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US3269709A - Mixing head - Google Patents

Mixing head Download PDF

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Publication number
US3269709A
US3269709A US410429A US41042964A US3269709A US 3269709 A US3269709 A US 3269709A US 410429 A US410429 A US 410429A US 41042964 A US41042964 A US 41042964A US 3269709 A US3269709 A US 3269709A
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United States
Prior art keywords
guide ring
funnel
mixing head
screens
vane wheel
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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
Application number
US410429A
Inventor
Roland Karg
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Dr Karg GmbH
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Dr Karg GmbH
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Publication date
Application filed by Dr Karg GmbH filed Critical Dr Karg GmbH
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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
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/86Mixing heads comprising a driven stirrer
    • B01F33/862Mixing heads comprising a driven stirrer the stirrer being provided with a surrounding stator
    • 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
    • B01F27/15Stirrers with tubes for guiding the material

Definitions

  • This invention relates to a mixing head for the homogenization, emulsification, dispersion, etc., of media having a highly fluid to highly viscous consistency, and for introducing dry solids to liquids.
  • the known mixing heads comprise a vane wheel or impeller, which is arranged in a cylindrical guide ring, which may be formed with apertures in its lower portion.
  • eddies formed near the rim of the guide ring upstream of the latter and had an adverse effeet on the action of the mixing head.
  • a mere increase in the length of the guide ring results in an appreciable increase in the resistance to flow so that the efiiciency of the mixing device is reduced.
  • An important object of the invention is to eliminate the above disadvantages of the known devices. This is achieved in that a funnel for the introduction of the material to be mixed is provided on the inflow side of said guide ring and the height of said funnel is substantially as large as the height of the guide ring.
  • FIG. 1 is a longitudinal sectional view showing a first embodiment.
  • FIG. 2 is also a longitudinal sectional view showing another embodiment, in which the funnel has an extension which is spaced around and overlaps the guide ring.
  • FIG. 3 is a longitudinal sectional view showing an embodiment which is basically similar to that of FIG. 1 but has a guide ring additionally provided with a baflle, and
  • FIG. 4 is a longitudinal sectional view showing an embodiment which is basically similar to that of FIG. 2 but has a funnel which has a curved generatrix.
  • the vane wheel is designated 1. This wheel may be replaced by a disc or the like.
  • the vane wheel 1 is mounted at the end of a shaft, which is mounted in a stationary bearing tube 2 and can be driven by an electric motor, not shown.
  • the vane wheel 1 is surrounded by a cylindrical guide or control ring 3, which is formed in its lower half with elongated apertures 4, which are regularly spaced around its periphery and extend longitudinally in the peripheral direction of the guide ring. Means, not shown, are provided to enable an axial adjustment of the guide ring 3 and the vane wheel 1 relative to each other.
  • a funnel 6 is arranged, which in the embodiment shown in FIG.
  • the vane wheel is substantially disposed at the junction between the guide ring 3 and the funnel 6.
  • the included angle a of this funnel is relatively large, but less than 90. The size of this included angle will be selected in view of the viscosity of the medium to be treated.
  • the height 8 of the funnel is substantially as large as the height 7 of the guide ring.
  • a plurality of braces 9 are connected to the funnel and have preferably a so-called streamlined crosssection to reduce the resistance to flow. These braces extend from a collar, which is mounted on the bearing tube 2.
  • Screens 10, 11 are mounted in the guide ring 3 below the vane wheel 1. These screens are disposed below and above the apertures in the guide ring, respectively. Each screen may be replaced by a plurality of screens.
  • the screens 10, 11 may have the same mesh size. It is preferable, however, to use an upper screen 10 having a larger mesh size than the lower screen 11.
  • the arrangement of the screens or only one screen particularly below the apertures is desirable particularly when pulverulent substances are to be dispensed in liquid or highly viscous media.
  • the powder to be dispersed has formed aggregates which are surrounded on the outside by an adhesive layer and which may be obtained particularly at the beginning of the dispersing operation, these aggregates will be disintegrated as they pass through the screen or screens and will be caused to disappear entirely as the mixing operation proceeds.
  • FIG. 2 shows the mixing head according to the invention in an embodiment which is particularly suit-able for liquids of low viscosity.
  • the funnel 6 does not merge directly into the top rim 5 of the guide ring 3 but is provided at its lower end with a cylindrical extension 12, which is spaced around and overlaps the upper rim 5 of the guide ring 3 so that the guide ring 3 and extension 12 define an annular space 13 between them.
  • the guide ring 3 is connected by braces 14 to the funnel 6, more particularly to its extension 12.
  • the funnel 6 is located by braces 9 to the machine frame, particularly to a collar of the bearing tube 2.
  • the funnel has the shape of a truncated straight cone.
  • the funnel may have generatrices which follow a curve which is convex with respect to the axis of the funnel or of the machine housing, preferably according to a logarithmic curve.
  • the funnel has a rounded portion merging with the extension.
  • the embodiment shown in longitudinal section in FIG. 3 is basically similar to that of FIG. 1 with the difference that the guide ring 3 carries at its outlet end a baffle plate 15, which is spaced below the lower rim of the guide ring 3 and has a diameter which is substantially as large as the outside diameter of the guide ring 3.
  • Braces 16 for fixing the baffle plate to the guide ring are regularly spaced around the periphery of the bafile plate.
  • the distance between the baffie plate and the lower rim of the guide ring 3 will depend on the nature of the liquid to be mixed. It is an object of the battle plate to cause a sudden deflection, virtually at right angles, of the flow emerging from the guide ring 3. This results in an improvement of the action of the mixing head.
  • the bafile plate may be provided with holes, if desired.
  • the embodiment shown in FIG. 4 is basically similar to the embodiment shown in FIG. 2 but comprises a funnel 6, which has a generatrix that follows a curve which is concave with respect to the axis of the funnel.
  • the curve begins preferably in the axial direction and progressively leads away from the axis, particularly according to a logarithmic function. Funnels extending according to such a curve may be used in all embodiments which have been described, of course.
  • the vane wheel may be fixed and the vane wheel may be arranged for adjustment in an axial direction along the drive shaft.
  • a mixing head comprising an impeller arranged in a guide ring through which the material to be mixed flows, drive means connected to said impeller, and a funnel disposed on the inflow side of said guide ring and serving to introduce the material to be mixed to the guide ring, the height of said funnel being substantially equal to the height of the guide ring, said funnel being provided at its lower end with a cylindrical extension, which is radi- 4 ally spaced around the upper portion of the guide ring, and the said guide ring being secured to said extension.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

Aug. 30, 1966 KARG Q 3,269,709
MIXING HEAD Filed Nov. 12, 1964 I NVENTOR.
ROLAND KARG .4 TTOR NE Y8 3,269,709 MIXING HEAD Roland Karg, Stuttgart, Germany, assignor to Dr. Karg G.m.b.H., Stuttgart, Germany Filed Nov. 12, 1964, Ser. No. 410,429 Claims priority, application Germany, Nov. 22, 1963, K 51,431 1 Claim. (Cl. 259-97) This invention relates to a mixing head for the homogenization, emulsification, dispersion, etc., of media having a highly fluid to highly viscous consistency, and for introducing dry solids to liquids.
The known mixing heads comprise a vane wheel or impeller, which is arranged in a cylindrical guide ring, which may be formed with apertures in its lower portion. In these devices, eddies formed near the rim of the guide ring upstream of the latter and had an adverse effeet on the action of the mixing head. On the other hand, a mere increase in the length of the guide ring results in an appreciable increase in the resistance to flow so that the efiiciency of the mixing device is reduced.
An important object of the invention is to eliminate the above disadvantages of the known devices. This is achieved in that a funnel for the introduction of the material to be mixed is provided on the inflow side of said guide ring and the height of said funnel is substantially as large as the height of the guide ring.
It is another object of the invention to provide a mixing device for an increased throughput of liquid not only as a result of the improved inflow conditions but also of the increase of the total inflow area.
Further features of the invention will be explained with reference to the drawing, which shows various illustrative embodiments of the mixing head according to the invention. FIG. 1 is a longitudinal sectional view showing a first embodiment. FIG. 2 is also a longitudinal sectional view showing another embodiment, in which the funnel has an extension which is spaced around and overlaps the guide ring. FIG. 3 is a longitudinal sectional view showing an embodiment which is basically similar to that of FIG. 1 but has a guide ring additionally provided with a baflle, and FIG. 4 is a longitudinal sectional view showing an embodiment which is basically similar to that of FIG. 2 but has a funnel which has a curved generatrix.
In the embodiment shown in FIG. 1, the vane wheel is designated 1. This wheel may be replaced by a disc or the like. The vane wheel 1 is mounted at the end of a shaft, which is mounted in a stationary bearing tube 2 and can be driven by an electric motor, not shown. The vane wheel 1 is surrounded by a cylindrical guide or control ring 3, which is formed in its lower half with elongated apertures 4, which are regularly spaced around its periphery and extend longitudinally in the peripheral direction of the guide ring. Means, not shown, are provided to enable an axial adjustment of the guide ring 3 and the vane wheel 1 relative to each other. Above the guide ring, on its inflow side, a funnel 6 is arranged, which in the embodiment shown in FIG. 1 has a substantially straight generatrix and merges directly into upper edge 5 of the guide ring 3 with a rounded portion shaped to reduce any turbulence. The vane wheel is substantially disposed at the junction between the guide ring 3 and the funnel 6. The included angle a of this funnel is relatively large, but less than 90. The size of this included angle will be selected in view of the viscosity of the medium to be treated. The height 8 of the funnel is substantially as large as the height 7 of the guide ring. A plurality of braces 9 are connected to the funnel and have preferably a so-called streamlined crosssection to reduce the resistance to flow. These braces extend from a collar, which is mounted on the bearing tube 2.
Screens 10, 11 are mounted in the guide ring 3 below the vane wheel 1. These screens are disposed below and above the apertures in the guide ring, respectively. Each screen may be replaced by a plurality of screens. The screens 10, 11 may have the same mesh size. It is preferable, however, to use an upper screen 10 having a larger mesh size than the lower screen 11. The arrangement of the screens or only one screen particularly below the apertures is desirable particularly when pulverulent substances are to be dispensed in liquid or highly viscous media. When the powder to be dispersed has formed aggregates which are surrounded on the outside by an adhesive layer and which may be obtained particularly at the beginning of the dispersing operation, these aggregates will be disintegrated as they pass through the screen or screens and will be caused to disappear entirely as the mixing operation proceeds. When two screens are disposed above and below the apertures, respectively, the medium cannot be retained between these screens even when it is highly concentrated because all particles disposed between the screens can pass out through the apertures so that they are once more admitted to the vane wheel. Hence, the flow through the guide ring or control ring cannot be impeded.
FIG. 2 shows the mixing head according to the invention in an embodiment which is particularly suit-able for liquids of low viscosity. In this embodiment the funnel 6 does not merge directly into the top rim 5 of the guide ring 3 but is provided at its lower end with a cylindrical extension 12, which is spaced around and overlaps the upper rim 5 of the guide ring 3 so that the guide ring 3 and extension 12 define an annular space 13 between them. The guide ring 3 is connected by braces 14 to the funnel 6, more particularly to its extension 12. The funnel 6 is located by braces 9 to the machine frame, particularly to a collar of the bearing tube 2. The funnel has the shape of a truncated straight cone. Alternatively, it may have generatrices which follow a curve which is convex with respect to the axis of the funnel or of the machine housing, preferably according to a logarithmic curve. In any case, the funnel has a rounded portion merging with the extension. The provision of the funnel with an extension which is spaced around the guide ring results in an additional liquid flow on the outside of the guide ring during the operation of the mixing head. Particularly with liquids of low viscosity, this liquid flow affords an additional improvement of the action of the mixing head.
The embodiment shown in longitudinal section in FIG. 3 is basically similar to that of FIG. 1 with the difference that the guide ring 3 carries at its outlet end a baffle plate 15, which is spaced below the lower rim of the guide ring 3 and has a diameter which is substantially as large as the outside diameter of the guide ring 3. Braces 16 for fixing the baffle plate to the guide ring are regularly spaced around the periphery of the bafile plate. The distance between the baffie plate and the lower rim of the guide ring 3 will depend on the nature of the liquid to be mixed. It is an object of the battle plate to cause a sudden deflection, virtually at right angles, of the flow emerging from the guide ring 3. This results in an improvement of the action of the mixing head. The bafile plate may be provided with holes, if desired.
The embodiment shown in FIG. 4 is basically similar to the embodiment shown in FIG. 2 but comprises a funnel 6, which has a generatrix that follows a curve which is concave with respect to the axis of the funnel. The curve begins preferably in the axial direction and progressively leads away from the axis, particularly according to a logarithmic function. Funnels extending according to such a curve may be used in all embodiments which have been described, of course.
To vary the relative position of the vane wheel and the guide ring, the latter may be fixed and the vane wheel may be arranged for adjustment in an axial direction along the drive shaft.
What is claimed is:
A mixing head comprising an impeller arranged in a guide ring through which the material to be mixed flows, drive means connected to said impeller, and a funnel disposed on the inflow side of said guide ring and serving to introduce the material to be mixed to the guide ring, the height of said funnel being substantially equal to the height of the guide ring, said funnel being provided at its lower end with a cylindrical extension, which is radi- 4 ally spaced around the upper portion of the guide ring, and the said guide ring being secured to said extension.
References Cited by the Examiner UNITED STATES PATENTS 2,140,315 12/1938 Dollinger 259-97 2,663,236 12/1953 Blankenship et a1 259-97 2,718,385 9/1955 Greblick et al. 25997 FOREIGN PATENTS 1,254,351 1/1961 France.
490,130 12/1930 Germany.
366,166 1/1963 Switzerland.
WALTER A. SCHEEL, Primary Examiner.
ROBERT W. JENKINS, Assistant Examiner.
US410429A 1963-11-22 1964-11-12 Mixing head Expired - Lifetime US3269709A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEK51431A DE1219447B (en) 1963-11-22 1963-11-22 Mixing head for homogenizing u. Like. From media of liquid to highly viscous consistency

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US3269709A true US3269709A (en) 1966-08-30

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US (1) US3269709A (en)
AT (1) AT250917B (en)
BE (1) BE656004A (en)
CH (1) CH434206A (en)
DE (1) DE1219447B (en)
DK (1) DK114760B (en)
GB (1) GB1021606A (en)
NL (2) NL149087B (en)
SE (1) SE218371C1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3572658A (en) * 1968-01-15 1971-03-30 Richards Of Rockford Inc Floating aerator
US20150367302A1 (en) * 2013-01-23 2015-12-24 Ge Healthcare Bio-Sciences Ab Magnetic agitator mixing system and an agitator mixing stand

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3517655A1 (en) * 1985-05-15 1986-11-20 Ystral Gmbh Maschinenbau Und Processtechnik, 7801 Ballrechten-Dottingen DEVICE FOR MIXING AND DISPERSING AT LEAST TWO MEDIA
US4871448A (en) * 1988-06-14 1989-10-03 Gosudarstvenny Proektno-Konstruktorsky I Experimentalny Institut Po Obogatitelnomu Oborudovaniju Mechanical flotation machine

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE490130C (en) * 1930-01-24 Paul Rueters Device for destroying the foam of milk in continuous heating tubs
US2140315A (en) * 1936-07-27 1938-12-13 Lewis L Dollinger Mixing apparatus
US2663236A (en) * 1950-12-14 1953-12-22 Jr William G Blankenship Fluid treating tank for photographic developing
US2718385A (en) * 1952-12-23 1955-09-20 Ethyl Corp Stirring apparatus
FR1254351A (en) * 1960-04-19 1961-02-17 Cofinin Company For Financial Method of mixing a heterogeneous liquid mass and corresponding stirring device
CH366166A (en) * 1960-04-28 1962-12-15 Schaerli Robert Slurry mixer

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1989668A (en) * 1931-08-07 1935-02-05 Garthe Fritz Mixing apparatus
US2061564A (en) * 1934-08-29 1936-11-24 Drake Diffusion impeller deflector
US2772863A (en) * 1954-08-30 1956-12-04 Pacific Pumps Inc Mixing pump
DE1034149B (en) * 1955-05-07 1958-07-17 Hans Kotthoff Centrifugal mixer with a fixedly arranged resistance element ring concentrically surrounding the centrifugal wheel
DE1779439A1 (en) * 1968-08-12 1971-09-30 Bottlaender Wilfried Dr Ing Device for ventilating, cooling and air-conditioning rooms, in particular greenhouses

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE490130C (en) * 1930-01-24 Paul Rueters Device for destroying the foam of milk in continuous heating tubs
US2140315A (en) * 1936-07-27 1938-12-13 Lewis L Dollinger Mixing apparatus
US2663236A (en) * 1950-12-14 1953-12-22 Jr William G Blankenship Fluid treating tank for photographic developing
US2718385A (en) * 1952-12-23 1955-09-20 Ethyl Corp Stirring apparatus
FR1254351A (en) * 1960-04-19 1961-02-17 Cofinin Company For Financial Method of mixing a heterogeneous liquid mass and corresponding stirring device
CH366166A (en) * 1960-04-28 1962-12-15 Schaerli Robert Slurry mixer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3572658A (en) * 1968-01-15 1971-03-30 Richards Of Rockford Inc Floating aerator
US20150367302A1 (en) * 2013-01-23 2015-12-24 Ge Healthcare Bio-Sciences Ab Magnetic agitator mixing system and an agitator mixing stand

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Publication number Publication date
CH434206A (en) 1967-04-30
GB1021606A (en) 1966-03-02
NL7605359A (en) 1976-08-31
NL149087B (en) 1976-04-15
DE1219447B (en) 1966-06-23
AT250917B (en) 1966-12-12
SE218371C1 (en) 1968-01-23
NL6413567A (en) 1965-05-24
DK114760B (en) 1969-08-04
BE656004A (en) 1965-03-16

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