US1338996A - Method of and apparatus for emulsification - Google Patents

Method of and apparatus for emulsification Download PDF

Info

Publication number
US1338996A
US1338996A US337599A US33759919A US1338996A US 1338996 A US1338996 A US 1338996A US 337599 A US337599 A US 337599A US 33759919 A US33759919 A US 33759919A US 1338996 A US1338996 A US 1338996A
Authority
US
United States
Prior art keywords
annular
bowl
passage
restricted
rotating
Prior art date
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
US337599A
Inventor
Collen E Norcross
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.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US337599A priority Critical patent/US1338996A/en
Application granted granted Critical
Publication of US1338996A publication Critical patent/US1338996A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • B01F27/81Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow

Definitions

  • My invention relates to a method of and apparatus for bringing materials into suspension in a liquid, or for emulsification.
  • My invention resides in apparatus of the character referred to wherein an annular bowl structure is employed rotatable at high speed to impart to a liquid and the material to be emulsified therewith or brought into suspension therein great centrifugal force under influence of which the mixture is caused to pass through suitable constricted passages and to suffer impact upon a wall more thoroughly and completel to induce y invention with a tubular bowl by which is effected a preliminary suspending or emulsifying action.
  • My invention resides further in an annular bowl structure formed between disk members which may yield or be moved relatively to each other in an axial direction for varying the width of a straight or circuitous restricted annular slot or passage through which the materials are forced by centrifugal action.
  • My invention resides further in such annular bowl structure with which cooperates a preferably perforated wall member, either stationary or preferably rotating with the bowl member, and against which the mixture is thrown after traversing the afore said restricted annularslot or passage.
  • My invention residesfii'rtliiT'inthe combination with structure above described of a stationary wall having a series of perforations substantially in alinement with the aforesaid slot or passage.
  • My invention resides also in a method of producing suspensions or emulsions by imparting to the mixture high rotative speed to develop sufiiciently great centrifugal force to compel the mixture to pass in a thin sheet through a restricted straight or circuitous passage in which fine subdivision and intimate mixture takes place; and fur.-
  • I igure 1 1s a veitical sectional view, some parts in elevation, of apparatus embodyingmy invention and suitable for effecting my method
  • F ig. 2 is .a fragmentary horizontal sectional View taken on the line 22 of Fig. 1.
  • Fig. 3 is a horizontal sectional view taken on the line 3--3 of Fig. 1.
  • Fig. 4 is a fragmentary view illustrating a modification.
  • Fig. 5 is a plan View of a modified form ofbowl structure.
  • Fig. 6 is a vertical sectional view taken on the line 66 of Fig. 5.
  • Fig. 7 is a top plan view of a further modification of bowl structure.
  • Fig. 8 is .a cross sectional view on the line 88 of Fig. 7.
  • A is a vessel, as of sheet metal, provided with the cover a supporting the shaft 6 rotated at high speed by any suitable means, as for example, pulley c secured upon an extension of shaft 1) and driven by belt 03.
  • any suitable means as for example, pulley c secured upon an extension of shaft 1) and driven by belt 03.
  • the tubular bowl member B Secured to or integral with the shaft 6 is the tubular bowl member B, which may'have one. or more longitudinally extending vanes e.
  • bowl B has an admission opening or port f i at its lower end, preferably of lesser diameter than the inner diameter of the bowl B to form a ledge or dam g.
  • Adjustable longitudinally upon the shaft 6 is the collar h secured to the shaft b at any desired longitudinal position by set screw 2'.
  • C and C are annular bowl members rotating with the shaft 1).
  • the member C is supported upon the shaft Z) by the sleeve j between whose flange 7c and the collar I; is the spring Z exerting downward pressure upon the member 0.
  • the member (l is supported upon the shaft 1) or bowl member B by its sleeve on.
  • the members C and G are provided with the substantially parallel flanges n and 0 between which is ormed a constricted or narrow radially extending passage, preferably ciriumferentially continuous, the vertical'width of the passage being variable by ,adjustment of the collar h by variation 1n 5 yielding of the flanges themselves when sufficiently thin and resilient.
  • the bowl space 79 between the members C and C may be traversed by a plurality of curved or straight outwardly extending vanes a, Fig.
  • 0 which may be secured to member and extend toward member C.
  • a plurality of holes or slots 1' In the upper end of the bowl member B forming communication between the interior thereof and the bowl space p is a plurality of holes or slots 1'.
  • a series of holes or slots '21 In the vertical flange or wall t and preferably in alinement with the slit or narrow annular passage between the flanges n and 0 is a series of holes or slots '21.
  • a tank T Into a tank T may be introduced the materialsto be emulsified.
  • the materialsto be emulsified For example, powdered evaporated milk, butter and warm water in case an emulsion or suspension simulating milk or cream, as for making ice cream, is desired.
  • the crude mixture may be delivered from the tank T through the pipe 2, controlled by valve a and delivered in a jet into the bowl B through the port 7.
  • the mixture may be delivered from the tank T through the pipe b controlled by valve 6 into the receptacle A in which it may rise to suitable level and pass into the bowl B through port f.' Either or both modes of delivering the material to the apparatus may be utilized, as may be desired.
  • Upon the exterior of the bowl member B may be secured any desired or suitable number of paddles or vanes (l for agitating the mixture within the receptacle A to assist in producing or maintaining the suspension or emulsion. These vanes al are particularly useful in batch operation for maintaining the materials in tank A well .mixed.
  • the crude mixture is delivered from tank T through pipe 2, at suitable rate determined by the setting of the valve a and de livered in jet form through the port 1 into the interior of the bowl B.
  • the mixture may be delivered through the pipe 72 at a the force opposing the spring Z, and byrate determined by the setting of the valve 0 into the interior of the vessel A, from which it rises through the port f into the bowl B.
  • the mixture within member B is caused to partake of similar s eed of rotation by intimate mixture of the materials as they pass therethrough into the bowl cavity between the annular bowl members 5 and C
  • the subdivision and intimate mixture of the materials is greatly increased or enhanced by rotation at high speed within the annular bowl member, slip age being prevented by the vanes q, an the mixture is subjected to far greater centrifu al force than in the tubular bowl member B, and is forced through the highly restricted slit or passage between the flanges n ando, further subdividing and intimately mixing the materials, the width of theslit or passage varying automatically with varying conditions of pressure within the annular hole structure, the spring Z yielding upwardly upon increase of pressure and returning the flanges n and 0 toward each other with decreasing pressure within the annular bow-l member, the flanges n and 0, if resilient, also yielding to pressure to increase the width of the passage between them.
  • the mixture leaves the passage between flanges n and 0 in a thin annular sheet and strikes upon the wall t of the member D which rotates with the annular bowl structure, this impact further subdividing and intimately mixing the materials, the mixture being retained by centrifugal force within the annular space between the flanges s and it, any excess overflowing through the annular space between flanges u and 0 into the interior of the receptacle A, where it may be again drawn throu h the port 7 and subjected to retreatment.
  • Mixture retained within the member D is forced outwardly through the restricted-passages or holes 01,.
  • the mixture so delivered is a suspension the spout of the notches extend the lugs f integral or emulsion which, particularly when of the materials above referred to, remains as such for a considerable length of time without serious or appreciable separation.
  • this stability is of importance in that the freezing operation need not take .place so soon after emulsification, as is the case with apparatus and methods heretofore employed,
  • the operation is continuous in that crude mixture is continuously fed from the tank T into the apparatus and the desired suspension or emulsion is continuously delivered through the spout y.
  • the .perforated impact member t may be stationary, as indicated in the fragmentary view in Fig. 4 at 6 in which case the member If is supported upon the inner wall of the vessel A and extends across the channel E. In this case the mixture passing through the apertures or restricted assages 'v in member 29 passes into channel and is delivered b spout 3/. Some of the material delivered rom the annular bowl strikes member 25 and falls into the interior of the vessel A and undergoes retreatment by reentry through the port 7 into the bowl member B.
  • Figs. .5 and 6 isindicated a modified structure of the annular bowl member.
  • the flange n has formed therein substantially rectangular or similar notches e upwardly through which and spaced from the edges with or carried by the flange 0 at its periphery.
  • the restricted passage or slit between the flanges 'n and 0 is then partly barred, in the radial direction, by -the lugs 7, against which the mixture is thrown, some rising through the narrow passage or slit 7 some through the'more or less radially extending slits it, and the remainder through the restricted passage between flanges n and 0 between neighboring lugs f this structure forming in effect a circuitous passage with sharp changes of direction of flow, which enhances sub-division and inti -m'ate mixture of the material undergoing treatment.
  • Figs. 7 and 8 is shown a modified structure for procuring a'circuitous narrow passage between the peripheral flanges upon the bowl members C and C
  • the peripheral flanges may be formed in any suitable way, as for example, in substantially straight radial portions joined by curved portions.
  • tubular bowl B As cooperating with the annular bowl structure, it will be under- Stood that the employment of the tubular bowl structure is not essential, though it is preferred, particularly in batch operation.
  • the mixture to be emulsified may be fed through an axial opening'in the annular bowl structure, as for example, through the sleeve m, which in such case may be of different diameter, generally smaller diameter.
  • a tubular member such as B may be employed which will produce inconsequential or' inconsiderable action, particularly when of smaller internal diameter and when the vane structure is omitted, and when hav-- ing unrestricted delivery into the annular bowl structure.
  • WVhile I have herein described the continuous operation of the apparatus, it may also operate upon batches of material.
  • the pipes 2 and b are omitted as well as the orificesw, channel E and spout y.
  • the material in such case is introduced into receptacle A and passes upwardly through the port f and receives treatment as hereinbefore described, the material being delivered by the bowl structure and falling again into the receptacle A an'd'undergoing retreatment until an emulsion or suspension of suitable nature is obtained, whereupon the centrifugal structure is removed with, the cover a; and the vessel A emptied and a subjecting the materials in the presence of each other to rotation at high. speed, delivering the material under the resultant centrifugal force through a narrow annular passage, impacting the annular jet of material upon a wall, and forcing the mixture through restricted orifices in said 'wall.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, and means for rotating the same athigh speed, said structure having a circuitous restricted peripheral annular discharge passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means forrotating the same at high speed, said structure comprising resilient members spaced from each. other and movable axially with respect to each other to form a restricted annular peripheral passage of varying width.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high ture comprising resilient annular members rotatable with said shaft, and peripheral flanges on said bowl members between which is formed a restricted peripheral annular passage.
  • Apparatus for producing suspensions or-emulsions comprising a shaft, means for rotating the same at high speed, bowl structure comprising annular members rotatable with said shaft, one of said membersmovable longitudinally of said shaft withre-f spect to the other, a spring opposing separation of said bowl members, and peripheral flanges onv said bowl members between which is formed a restricted annular passage.
  • Apparatus for producing suspensions or emulsions comprising annular'bowl struclen ture,means for rotating the same at high speed, said structure having a restricted (peripheral annular discharge passage, an .a
  • .wall member adapted to rotate withsaid structure receiving the impact of liquid discharged from said'passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for'rotating the same at high speed, said structure'having a restricted peripheral annular discharge passage whose h is reat as compared with its axial wi th, an a perforated wall member.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure',means for rotating the same at high speed, said structure comprisin members spaced from each other and yiel 1ng axially with respect to each other to form a restricted annular peripheral passage of varying width, and a wall member receiving the 1mpact of liquid discharged from said passage.
  • Apparatus for producing suspensions or emulsions comprising annular-bowl struc-..
  • said structure comprising members having juxtaposed peripheral flanges yielding with respect to each other, means for ad A justing said members as to their axial rela.- tion with respect to each-other, said bowl structure having a restricted lperipheral annular passage between said anges, and a perforated wall member receivin the impact of liquid discharged from sai passage;
  • Apparatus for producing suspensions or emulslons comprising a shaft, means for ture comprising annular members rotatable with said shaft, one of said members movable longitudinally of said shaft with rerotating the same at high speed, bowl strucspect to the other, peripheral flanges on said bowl members between which is formed a restricted'peripheral annular passage, and a wall member receiving the impact of liquid discharged from said passage.
  • Apparatus for producin suspensions or emulsions comprising a sha t, means for rotating-the same at high speed, bowl structure comprising annular members rotatable with said shaft, one of said members movable longitudinally of said shaftwith respect to the other, a spring opposing se aration of said bowl members, 'perip eral flanges on'said bowl members between which is formed a restricted annular passage, and a perforated wall member receiving the impact of liquid discharged from said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl struc ture, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, and a wall rotating with said structure and receiving the impactof the liquid discharged from said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, and a perforated wall rotating with said structure and receiving the impact of the liquid discharged from said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted pe-' ripheral annular discharge passage, and an open annular channel member rotating with said structure and receiving the liquid discharged from said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, and an open annular channel member rotating with said structure and receiving the liquid discharged from said passage, said channel member having perforations in its peripheral wall.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral. annular discharge passage, and a vessel inclosing said structure and having perforations in the wall thereof substantially in alinement with said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, a wall member receiving the impact of liquid discharged from said passage, and a vessel inclosing said structure and having perforations in the wall thereof substantially in alinement with said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage whose length is great as compared with its axial width, a perforated wall member receiving the impact of liquid discharged from said passage, and a vessel inclosing said structure and havingperforations in the wall thereof substantially in alinement with said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted pe ripheral annular discharge passage, a wall rotating with said structure and receiving the impact of the liquid discharged from said passage, and a vessel inclosmg said structure and having perforations in the said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, an open annular channel member rotating with said structure and receiving the liquid discharged from said passage, and a vessel inclosmg said structure and having perforations in i the wall thereof substantially in alinexnent with said passage.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, a coaxial tubular bowl member delivering into said bowl structure, and restricted orifices between said bowl member and said bowl structure.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed. said structure comprising members spaced from each other and movable axially with respect to each other to form a restricted annular peripheral passage of varying axial width, and a coaxial tubular bowl member delivering into said bowl structure.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure. means for rotating the same at high speed, said structure having a restricted pe ripheral annular discharge passage, a wall rotating with said structure and receiving the impact of the liquid discharged from said passage, and a coaxial tubular bowl member delivering into said bowl structure.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, an open annular channel member rotating with said structure and receiving the liquid discharged from said passage, .and a coaxial tubular bowl member delivering into said bowl structure.
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure. means for rotating the same at high wall thereof substantially in alinement with speed, said structure having a restricted peripheral annular discharge passage, a coaxial tubular bowl member delivering into said bowl structure, a receptacle within which said bowl member is disposed, and paddle structure on the exterior of said bowl member rotating therewith.
  • Apparatus for producing suspensions or emulsions comprising a plurality of annular members spaced from each other to form an annular bowl, peripheral flanges on said members between which is formed a restricted annular discharge passage, and vane structure within said bowl.
  • Apparatus for producing suspensions or emulsions comprising a plurality of annular members spaced from each other to form an annular bowl, peripheral flanges on said members between which is formed a restricted annular discharge passage, and
  • Apparatus for producing suspensions or emulsions comprising annular bowl structure, said structure comprising members.
  • said structure comprising juxtaposed peripheral flanges formed of joined radially straight and curved portions.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Colloid Chemistry (AREA)

Description

C. E. NORCROSS.
METHOD OF AND APPARATUS FOR EMULSIFiCATION.
APPLICATION FILED NOV-12,1919. 1,338,996. A Patented May 4, 1920.
, I 2 SHEETS-SHEET I- I c. Et'moacao'ss. METHOD OF AND APPARATUS FOR -EMULSlF|CATI-0N.
. APPLICATION FILED NOV- 12, I919: v 1,338,996. ate ted May 4, 1920.
2 SHEETS-SHEET 2- suspension or emulsification.
resides also in such structure 1n combination COLLEN E. NORCROSS, OF WEST CHESTER, PENNSYLVANIA.
METHOD OF AND APPARATUS FOR EMULSIFICA'IIGN.
Specification of Letters Patent.
Application filed November 12, 1919. Serial No. 337,599.
To all whom it may concern Be it known that I, COLLEN E. NORCROSS, a citizen of the'United States, residing in West Chester, county of Chester, and State of Pennsylvania, have invented a new and useful Method of and Apparatus for Emulsification, of which the following is a specification. I
My invention relates to a method of and apparatus for bringing materials into suspension in a liquid, or for emulsification.
My invention resides in apparatus of the character referred to wherein an annular bowl structure is employed rotatable at high speed to impart to a liquid and the material to be emulsified therewith or brought into suspension therein great centrifugal force under influence of which the mixture is caused to pass through suitable constricted passages and to suffer impact upon a wall more thoroughly and completel to induce y invention with a tubular bowl by which is effected a preliminary suspending or emulsifying action.
My invention resides further in an annular bowl structure formed between disk members which may yield or be moved relatively to each other in an axial direction for varying the width of a straight or circuitous restricted annular slot or passage through which the materials are forced by centrifugal action.
My invention resides further in such annular bowl structure with which cooperates a preferably perforated wall member, either stationary or preferably rotating with the bowl member, and against which the mixture is thrown after traversing the afore said restricted annularslot or passage.
My invention residesfii'rtliiT'inthe combination with structure above described of a stationary wall having a series of perforations substantially in alinement with the aforesaid slot or passage.
My invention resides also in a method of producing suspensions or emulsions by imparting to the mixture high rotative speed to develop sufiiciently great centrifugal force to compel the mixture to pass in a thin sheet through a restricted straight or circuitous passage in which fine subdivision and intimate mixture takes place; and fur.-
ther, in impacting the mixture delivered in a thin sheet against a stationary or rotating Patented May 4,1920.
surface for effecting further subdivision and intimate mixture.
My invention resides in furtherfeatures of structure and method hereinafter described.
For an illustration of some of the various forms my apparatus may take, and. for
an understanding of my .method, reference is to be had to the accompanying drawing,
in which;
I igure 1 1s a veitical sectional view, some parts in elevation, of apparatus embodyingmy invention and suitable for effecting my method F ig. 2 is .a fragmentary horizontal sectional View taken on the line 22 of Fig. 1.
Fig. 3 is a horizontal sectional view taken on the line 3--3 of Fig. 1.
Fig. 4 is a fragmentary view illustrating a modification.
Fig. 5 is a plan View of a modified form ofbowl structure.
Fig. 6 is a vertical sectional view taken on the line 66 of Fig. 5.
Fig. 7 is a top plan view of a further modification of bowl structure.
Fig. 8 is .a cross sectional view on the line 88 of Fig. 7. I
Referring to Figs..1 to 3 inclusive,"A is a vessel, as of sheet metal, provided with the cover a supporting the shaft 6 rotated at high speed by any suitable means, as for example, pulley c secured upon an extension of shaft 1) and driven by belt 03. Secured to or integral with the shaft 6 is the tubular bowl member B, which may'have one. or more longitudinally extending vanes e. The
bowl B has an admission opening or port f i at its lower end, preferably of lesser diameter than the inner diameter of the bowl B to form a ledge or dam g.
Adjustable longitudinally upon the shaft 6 is the collar h secured to the shaft b at any desired longitudinal position by set screw 2'. C and C are annular bowl members rotating with the shaft 1). The member C is supported upon the shaft Z) by the sleeve j between whose flange 7c and the collar I; is the spring Z exerting downward pressure upon the member 0. The member (l is supported upon the shaft 1) or bowl member B by its sleeve on. At their peripheries the members C and G are provided with the substantially parallel flanges n and 0 between which is ormed a constricted or narrow radially extending passage, preferably ciriumferentially continuous, the vertical'width of the passage being variable by ,adjustment of the collar h by variation 1n 5 yielding of the flanges themselves when sufficiently thin and resilient. The bowl space 79 between the members C and C may be traversed by a plurality of curved or straight outwardly extending vanes a, Fig.
0 3, which may be secured to member and extend toward member C. In the upper end of the bowl member B forming communication between the interior thereof and the bowl space p is a plurality of holes or slots 1'. vOn one of the annular bowl members, as C, may be secured the annular channelshaped member D by its radially extending horizontal flange s, from which depends the vertical wall 15 having the inwardly extending flange u, the. latter spaced from the flange 0. In the vertical flange or wall t and preferably in alinement with the slit or narrow annular passage between the flanges n and 0 is a series of holes or slots '21.
Preferably at the same height as the perforations '0, there are provided through the wall of the receptacle A the holes'or preferably circumferentially extending slots w communicating with the annular chamber E 80 formed between the outer surface of the receptacle A and the member 1', a delivery spout y communicating with the annular channel or space E so formed.
Into a tank T may be introduced the materialsto be emulsified. For example, powdered evaporated milk, butter and warm water in case an emulsion or suspension simulating milk or cream, as for making ice cream, is desired. The crude mixture may be delivered from the tank T through the pipe 2, controlled by valve a and delivered in a jet into the bowl B through the port 7. Or the mixture may be delivered from the tank T through the pipe b controlled by valve 6 into the receptacle A in which it may rise to suitable level and pass into the bowl B through port f.' Either or both modes of delivering the material to the apparatus may be utilized, as may be desired.
Upon the exterior of the bowl member B may be secured any desired or suitable number of paddles or vanes (l for agitating the mixture within the receptacle A to assist in producing or maintaining the suspension or emulsion. These vanes al are particularly useful in batch operation for maintaining the materials in tank A well .mixed.
The operation is as follows:
The crude mixture is delivered from tank T through pipe 2, at suitable rate determined by the setting of the valve a and de livered in jet form through the port 1 into the interior of the bowl B. Or the mixture may be delivered through the pipe 72 at a the force opposing the spring Z, and byrate determined by the setting of the valve 0 into the interior of the vessel A, from which it rises through the port f into the bowl B.
The mixture within member B is caused to partake of similar s eed of rotation by intimate mixture of the materials as they pass therethrough into the bowl cavity between the annular bowl members 5 and C The subdivision and intimate mixture of the materials is greatly increased or enhanced by rotation at high speed within the annular bowl member, slip age being prevented by the vanes q, an the mixture is subjected to far greater centrifu al force than in the tubular bowl member B, and is forced through the highly restricted slit or passage between the flanges n ando, further subdividing and intimately mixing the materials, the width of theslit or passage varying automatically with varying conditions of pressure within the annular hole structure, the spring Z yielding upwardly upon increase of pressure and returning the flanges n and 0 toward each other with decreasing pressure within the annular bow-l member, the flanges n and 0, if resilient, also yielding to pressure to increase the width of the passage between them.
The mixture leaves the passage between flanges n and 0 in a thin annular sheet and strikes upon the wall t of the member D which rotates with the annular bowl structure, this impact further subdividing and intimately mixing the materials, the mixture being retained by centrifugal force within the annular space between the flanges s and it, any excess overflowing through the annular space between flanges u and 0 into the interior of the receptacle A, where it may be again drawn throu h the port 7 and subjected to retreatment. Mixture retained within the member D is forced outwardly through the restricted-passages or holes 01,.
thereby undergoing further subdivision and intimate mixture followed by further impact upon the inner wall of the vessel A and in large proportion passing through the slots or openings w in the wall of the vessel A into the receiving channel. or conduit, E, from which it is delivered through y to any suitable receptacle.-
The mixture so delivered is a suspension the spout of the notches extend the lugs f integral or emulsion which, particularly when of the materials above referred to, remains as such for a considerable length of time without serious or appreciable separation. In the manufacture of ice cream, for example, this stability is of importance in that the freezing operation need not take .place so soon after emulsification, as is the case with apparatus and methods heretofore employed,
so far as I am aware.
By the structure and method described the operation is continuous in that crude mixture is continuously fed from the tank T into the apparatus and the desired suspension or emulsion is continuously delivered through the spout y.
' In lieu of rotating with the annular bowl structure, the .perforated impact member t may be stationary, as indicated in the fragmentary view in Fig. 4 at 6 in which case the member If is supported upon the inner wall of the vessel A and extends across the channel E. In this case the mixture passing through the apertures or restricted assages 'v in member 29 passes into channel and is delivered b spout 3/. Some of the material delivered rom the annular bowl strikes member 25 and falls into the interior of the vessel A and undergoes retreatment by reentry through the port 7 into the bowl member B.
In Figs. .5 and 6 isindicated a modified structure of the annular bowl member. The flange n has formed therein substantially rectangular or similar notches e upwardly through which and spaced from the edges with or carried by the flange 0 at its periphery. The restricted passage or slit between the flanges 'n and 0 is then partly barred, in the radial direction, by -the lugs 7, against which the mixture is thrown, some rising through the narrow passage or slit 7 some through the'more or less radially extending slits it, and the remainder through the restricted passage between flanges n and 0 between neighboring lugs f this structure forming in effect a circuitous passage with sharp changes of direction of flow, which enhances sub-division and inti -m'ate mixture of the material undergoing treatment. y
In Figs. 7 and 8 is shown a modified structure for procuring a'circuitous narrow passage between the peripheral flanges upon the bowl members C and C The peripheral flanges may be formed in any suitable way, as for example, in substantially straight radial portions joined by curved portions. The long restricted slit or passage so formed, particularly because of abrupt changes in direction, assists in subdivision and intimate mixture of the materials undergoing suspension or emulsifica tion.
While I have in each instance illustrated a tubular bowl B as cooperating with the annular bowl structure, it will be under- Stood that the employment of the tubular bowl structure is not essential, though it is preferred, particularly in batch operation.
When the tubular bowl structure is omitted, the mixture to be emulsified may be fed through an axial opening'in the annular bowl structure, as for example, through the sleeve m, which in such case may be of different diameter, generally smaller diameter.
Or a tubular member such as B may be employed which will produce inconsequential or' inconsiderable action, particularly when of smaller internal diameter and when the vane structure is omitted, and when hav-- ing unrestricted delivery into the annular bowl structure.
WVhile I have herein described the continuous operation of the apparatus, it may also operate upon batches of material. In
such case the pipes 2 and b are omitted as well as the orificesw, channel E and spout y. The material in such case is introduced into receptacle A and passes upwardly through the port f and receives treatment as hereinbefore described, the material being delivered by the bowl structure and falling again into the receptacle A an'd'undergoing retreatment until an emulsion or suspension of suitable nature is obtained, whereupon the centrifugal structure is removed with, the cover a; and the vessel A emptied and a subjecting the materials in the presence of each other to rotation at high. speed, delivering the material under the resultant centrifugal force through a narrow annular passage, impacting the annular jet of material upon a wall, and forcing the mixture through restricted orifices in said 'wall.
3. The method of bringing materials into suspension or emulsion. which consists in subjecting the materials in the presence of each other to rotation at high speed, delivering the material under the resultant centrifugal force through a narrow annular passage, impacting the annular jet of material upon awall rotating with said material, and forcing the mixture through restricted orifices in said wall.
4. The method of bringing materials into suspension or .emulsion, which consists in subjecting the materials in the presence of each other to rotation at high speed, delivering the material under the resultant centrifugal force through a. narrow-annular passage varyin in width with variations in the pressure .said rotating material, and
impacting'the annular jet of materialupon a fwall;
5. The method of bringing. materials into suspension or emulsion, which consists in subjecting the materials in the presence of each other to rotation at high speed, delivering the material under the resultant cen- 'trifugal force through a narrow annular passage varyin in Width with variations n the pressure 0 said rotatin material, and
impacting the annular jet 0 material upon.
a wall rotating with said material.
6. Apparatus for producing suspensions or emulsions comprising annular bowl structure, and means for rotating the same athigh speed, said structure having a circuitous restricted peripheral annular discharge passage.
7 Apparatus for producing suspensions or emulsions comprising annular bowl structure, means forrotating the same at high speed, said structure comprising resilient members spaced from each. other and movable axially with respect to each other to form a restricted annular peripheral passage of varying width.
8. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high ture comprising resilient annular members rotatable with said shaft, and peripheral flanges on said bowl members between which is formed a restricted peripheral annular passage.
10. Apparatus for producing suspensions or-emulsions comprising a shaft, means for rotating the same at high speed, bowl structure comprising annular members rotatable with said shaft, one of said membersmovable longitudinally of said shaft withre-f spect to the other, a spring opposing separation of said bowl members, and peripheral flanges onv said bowl members between which is formed a restricted annular passage. y
11. Apparatus for producing suspensions or emulsions comprising annular'bowl struclen ture,means for rotating the same at high speed, said structure having a restricted (peripheral annular discharge passage, an .a
.wall member adapted to rotate withsaid structure receiving the impact of liquid discharged from said'passage.
12. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for'rotating the same at high speed, said structure'having a restricted peripheral annular discharge passage whose h is reat as compared with its axial wi th, an a perforated wall member. re-
ceiving the impact of liquid discharged I from said passage.
.13. Apparatus for producing suspensions or emulsions comprising annular bowl structure',means for rotating the same at high speed, said structure comprisin members spaced from each other and yiel 1ng axially with respect to each other to form a restricted annular peripheral passage of varying width, and a wall member receiving the 1mpact of liquid discharged from said passage.
14. Apparatus for producing suspensions or emulsions comprising annular-bowl struc-..
ture, means for rotating the same at high speed, said structure comprising members having juxtaposed peripheral flanges yielding with respect to each other, means for ad A justing said members as to their axial rela.- tion with respect to each-other, said bowl structure having a restricted lperipheral annular passage between said anges, and a perforated wall member receivin the impact of liquid discharged from sai passage;
15. Apparatus for producing suspensions or emulslons comprising a shaft, means for ture comprising annular members rotatable with said shaft, one of said members movable longitudinally of said shaft with rerotating the same at high speed, bowl strucspect to the other, peripheral flanges on said bowl members between which is formed a restricted'peripheral annular passage, and a wall member receiving the impact of liquid discharged from said passage.
16. Apparatus for producin suspensions or emulsions comprising a sha t, means for rotating-the same at high speed, bowl structure comprising annular members rotatable with said shaft, one of said members movable longitudinally of said shaftwith respect to the other, a spring opposing se aration of said bowl members, 'perip eral flanges on'said bowl members between which is formed a restricted annular passage, and a perforated wall member receiving the impact of liquid discharged from said passage.
17. Apparatus for producing suspensions or emulsions comprising annular bowl struc ture, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, and a wall rotating with said structure and receiving the impactof the liquid discharged from said passage.
18. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, and a perforated wall rotating with said structure and receiving the impact of the liquid discharged from said passage.
19. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted pe-' ripheral annular discharge passage, and an open annular channel member rotating with said structure and receiving the liquid discharged from said passage.
20. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, and an open annular channel member rotating with said structure and receiving the liquid discharged from said passage, said channel member having perforations in its peripheral wall.
21. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral. annular discharge passage, and a vessel inclosing said structure and having perforations in the wall thereof substantially in alinement with said passage.
22. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, a wall member receiving the impact of liquid discharged from said passage, and a vessel inclosing said structure and having perforations in the wall thereof substantially in alinement with said passage.
23. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage whose length is great as compared with its axial width, a perforated wall member receiving the impact of liquid discharged from said passage, and a vessel inclosing said structure and havingperforations in the wall thereof substantially in alinement with said passage.
24. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted pe ripheral annular discharge passage, a wall rotating with said structure and receiving the impact of the liquid discharged from said passage, and a vessel inclosmg said structure and having perforations in the said passage.
25. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, an open annular channel member rotating with said structure and receiving the liquid discharged from said passage, and a vessel inclosmg said structure and having perforations in i the wall thereof substantially in alinexnent with said passage.
26. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, a coaxial tubular bowl member delivering into said bowl structure, and restricted orifices between said bowl member and said bowl structure.
27. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed. said structure comprising members spaced from each other and movable axially with respect to each other to form a restricted annular peripheral passage of varying axial width, and a coaxial tubular bowl member delivering into said bowl structure.
28. Apparatus for producing suspensions or emulsions comprising annular bowl structure. means for rotating the same at high speed, said structure having a restricted pe ripheral annular discharge passage, a wall rotating with said structure and receiving the impact of the liquid discharged from said passage, and a coaxial tubular bowl member delivering into said bowl structure.
29. Apparatus for producing suspensions or emulsions comprising annular bowl structure, means for rotating the same at high speed, said structure having a restricted peripheral annular discharge passage, an open annular channel member rotating with said structure and receiving the liquid discharged from said passage, .and a coaxial tubular bowl member delivering into said bowl structure.
80. Apparatus for producing suspensions or emulsions comprising annular bowl structure. means for rotating the same at high wall thereof substantially in alinement with speed, said structure having a restricted peripheral annular discharge passage, a coaxial tubular bowl member delivering into said bowl structure, a receptacle within which said bowl member is disposed, and paddle structure on the exterior of said bowl member rotating therewith.
31. Apparatus for producing suspensions ber, restricted outlet structure at the other end of said bowl member, and paddle structure on the exterior of said bowl member rotating therewith.
j 32. Apparatus for producing suspensions or emulsions comprising a plurality of annular members spaced from each other to form an annular bowl, peripheral flanges on said members between which is formed a restricted annular discharge passage, and vane structure within said bowl.
33. Apparatus for producing suspensions or emulsions comprising a plurality of annular members spaced from each other to form an annular bowl, peripheral flanges on said members between which is formed a restricted annular discharge passage, and
'- vane structure within saidbowl secured upon one of said members and extending toward the other.
34. The method of bringing materials into suspension or emulsion, which consists in agitating and mixing said materials, subjecting said materials to rotation at high speed, delivering the materials under the resultant centrifugal force through restricted orifices, again subjecting said materials to rotation at high speed, and impacting said materials under the resultant centrifugal force upon a wall.
35. The method of bringing materials into suspension or emulsion, which consists in agitating and mixing said materials, subjecting the resultant mixture to rotation at high speed and delivering them through restricted orifices, again subjecting said materials to rotation at high speed, delivering said materials through a narrow annular passage, impacting said materials upon a wall, and forcing said materials through restricted orifices in said wall.
36. The method of bringing materials into suspension or emulsion, which consists in subjecting the materials to rotation at high speed, delivering the materials under the resultant centrifugal force through a narrow annular orifice, impacting the resultant annular jet upon a wall having restricted restricted orifices in said wall under the resultant centrifugal force, collecting the remainder of said materials, and returning said collected materials for retreatment.
38. The method of bringing materials into suspension or emulsion, which consists in delivering said materials in rapid rotation and under centrifugal force through an extended narrow annular orifice, impacting the resultant annular jet against a wall and forcing said materials in rapid rotation and under centrifugal force through restricted orifices, and impacting the materials passing through said orifices under centrifugal force upon a wall.
39. Apparatus for producing suspensions or emulsions comprising annular bowl structure, said structure comprising members.
having juxtaposed peripheral fianges, and a channel member surrounding the periphery of said flanges comprising an upper wall secured to one flange member and paral lel thereto, a second wall spaced from and perpendicular to said flan es, and a third wall parallel to and spaced from said flanges, said perpendicular wall having restricted orifices.
40. Apparatus for producing suspensions or emulsions comprising bowl structure,
means for rotating the same at high speed,
said structure comprising juxtaposed peripheral flanges formed of joined radially straight and curved portions.
in testimony whereof I have hereunto aflixed my signature this 10th day of November, 1919.
COLLEN E. Nono'aoss.
US337599A 1919-11-12 1919-11-12 Method of and apparatus for emulsification Expired - Lifetime US1338996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US337599A US1338996A (en) 1919-11-12 1919-11-12 Method of and apparatus for emulsification

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US337599A US1338996A (en) 1919-11-12 1919-11-12 Method of and apparatus for emulsification

Publications (1)

Publication Number Publication Date
US1338996A true US1338996A (en) 1920-05-04

Family

ID=23321197

Family Applications (1)

Application Number Title Priority Date Filing Date
US337599A Expired - Lifetime US1338996A (en) 1919-11-12 1919-11-12 Method of and apparatus for emulsification

Country Status (1)

Country Link
US (1) US1338996A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2572287A (en) * 1946-08-28 1951-10-23 Laval Separator Co De Method and apparatus for treating mixtures to make or break emulsions
US2584424A (en) * 1952-02-05 Method and apparatus for treating
US5292194A (en) * 1988-08-16 1994-03-08 Dieter Gabor Device for preparing liquid to thin pulpy media
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
US20040022122A1 (en) * 2002-08-02 2004-02-05 Kozyuk Oleg V. Devices for cavitational mixing and pumping and methods of using same

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2584424A (en) * 1952-02-05 Method and apparatus for treating
US2572287A (en) * 1946-08-28 1951-10-23 Laval Separator Co De Method and apparatus for treating mixtures to make or break emulsions
US5292194A (en) * 1988-08-16 1994-03-08 Dieter Gabor Device for preparing liquid to thin pulpy media
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
US20040022122A1 (en) * 2002-08-02 2004-02-05 Kozyuk Oleg V. Devices for cavitational mixing and pumping and methods of using same
US6857774B2 (en) 2002-08-02 2005-02-22 Five Star Technologies, Inc. Devices for cavitational mixing and pumping and methods of using same

Similar Documents

Publication Publication Date Title
US4026817A (en) Method for the preparation in a continuous way of water/oil emulsions and apparatus suitable therefor
US2706108A (en) Apparatus for continuously blending latex and a preformed froth
US1338996A (en) Method of and apparatus for emulsification
US1842877A (en) Apparatus for the preparation of emulsions
US3233835A (en) Apparatus for milling and dispersing substances in liquid media
US1906457A (en) Means for feeding liquids to centrifugal separator bowls
US1589097A (en) Apparatus for continuously separating liquids from solids
US2557629A (en) Method and apparatus for continuous centrifugal separation
US1718871A (en) Method of and means for separating comminuted matter from the liquid in which it is immersed
US2010405A (en) Centrifugal method and apparatus
US2645415A (en) Centrifugal bowl
US1363572A (en) Emulsifier
US1724254A (en) Centrifugal separator
US2068136A (en) Process of preparing emulsions
US1926484A (en) Method and apparatus for emulsifying
US1701164A (en) Mixing apparatus and process
GB409832A (en) Improvements in or relating to methods of and means for effecting centrifugal separation
US2649287A (en) Apparatus for continuous frothing of rubber latex
US1398735A (en) Method of desiccating fluid mixtures
US1650685A (en) Process and apparatus for separating liquids from solids
US1526465A (en) Process of producing emulsions
US1362131A (en) Method and apparatus for emulsification
US1266501A (en) Emulsifier.
US1770302A (en) Mixing and emulsifying apparatus
US1678477A (en) Process for whipping or agitating cream