US2559518A - Recirculating tank mixing system - Google Patents
Recirculating tank mixing system Download PDFInfo
- Publication number
- US2559518A US2559518A US17145A US1714548A US2559518A US 2559518 A US2559518 A US 2559518A US 17145 A US17145 A US 17145A US 1714548 A US1714548 A US 1714548A US 2559518 A US2559518 A US 2559518A
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- US
- United States
- Prior art keywords
- impeller
- container
- materials
- agitator
- mixing system
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/52—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle with a rotary stirrer in the recirculation tube
Definitions
- the present invention relates to a tank mixing system and particularly to a method and apparatus for preparing mixtures such as are employed in grease making, acid and caustic treating operations, in dissolving solids in liquid materials or making slurries thereof, and operations of a similar nature. It is an object of the invention to provide a method and means for improving the efliciency of mixing by mechanical agitation, and to reduce the mixing time required under any given circumstance.
- Figure 2 is a cross sectional view along the line IIII of Figure l.
- FIG. 3 is an alternate form of apparatus according to the invention.
- the numeral I indicates a tank or other. container for a batch of two or more materials to be mixed, either or both of which may be a liquid.
- the method and apparatus may also be utilized for the production of solutions of solid materials in a liquid or for producing slurries of solid materials in liquids.
- the tank or container is provided with means for agitating a body of materials to be mixed therein.
- a hollow, agitator-impeller member 2 supported within the container as by means of a hollow shaft 3.
- Suitable bearing means such as shown at 4 may be provided to support the shaft and facilitate rotation as by a motor 5 attached to the shaft at its upper end, or by other means.
- the hollow impeller member 2 illustrated in Figures 1 and 2 of the drawings is provided with a plurality of Jet passageways 6 opening outwardly therefrom through the trailing ApplicationMai-ch 26,4948, Serial No. 17,145
- a zone of low turbulence usually occurs in the area immediately above the impeller member, substantially within the rotation radius thereof.
- This zone of low turbulence may have the form of a substantially cylindrical core immediately above the impeller.
- This core or low turbulence zone is indicated by the numeral I, and by light parallel vertical lines in Figure l and light circular lines in Figure 2.
- one or more conduits 8 are extended into the container l opening at the inner and within the area immediately above the impeller 2, and within the rotation radius of the impeller blades.
- the conduits 8 communicate, as through a header or manifold 9, with the suction line In of pump Ii.
- the discharge line 12 is suitably connected to the hollow shaft 3, as by a collar i3, and the returned material is discharged through the trailing edge portions of the impeller 2 by way of passageways 6.
- the pump l0 continuously withdraws a portion of the materials being mixed from the low turbulence zone I through conduits or lines 8, 9, and I0, and returns it to, the container through line l2, hollow shaft 3, and is discharged into the high turbulence zone in the immediate vicinity of the impeller 2, by way of jet passageways 6. If suflicient pressure is provided by the pump H, the jetted discharge from the passageways 6 may be utilized to drive the agitator-impeller 2, or to supplement the action of driving means such as the motor 5.
- the line I2 is connected to an annular conduit member ll disposed peripherally within the container at a level intermediate that of the impeller and the container bottom, within the high turbulence zone adjacent the impeller.
- the material may be discharged into this area from line I4 by passageways or jets I 5 opening through the walls of the line or conduit H.
- the agitator-impeller and shaft need not be hollow, and a simple paddle wheel l6 and solid shaft may be utilized.
- a mixing apparatus comprising a container for a fluid body of materials to-be mixed, said container having a bottom wall, rotatable agitator-impeller means disposed in said container closely spaced in vertical relation to the bottom wall thereof, rotatable shaft means extended into said container and connected to said agitatorimpeller for rotation thereof, a plurality of conduit elements, for withdrawal therefrom of portions of a.
- fluid body of materials in said container e'xtended into said container, eachhaving an inner end terminating and opening in radially and vertically spaced relation to one another and to said shaft means and agitator-impeller respectively, and within the radius of rotation of said agitator-impeller, and an outer end exteriorly of said container, pump means connected to the outer ends of-said conduit elements for withdrawing portions of the body of materials contained therein, and means for returning the material portions withdrawn to the container adjacent said agitator-impeller.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Description
July 3, 1951 c. w. SMITH RECIRCULATING TANK MIXING SYSTEM Filed March 26, 1948 Patented July 3,1951
2,559,518 RECIRCULATING TANK MIXING SYSTEM Charles W. Smith Plainfield, N. 1., assignor to Standard Oil Development Company, a corporation of Delaware 3 Claims.
The present invention relates to a tank mixing system and particularly to a method and apparatus for preparing mixtures such as are employed in grease making, acid and caustic treating operations, in dissolving solids in liquid materials or making slurries thereof, and operations of a similar nature. It is an object of the invention to provide a method and means for improving the efliciency of mixing by mechanical agitation, and to reduce the mixing time required under any given circumstance. I
It has been found that in operations involving the mixing of two or more materials, particularly in such operations where a body of such materials is mechanically agitated by paddles or propeller mechanisms in a tank or similar container that there is formed a central core of material above the agitator blades in which the materials are mixed at a much slower rate than in the zone or area in the immediate vicinity of the agitator blades. To overcome such a condition, it is now proposed that provision be made for withdrawing materials from the low turbulence central core above the agitator blades for recirculation and discharge into the high turbulence zone in the immediate vicinity of the agitator blades.
The invention and its objects may be more readily understood from the following description when read in conjunction with the accompanying drawing in which Figure 1 is a diagrammatic showing of the apparatus in vertical section,
Figure 2 is a cross sectional view along the line IIII of Figure l, and
Figure 3 is an alternate form of apparatus according to the invention.
In the drawings, the numeral I indicates a tank or other. container for a batch of two or more materials to be mixed, either or both of which may be a liquid. As indicated, the method and apparatus may also be utilized for the production of solutions of solid materials in a liquid or for producing slurries of solid materials in liquids. As shown, the tank or container is provided with means for agitating a body of materials to be mixed therein. Preferably such means is a hollow, agitator-impeller member 2, supported within the container as by means of a hollow shaft 3. Suitable bearing means such as shown at 4 may be provided to support the shaft and facilitate rotation as by a motor 5 attached to the shaft at its upper end, or by other means. The hollow impeller member 2 illustrated in Figures 1 and 2 of the drawings, is provided with a plurality of Jet passageways 6 opening outwardly therefrom through the trailing ApplicationMai-ch 26,4948, Serial No. 17,145
edge portions of the impeller, and is in direct communication interiorly with the hollow shaft 3 In a conventional system, in which the mixing operation is accomplished by use of a generally comparable impeller mechanism, a zone of low turbulence usually occurs in the area immediately above the impeller member, substantially within the rotation radius thereof. This zone of low turbulence may have the form of a substantially cylindrical core immediately above the impeller. This core or low turbulence zone is indicated by the numeral I, and by light parallel vertical lines in Figure l and light circular lines in Figure 2. To overcome the stagnation effect of such a central zone or core, one or more conduits 8 are extended into the container l opening at the inner and within the area immediately above the impeller 2, and within the rotation radius of the impeller blades. The conduits 8 communicate, as through a header or manifold 9, with the suction line In of pump Ii. Material which is withdrawn from the low turbulence zone I in the container l, by way of lines 8, 9, and I0, is returned by pump ll through discharge line l2 to the high turbulence zone in the vicinity of the impeller 2. As illustrated in Figures 1 and 2, the discharge line 12 is suitably connected to the hollow shaft 3, as by a collar i3, and the returned material is discharged through the trailing edge portions of the impeller 2 by way of passageways 6.
In operation, the pump l0 continuously withdraws a portion of the materials being mixed from the low turbulence zone I through conduits or lines 8, 9, and I0, and returns it to, the container through line l2, hollow shaft 3, and is discharged into the high turbulence zone in the immediate vicinity of the impeller 2, by way of jet passageways 6. If suflicient pressure is provided by the pump H, the jetted discharge from the passageways 6 may be utilized to drive the agitator-impeller 2, or to supplement the action of driving means such as the motor 5.
In the apparatus as shown in Figure 3, the line I2 is connected to an annular conduit member ll disposed peripherally within the container at a level intermediate that of the impeller and the container bottom, within the high turbulence zone adjacent the impeller. The material may be discharged into this area from line I4 by passageways or jets I 5 opening through the walls of the line or conduit H. In this form of the apparatus, as illustrated, the agitator-impeller and shaft need not be hollow, and a simple paddle wheel l6 and solid shaft may be utilized.
Although the invention has been set forth with reference to specific embodiments thereof, for the purpose of illustration, it is not intended to be limited thereby, but only by the appended claims.
What is claimed is:
1. A mixing apparatus comprising a container for a fluid body of materials to-be mixed, said container having a bottom wall, rotatable agitator-impeller means disposed in said container closely spaced in vertical relation to the bottom wall thereof, rotatable shaft means extended into said container and connected to said agitatorimpeller for rotation thereof, a plurality of conduit elements, for withdrawal therefrom of portions of a. fluid body of materials in said container e'xtended into said container, eachhaving an inner end terminating and opening in radially and vertically spaced relation to one another and to said shaft means and agitator-impeller respectively, and within the radius of rotation of said agitator-impeller, and an outer end exteriorly of said container, pump means connected to the outer ends of-said conduit elements for withdrawing portions of the body of materials contained therein, and means for returning the material portions withdrawn to the container adjacent said agitator-impeller.
'2. A mixing apparatus according to claim 1, in which said agitator-impeller means is a hollow REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 909,058 Carmichael Jan. 5, 1909 1,192,478 Vandercook July 25, 1916 1,438,733 Werner Dec. 12, 1922 1,706,418 Sissom Mar. 26, 1929 2,135,261 Rosmait Nov. 1, 1938 2,432,175 Schmidt Dec. 9, 1942
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US17145A US2559518A (en) | 1948-03-26 | 1948-03-26 | Recirculating tank mixing system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US17145A US2559518A (en) | 1948-03-26 | 1948-03-26 | Recirculating tank mixing system |
Publications (1)
Publication Number | Publication Date |
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US2559518A true US2559518A (en) | 1951-07-03 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US17145A Expired - Lifetime US2559518A (en) | 1948-03-26 | 1948-03-26 | Recirculating tank mixing system |
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US (1) | US2559518A (en) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2793005A (en) * | 1953-12-04 | 1957-05-21 | Robert J Wagner | Automatic temperature and water regulation for photographic developing |
DE1075559B (en) * | 1960-02-18 | Pintsch Bamag Aktiengesellschaft, Berlin | Blade stirrer with hollow shaft for dividing gases into liquids | |
US2958516A (en) * | 1957-03-15 | 1960-11-01 | Gen Motors Corp | Apparatus for making synthetic resins |
US2963415A (en) * | 1956-08-28 | 1960-12-06 | Standard Oil Co | Asphalt blending |
US2972546A (en) * | 1957-03-08 | 1961-02-21 | Eastman Kodak Co | Method and apparatus for manufacturing colored sheeting |
US3215624A (en) * | 1961-06-30 | 1965-11-02 | Fuller Co | Continuous ion exchange apparatus and process |
US3326815A (en) * | 1963-10-02 | 1967-06-20 | Knapsack Ag | Process for the manufacture of aqueous clay suspensions |
US4100610A (en) * | 1975-12-23 | 1978-07-11 | John Blue Company Division Of Subscription Television, Inc. | Rotating nozzle sparging system for suspension fertilizer tanks |
FR2482471A1 (en) * | 1980-05-16 | 1981-11-20 | Lambert Ind | Hydraulic agitator to maintain an aq. suspension - for blending particulate pigments into plaster or cement without mechanical beating |
US5558434A (en) * | 1994-10-12 | 1996-09-24 | Nkk Corporation | Method for preventing accumulation of sludge in a coal water mixture storage tank |
US5615950A (en) * | 1993-08-17 | 1997-04-01 | Frei; Alexandra S. | Apparatus for preventing sedimentation |
US5620250A (en) * | 1996-03-05 | 1997-04-15 | Pro-Quip, Inc. | Jet mixer having a self-centering liquid bearing hub arrangement |
US5863119A (en) * | 1996-07-03 | 1999-01-26 | J. R. Simplot Company | Apparatus for mixing a slurry within a bioreactor vessel |
US6207055B1 (en) | 1997-06-16 | 2001-03-27 | Idaho Research Foundation, Inc. | Method and apparatus for forming a slurry |
US6481885B2 (en) * | 1998-10-12 | 2002-11-19 | Petrojet International | Hydrodynamic stirring device and lance |
WO2003022464A2 (en) * | 2001-09-07 | 2003-03-20 | Gunclean Toftejorg Ab | Equipment and use of the equipment for cleaning a tank space or preparation of drilling mud |
US20050281131A1 (en) * | 2004-06-17 | 2005-12-22 | Yungblut John D | Rotary fluid agitator |
US20070084638A1 (en) * | 2005-10-19 | 2007-04-19 | Clyde Bohnsack | Drilling fluid flow facilitation |
US20120069694A1 (en) * | 2009-06-08 | 2012-03-22 | Ekato Ruhr-Und Mischtechnik Gmbh | Stirring arrangement |
US20120085688A1 (en) * | 2009-06-23 | 2012-04-12 | Zoeller Pump Company, Llc | Grinder pump basin system |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US909058A (en) * | 1907-10-16 | 1909-01-05 | Anderson William Carmichael | Apparatus for the manufacture of rosin soap and the like. |
US1192478A (en) * | 1914-06-16 | 1916-07-25 | California Macvan Company | Amalgamator. |
US1438733A (en) * | 1922-02-11 | 1922-12-12 | Ernest E Werner | Apparatus for producing emulsions |
US1706418A (en) * | 1926-11-01 | 1929-03-26 | Thomas A Sissom | Apparatus for spraying plants and trees |
US2135261A (en) * | 1936-05-11 | 1938-11-01 | John A Rosfmait | Pulp stock agitating apparatus |
US2432175A (en) * | 1944-10-16 | 1947-12-09 | George G Schmidt | Apparatus for mixing and blending fluids |
-
1948
- 1948-03-26 US US17145A patent/US2559518A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US909058A (en) * | 1907-10-16 | 1909-01-05 | Anderson William Carmichael | Apparatus for the manufacture of rosin soap and the like. |
US1192478A (en) * | 1914-06-16 | 1916-07-25 | California Macvan Company | Amalgamator. |
US1438733A (en) * | 1922-02-11 | 1922-12-12 | Ernest E Werner | Apparatus for producing emulsions |
US1706418A (en) * | 1926-11-01 | 1929-03-26 | Thomas A Sissom | Apparatus for spraying plants and trees |
US2135261A (en) * | 1936-05-11 | 1938-11-01 | John A Rosfmait | Pulp stock agitating apparatus |
US2432175A (en) * | 1944-10-16 | 1947-12-09 | George G Schmidt | Apparatus for mixing and blending fluids |
Cited By (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1075559B (en) * | 1960-02-18 | Pintsch Bamag Aktiengesellschaft, Berlin | Blade stirrer with hollow shaft for dividing gases into liquids | |
US2793005A (en) * | 1953-12-04 | 1957-05-21 | Robert J Wagner | Automatic temperature and water regulation for photographic developing |
US2963415A (en) * | 1956-08-28 | 1960-12-06 | Standard Oil Co | Asphalt blending |
US2972546A (en) * | 1957-03-08 | 1961-02-21 | Eastman Kodak Co | Method and apparatus for manufacturing colored sheeting |
US2958516A (en) * | 1957-03-15 | 1960-11-01 | Gen Motors Corp | Apparatus for making synthetic resins |
US3215624A (en) * | 1961-06-30 | 1965-11-02 | Fuller Co | Continuous ion exchange apparatus and process |
US3326815A (en) * | 1963-10-02 | 1967-06-20 | Knapsack Ag | Process for the manufacture of aqueous clay suspensions |
US4100610A (en) * | 1975-12-23 | 1978-07-11 | John Blue Company Division Of Subscription Television, Inc. | Rotating nozzle sparging system for suspension fertilizer tanks |
FR2482471A1 (en) * | 1980-05-16 | 1981-11-20 | Lambert Ind | Hydraulic agitator to maintain an aq. suspension - for blending particulate pigments into plaster or cement without mechanical beating |
US5615950A (en) * | 1993-08-17 | 1997-04-01 | Frei; Alexandra S. | Apparatus for preventing sedimentation |
US5558434A (en) * | 1994-10-12 | 1996-09-24 | Nkk Corporation | Method for preventing accumulation of sludge in a coal water mixture storage tank |
US5620250A (en) * | 1996-03-05 | 1997-04-15 | Pro-Quip, Inc. | Jet mixer having a self-centering liquid bearing hub arrangement |
US5863119A (en) * | 1996-07-03 | 1999-01-26 | J. R. Simplot Company | Apparatus for mixing a slurry within a bioreactor vessel |
US6207055B1 (en) | 1997-06-16 | 2001-03-27 | Idaho Research Foundation, Inc. | Method and apparatus for forming a slurry |
US6481885B2 (en) * | 1998-10-12 | 2002-11-19 | Petrojet International | Hydrodynamic stirring device and lance |
US7507298B2 (en) | 2001-09-07 | 2009-03-24 | Alfa Laval Tank Equipment A/S | Cleaning equipment and use thereof |
WO2003022464A3 (en) * | 2001-09-07 | 2004-03-25 | Gunclean Toftejorg Ab | Equipment and use of the equipment for cleaning a tank space or preparation of drilling mud |
US20040238009A1 (en) * | 2001-09-07 | 2004-12-02 | Henrik Falster-Hansen | Cleaning equipment and use thereof |
WO2003022464A2 (en) * | 2001-09-07 | 2003-03-20 | Gunclean Toftejorg Ab | Equipment and use of the equipment for cleaning a tank space or preparation of drilling mud |
US20050281131A1 (en) * | 2004-06-17 | 2005-12-22 | Yungblut John D | Rotary fluid agitator |
US7252429B2 (en) * | 2004-06-17 | 2007-08-07 | John David Yungblut | Rotary fluid agitator |
US20070084638A1 (en) * | 2005-10-19 | 2007-04-19 | Clyde Bohnsack | Drilling fluid flow facilitation |
US20090020336A1 (en) * | 2005-10-19 | 2009-01-22 | Clyde Bohnsack | Drilling fluid flow facilitation |
US20120069694A1 (en) * | 2009-06-08 | 2012-03-22 | Ekato Ruhr-Und Mischtechnik Gmbh | Stirring arrangement |
US8894047B2 (en) * | 2009-06-08 | 2014-11-25 | Ekato Ruehr- und Mischtechnek GmbH | Stirring arrangement |
US20120085688A1 (en) * | 2009-06-23 | 2012-04-12 | Zoeller Pump Company, Llc | Grinder pump basin system |
US9004381B2 (en) * | 2009-06-23 | 2015-04-14 | Zoeller Pump Company, Llc | Grinder pump basin system |
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