US1489786A - Machine for disintegrating and emulsifying materials - Google Patents

Machine for disintegrating and emulsifying materials Download PDF

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Publication number
US1489786A
US1489786A US655542A US65554223A US1489786A US 1489786 A US1489786 A US 1489786A US 655542 A US655542 A US 655542A US 65554223 A US65554223 A US 65554223A US 1489786 A US1489786 A US 1489786A
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machine
members
blades
casing
disintegrating
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US655542A
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Povey Harry
Hallas Haldane Oswald
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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
    • B01F27/40Mixers with rotor-rotor system, e.g. with intermeshing teeth
    • 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
    • B01F27/40Mixers with rotor-rotor system, e.g. with intermeshing teeth
    • B01F27/41Mixers with rotor-rotor system, e.g. with intermeshing teeth with the mutually rotating surfaces facing each other
    • B01F27/411Mixers with rotor-rotor system, e.g. with intermeshing teeth with the mutually rotating surfaces facing each other provided with intermeshing elements

Definitions

  • Our invention relates to machine for disintegrating solid material in the presence of a liquid and also for the emulsification or admixture of liquids.
  • Our invention has for its object to provide an improved machine in which the disintegration, emulsification or admixture of materials may be efiected in a more eflicient manner than has up to the present been attainable.
  • Our invention consists in the improved disintegrating, emulsifying or admixing machines to be hereinafter described.
  • Figure 1 shows a part sectional elevation of one form of machine constructed accordingto our invention, while Figures 2 and 3 show front elevations of the oppositely rotating members shown in Figure 1. 7
  • Figures 4, 5, 6 and 7, show sectional and front elevations alternately of modified forms of oppositely rotating members.
  • the shaft 5 is rotatably mounted on beari'ngs 7 and 8, integrally formed with the casing while the shaft 6 is similarly mounted on the bearings 9 and 10.
  • a pulley 11 is rigidly attached to the shaft 5, while a pulley 12 is similarly mounted on the shaft 6, between the bearings 9 and 10.
  • the shaft. 5 is of reduced diameter and has a threaded portion 13 formed at its outer an wh le a $89 9 threaded portion 14 is also formed on the shaft 5, in proximity to the inner face of the bearing. 'With these threaded portions circular nuts 15 and 16 engage, the nuts being provided with spaced holes 17 on their peripheries for manipulating puroses.
  • the shaft 6 is similarly formed, and is provided with nuts 18 and 19 which have holes 20 formed on their peripheries.
  • the position of the shafts 5 and 6 in the flanged sleeves 63 and 64 and consequently that of the members 3 and 4 may be ad justed relatively to one another longitudinally in order to obtain the desired clearance between the flanged portions 21 and 22 of the members, and also between the ends of the blades thereon as will be hereinafter described.
  • the projections 32, 33 and 34 on the member 4 have likewise axially disposed blades 36 formed thereon.
  • packing rings 39 and 40 are disposed between the members 3 and 4 and the portions 1 and 2 of the casing to prevent leakage of the material between these parts.
  • a gland 41 carrying a packing ring 42, and a loose ring 43 are provided around the shaft 5, to prevent leakage of lubricating oil into the casing, a similar arrangement, not shown, being provided around the shaft 6.
  • the flanged portions 21 and 22'of the members 3 and 4 are spaced a art to form a narrow annular duct throug material is projected after treatment by which the the blades, into a peripheral collecting channel 44, formed in the casing.
  • the material is fed to the pipe 45 from a ravity tank, and after. being treated is discharged from the casing through the pipe 50.
  • the material to be treated is led through the branch pipes 48 and 49 into the chambers 46 and 47,- from which. it passes through the axial ducts 37 and 38.
  • 3 gallons per minute of treated fluid may be obtained with an expenditureof 3 horse power, the material being passed only once through the machine.
  • the speed of the rotating members, the end clearance between the intermeshing bladed sections and the form and arrangement of the blades as well as the width of the annular duct may be varied as desired, or in accordance with the materials being treated.'
  • one of the liquids may be introduced through the axial duct in one of the rotating members, inthe machine illustrated in Figure 1, and the other liquid through the axial duct in theother rotating member.
  • the disintegration, emulsification or admixture of materials may be performed in an exceedingly manner and solid materials when treated alon with a liquid may be reduced to a state 0 division approaching the colloidal so that it remains in suspension for several weeks.
  • a casing In a disintegrating, emulsifying, or admixing machine, a casing, relatively rotatable members mounted in the casing and having their proximate faces formed with I interfitting relatively spaced blades and their edges beyond the blades defining a narrow discharge channel, the discharge channel being ofless widththan the space between the interfitting blades, fe ding means for delivering material into the casing beyond each of the respective members, and means formed in said members for delivering the material from the casing axially of the members and adjacent their centres of rotation.
  • a disintegrating, emulsifying or ad mixing machine a casing, aligned driven shafts mounted in the casing, a member fixed on the inner end of each shaft, the proximate faces of the members being formed with interfitting relatively s aced blades and beyond such blades to de e a narrow discharge channel, inlets formed in each member adjacent to and surrounding shaft, and means for delivering materlal. to thecasing beyond the inlets of each member.

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

Description

Apri? 8 1924.,
' 1,489,786 H. POVEY ET AL MACHINE FOR DISINTEGRATING AND EMULSIFYING MATERIALS Filed Aug. 5, 1923 I 3 Sheets-She'd 1 ff. Povqy '12. 0. Ha liars April 8, 1924; 1,489,786
H. POVEY ET AL MACHINE FOR DISINTEGRATING AND EMULSIFYING MATERIALS Filed Aug. 5, 1923 3 Sheets-Sheet 2 1!. 1 01/6 ii 0. fizz A ril 8 1924. 1,489,786
H. POVEY ET AL MACHINE FOR DISINTEGRATING AND EMULSIFYING MATERIALS Filed Aug. 5, 1923 s Sheets-Shed 3 1i Pave 12. 0.12
atented Apr.-
PATENT OFFICE.
. i- POVEY, or STANMORE, AND HALDANE OSWALD ms, or LoNnoN, ENGLAND.
MACHINE FOR DIS INTEGRATING AND EMULSIFYING MATERIALS.
Application filed August 8, 1923. Serial No. 655,542.
To all whom it may concern:
Be it known that we, HARRY Povnr and HALDANE OswALn HALLAs, both subjects of the King of Great Britain, residing at Stanmore, Middlesex, England, and London, England, respectively, have invented certain new and useful Improvements in P -Machines for Disinte rating and Emulsifying Materials, of w ich the following is a specification.
Our invention relates to machine for disintegrating solid material in the presence of a liquid and also for the emulsification or admixture of liquids.
Our invention has for its object to provide an improved machine in which the disintegration, emulsification or admixture of materials may be efiected in a more eflicient manner than has up to the present been attainable.
Our invention consists in the improved disintegrating, emulsifying or admixing machines to be hereinafter described.
Referring now to the accompanying drawings, which illustrate our invention,
and form part of our specification,
Figure 1 shows a part sectional elevation of one form of machine constructed accordingto our invention, while Figures 2 and 3 show front elevations of the oppositely rotating members shown in Figure 1. 7
Figures 4, 5, 6 and 7, show sectional and front elevations alternately of modified forms of oppositely rotating members.
In carrymg our invention into efiect according to one form, a casing formed of two similar portions 1 and 2,.is constructed and assembled as shown in Figure 1.
In this casing members 3 and 4 arranged to rotate in opposite directions, are mounted, the member 3 being mounted on the shaft 5, and the member 4 on the shaft 6.
The shaft 5 is rotatably mounted on beari'ngs 7 and 8, integrally formed with the casing while the shaft 6 is similarly mounted on the bearings 9 and 10.
Between the bearings 7 and 8, a pulley 11 is rigidly attached to the shaft 5, while a pulley 12 is similarly mounted on the shaft 6, between the bearings 9 and 10.
a 5 In the bearing 7 the shaft. 5 is of reduced diameter and has a threaded portion 13 formed at its outer an wh le a $89 9 threaded portion 14 is also formed on the shaft 5, in proximity to the inner face of the bearing. 'With these threaded portions circular nuts 15 and 16 engage, the nuts being provided with spaced holes 17 on their peripheries for manipulating puroses.
The shaft 6 is similarly formed, and is provided with nuts 18 and 19 which have holes 20 formed on their peripheries.
By manipulating the nuts 13, 16 and 18, 19, the position of the shafts 5 and 6 in the flanged sleeves 63 and 64 and consequently that of the members 3 and 4 may be ad justed relatively to one another longitudinally in order to obtain the desired clearance between the flanged portions 21 and 22 of the members, and also between the ends of the blades thereon as will be hereinafter described.
We will now describe one form of oppo-' sitely rotating members which we have found efficient in practice.
In the face of the member 3, Figures 2 and 3, we form a number of annular grooves 23, 24 and 25 with alternate annular projections 26, 27 and 28 while on the member 4 corresponding grooves 29, 30 and 31 with projections 32, 33 and 34 are simimember 3, Figure 2, a number of axially disposed blades 35 are formed.
The projections 32, 33 and 34 on the member 4 have likewise axially disposed blades 36 formed thereon.
Co-axial with the shafts 5 and 6 a number of ducts 37* and 38 respectively are formed for leading the material to the operative faces of the members 3 and 4.
Between the members 3 and 4 and the portions 1 and 2 of the casing, packing rings 39 and 40 are disposed to prevent leakage of the material between these parts.
A gland 41 carrying a packing ring 42, and a loose ring 43 are provided around the shaft 5, to prevent leakage of lubricating oil into the casing, a similar arrangement, not shown, being provided around the shaft 6. i The flanged portions 21 and 22'of the members 3 and 4 are spaced a art to form a narrow annular duct throug material is projected after treatment by which the the blades, into a peripheral collecting channel 44, formed in the casing.
- bers 46 and 47 therein by the branches 48 and 49.
The material is fed to the pipe 45 from a ravity tank, and after. being treated is discharged from the casing through the pipe 50. I
In operation, the material to be treated is led through the branch pipes 48 and 49 into the chambers 46 and 47,- from which. it passes through the axial ducts 37 and 38.
The streams of material from these ducts impinge upon one another, and are forced outwards by centrifugal force, assisted by the head in the case of gravity feed, through the bladed portions of the members 3 and 4, in which the material is-beaten, stirred and sheared and the state of division of the solids therein reduced.
The materials are thereafter ejected through the annular duct between the flanged portions 21 and 22, where a further reduction is eiiected, into the peripheral chamber 44, and are finally discharged through the outlet 50. r
In a machine constructed as above described operating with a mixture of milk powder and water and having oppositely rotating members of 6%; inches in diameter running at 3000 revolutions per minute, 3 gallons per minute of treated fluid may be obtained with an expenditureof 3 horse power, the material being passed only once through the machine.
The end and radial clearances of the blades in the above machine were approximately of an inch which the width of the annular duct between the members external to the blades was approximately .03 of an inch.
The solids in the treated fluid were re duced to a degree of division which showed no participation or sign of settlin out after several weeks observation and un er the microscope exhibited Brownian movements.
In some cases, we may modify the construction of the oppositely running members and arrange a greater number of blades thereon. In Figures 4 to 7' we have shown an example of such a modification in which a pair of rotating members 51 and 52 have four rings of blades 53, 54, 55, 56, and 57, 58, 59, respectively, with sixteen blades on each ring. The blades in this case are not formed on annular projections, as in the previous examples, but directly on the face of the oppositely rotating members. Axial ducts 61 and 62, as before, are arranged on the rotating members, for the introduction of the material.
In some cases we may modify the construction of the shown in Flgure 1, and arrange a single rotating bladed member only in the casing. This member is formed'in a similar manner to those about described, the blades thereon intermeshing with corresponding blades on the casing. A narrow annular duct extends outside the bladed sections between the rotating member and the casing, and discharges the treated material as before into a peripheral chamber.
The speed of the rotating members, the end clearance between the intermeshing bladed sections and the form and arrangement of the blades as well as the width of the annular duct may be varied as desired, or in accordance with the materials being treated.'
Although we have described our invention as operating with a mixture of milk powder and water its use is not limited to this application as it may also be used for the d1sintegration of china clay, barytes and other substances in the presence of a liquid and also for the emulsification or intimate admixture of two or more liquids.
In some cases owing to the nature of the materials being treated it may be necessary to pass them two or more times through the machineto reduce them to the state of division indicated above.
When applying our invention to the emulsification or admixture of two liquids, one of the liquids may be introduced through the axial duct in one of the rotating members, inthe machine illustrated in Figure 1, and the other liquid through the axial duct in theother rotating member.
By means of our invention the disintegration, emulsification or admixture of materials may be performed in an exceedingly eficient manner and solid materials when treated alon with a liquid may be reduced to a state 0 division approaching the colloidal so that it remains in suspension for several weeks.
We wish it to be understood that the above examples of our invention are simply to be regarded as typical only, and not as in any way restricting our invention thereto, as modifications may be made therein without departing beyond the scope of our invention.
We claim:
1. In a disintegrating, emulsifying, or admixing machine, a casing, relatively rotatable members mounted in the casing and having their proximate faces formed with I interfitting relatively spaced blades and their edges beyond the blades defining a narrow discharge channel, the discharge channel being ofless widththan the space between the interfitting blades, fe ding means for delivering material into the casing beyond each of the respective members, and means formed in said members for delivering the material from the casing axially of the members and adjacent their centres of rotation.
2. In a disintegrating, emulsifying or ad mixing machine, a casing, aligned driven shafts mounted in the casing, a member fixed on the inner end of each shaft, the proximate faces of the members being formed with interfitting relatively s aced blades and beyond such blades to de e a narrow discharge channel, inlets formed in each member adjacent to and surrounding shaft, and means for delivering materlal. to thecasing beyond the inlets of each member.
3. In a disintegrating, emulsifying or admixing machine, a casing, aligned driven shafts mounted in the casing, a member the fixed on the inner end of each shaft, the
roximate faces of the members I being 1 ormed with interfitting relatively s ace "20 blades and beyond such blades to de e a narrow discharge channel, inlets formed in each member adjacent to'and surroundingthe shaft, and means for delivering material to the casing beyond the inlets of each 25 member, said casing being formed with a receiving channelin line with and beyond the discharge channel of the members, and an outlet leading from such channels.
In testimony whereof we have signed our '30 names to thisspecification.
HARRY POVEY.
OSWALD HALLAS.
US655542A 1923-08-03 1923-08-03 Machine for disintegrating and emulsifying materials Expired - Lifetime US1489786A (en)

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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2435216A (en) * 1943-04-17 1948-02-03 C O Bartlett And Snow Company Apparatus for mixing
US3252690A (en) * 1964-06-15 1966-05-24 Warner J Cooper Liquid mixing device
US3289951A (en) * 1963-07-26 1966-12-06 Maruma Entpr Ltd Counterrotating disk cohesive material disintegrator
US4011027A (en) * 1974-09-23 1977-03-08 Escher Wyss G.M.B.H. Stain removal apparatus
US4118800A (en) * 1976-01-30 1978-10-03 Rolf Bertil Reinhall Device for use in beating or refining machines
US4131061A (en) * 1976-06-01 1978-12-26 The Bauer Bros. Co. System and apparatus for milling corn starch and like raw materials
US6016798A (en) * 1995-04-18 2000-01-25 Advanced Molecular Technologies Llc Method of heating a liquid and a device therefor
US6019499A (en) * 1995-04-18 2000-02-01 Advanced Molecular Technologies, Llc Method of conditioning hydrocarbon liquids and an apparatus for carrying out the method
US20040223406A1 (en) * 2003-05-07 2004-11-11 Burak Stephen R. Fuel processing device having magnetic coupling and method of operating thereof
US20070097784A1 (en) * 2003-10-16 2007-05-03 Basell Poliolefine Italia S.R.L. Process for the continuous production of emulsions
US20090175122A1 (en) * 2006-06-03 2009-07-09 Sascha Lais Homogenizer Device Having Horizontally Mounted Gear Rims
EP1871949A4 (en) * 2005-04-18 2011-03-16 Metso Panelboard Ab WINDOW BOX
WO2015032008A1 (en) * 2013-09-06 2015-03-12 Miteco Ag Device for mixing and/or homogenizing at least one liquid product
US20220275791A1 (en) * 2010-08-24 2022-09-01 Qwtip, Llc Waveform Disks and a System Using the Waveform Disks
US20240269629A1 (en) * 2023-02-10 2024-08-15 Coactus, LLC Fluid Refining Systems and Methods Incorporating Interlaced Cylinders

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2435216A (en) * 1943-04-17 1948-02-03 C O Bartlett And Snow Company Apparatus for mixing
US3289951A (en) * 1963-07-26 1966-12-06 Maruma Entpr Ltd Counterrotating disk cohesive material disintegrator
US3252690A (en) * 1964-06-15 1966-05-24 Warner J Cooper Liquid mixing device
US4011027A (en) * 1974-09-23 1977-03-08 Escher Wyss G.M.B.H. Stain removal apparatus
US4118800A (en) * 1976-01-30 1978-10-03 Rolf Bertil Reinhall Device for use in beating or refining machines
US4131061A (en) * 1976-06-01 1978-12-26 The Bauer Bros. Co. System and apparatus for milling corn starch and like raw materials
US6016798A (en) * 1995-04-18 2000-01-25 Advanced Molecular Technologies Llc Method of heating a liquid and a device therefor
US6019499A (en) * 1995-04-18 2000-02-01 Advanced Molecular Technologies, Llc Method of conditioning hydrocarbon liquids and an apparatus for carrying out the method
US6227193B1 (en) 1995-04-18 2001-05-08 Advanced Molecular Technologies, L.L.C. Method for heating a liquid and a device for accomplishing the same
US7186018B2 (en) * 2003-05-07 2007-03-06 Ashland Licensing And Intellectual Property Llc Fuel processing device having magnetic coupling and method of operating thereof
US20040223406A1 (en) * 2003-05-07 2004-11-11 Burak Stephen R. Fuel processing device having magnetic coupling and method of operating thereof
US20070133349A1 (en) * 2003-05-07 2007-06-14 Burak Stephen R Fuel Processing Device Having Magnetic Coupling and Method of Operating Thereof
US20070097784A1 (en) * 2003-10-16 2007-05-03 Basell Poliolefine Italia S.R.L. Process for the continuous production of emulsions
US7942572B2 (en) * 2003-10-16 2011-05-17 Basell Poliolefine Italia S.R.L. Process for the continuous production of emulsions
EP1871949A4 (en) * 2005-04-18 2011-03-16 Metso Panelboard Ab WINDOW BOX
US20090175122A1 (en) * 2006-06-03 2009-07-09 Sascha Lais Homogenizer Device Having Horizontally Mounted Gear Rims
US8215824B2 (en) * 2006-06-03 2012-07-10 Frymakoruma Ag Homogenizer device having horizontally mounted gear rims
DE102007025832B4 (en) * 2006-06-03 2016-01-14 Frymakoruma Ag Homogenizer device with horizontally mounted sprockets
US20220275791A1 (en) * 2010-08-24 2022-09-01 Qwtip, Llc Waveform Disks and a System Using the Waveform Disks
US12392330B2 (en) * 2010-08-24 2025-08-19 Qwtip Llc Waveform disks and a system using the waveform disks
WO2015032008A1 (en) * 2013-09-06 2015-03-12 Miteco Ag Device for mixing and/or homogenizing at least one liquid product
US20240269629A1 (en) * 2023-02-10 2024-08-15 Coactus, LLC Fluid Refining Systems and Methods Incorporating Interlaced Cylinders

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