viscous fluids
US20050195683A1 (en) * 1995-12-05 2005-09-08 King David M. Method of mixing viscous fluids
US7553065B2 (en) 1995-12-05 2009-06-30 Site-B Company Mixing device
US7070317B2 (en) * 1995-12-05 2006-07-04 Site-B Company Method of mixing using vaned mixing device
US6543927B2 (en) * 1995-12-05 2003-04-08 David Marshall King Method of mixing viscous fluids
US7226205B2 (en) 2000-08-11 2007-06-05 Site-B Company Fluid mixing device
US6971788B1 (en) 2000-08-11 2005-12-06 Site-B Company Fluid mixing device
US6523995B2 (en) * 2001-03-23 2003-02-25 Chemineer, Inc. In-tank mixing system and associated radial impeller
US20120138276A1 (en) * 2009-07-30 2012-06-07 Aisin Seiki Kabushiki Kaisha Device for diluting viscous substance
US8506156B2 (en) * 2009-07-30 2013-08-13 Aisin Seiki Kabushiki Kaisha Device for diluting viscous substance

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