US1789320A - Apparatus for mixing materials - Google Patents

Apparatus for mixing materials Download PDF

Info

Publication number
US1789320A
US1789320A US73609A US7360925A US1789320A US 1789320 A US1789320 A US 1789320A US 73609 A US73609 A US 73609A US 7360925 A US7360925 A US 7360925A US 1789320 A US1789320 A US 1789320A
Authority
US
United States
Prior art keywords
conduits
bulk supply
mixed
conduit
mixing
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
US73609A
Inventor
Frederick C Overbury
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.)
Flintkote Co
Original Assignee
Flintkote Co
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 Flintkote Co filed Critical Flintkote Co
Priority to US73609A priority Critical patent/US1789320A/en
Application granted granted Critical
Publication of US1789320A publication Critical patent/US1789320A/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
    • B01F27/85Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts
    • B01F27/851Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts the receptacle being subdivided in adjacent compartments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32Driving arrangements
    • B01F35/323Driving arrangements for vertical stirrer shafts
    • B01F35/3231Driving several stirrer shafts, e.g. about the same axis
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S366/00Agitating
    • Y10S366/605Paint mixer

Definitions

  • This invention relates to process and ap-* paratus for mixing materials, and refers more particularly to a process and apparatus 5 for producing emulsions. and mixtures there- -'5' of, and is more specifically directed to a device in which relatively large quantities of emulsion and mixtures thereof can be produced, with a high rate of production.
  • the invention is also designed to accommodate a plurality of streams of material undergoing simultaneous emulsification. By dividing these streams instead of introducing a combined stream, better emulsification and finer dispersion will result.
  • the apparatus is also designed to provide better means of controlling the temperatures than may be affected' with present types of apparatus.
  • the improvements in the present invention comprise a plurality of open ended mixing or emulsifying conduits preferably equi-spaced from each other and supportedin an enlarged chamber in which a bulk supply of the end product is maintained.
  • Agitating elements are mounted in the individual conduits, each conduit having separate inlets for the materials tote mixed or emulsi-n fied therein.
  • FIG. 2 is a top plan view of Fig. 1, eliminating the gears and bearing support therefor, for the sake of clearness
  • Fig. 3 is a cross sectional side elevational view of a somewhat modified type of apparatus.
  • Fig. 1 designates a main chamber or vessel for containing a bulk supply of the end product having aclosed base 2 and open to the atmosphere at its upper end.
  • a plurality of open ended conduits are mounted within the vessel 1, their lower open ends being spaced away from the base 2 and supported by means of the supports 4, and their upper ends dis posed below the normal level ofthe bulk sup--'
  • Fig. 1 is a diagrammatic terial' ply of end product in the container. There may be any number of these open ended conduits 3 preferably equi-spaced from each other.
  • the conduits are preferably pro-" 'vided with jackets 5 for-the purpose of per- ".understood of course, that there may be any number of these propeller or agitator blades and that they may be spaced at varying dis tances from each other, although itis-pref erable to provide propeller'blades having an upward pitch:
  • The'enlarged 'gear7 isadapted to mesh with thesmal-lpinion gears 9 t0 drive the propeller shafts '10.
  • One of these propeller shafts 10 is mounted in each of the conduits 3 and-is also provided intermediate its lengthflwith propellergior agitator .7 blades 11.; 7
  • the container 1 is also provided with a jacket 12 for theintroduction of a cooling or' heating medium.
  • the bearings 13 for the shafts6 and 10 may be supported on the bracket support. 14 mounted above the container'.
  • An inlet pipe 16 communicates 5 for the purpose of introducing the heating or cooling medium, this particular jacket discharging said heating or cooling medium into the cooling coil 15, which cooling coil discharges said heating or cooling medium into another jacket 5, and from this jacket through the connectingpipes 17- into the The heating or cooling medium may then be withdrawn through the discharge pipe 18.
  • the mixer is provided with the drawofi 19 which may be provided with the knife valve or gate 20, and a plurality of pipes 21 and 22 1 are provided discharging into each oithe conduits 3, preferably two for each conother or others may be used merely as a secondary mixing device by refraining from introducmg any new materials to be emulsified.
  • the present invention contemplates the simultaneous emulsification of two or more difierent types of waterproofing material, for example, in one or more conduits, one type of waterproofing material such for instance, as asphalt, may be undergoing emulsification while simultaneously. in another or others, a different type of waterproofing materialsuch for instance, as a resinous pitch may be undergoing emulsification, so that *the finished product will have difierent constituents as its internal phase.
  • the differentconduits may be supplied with different types of emulsifying agent'such as different kinds of clay, bentonite or other colloid.
  • the addition of va-- rious fillers, coloring agents and fibres may also be made by employing one or more of the conduits 3 for this purpose. while emulsification is taking place in an adjacent conduit or conduits.
  • FIG. 3 the apparatus there described, is similar to theapparain Figs. 1 and 2, including as part ofthe mixing unit an additional mixing chamber23 in which rotates the driving shaft 24 provided with the propeller or agitator blades 25 and'having a sprocket 26 at its upper end, which sprocket is driven by means of the sprocket chain 27 meshin t with a similar sprocket 28 mounted on the hearing 4 of shaft 6.
  • the mixed or emulsified mass will flow upwardly into the space 29 and eventually over the wall of the conduit 23.
  • Fillers, pigments, fibres and other materials may be introduced to the conduit 23 through the inlet pipe 30, the intermediate mixture being agitated and thoroughly incorporated together by meansof the propeller blades 35 in this auxiliary conluo duit 23 and withdrawn through the outlet 19 controlled by valve 20.
  • one or more of the conduits 3 may be used to produce an emulsion, that is, such conduits may receive regulated quantities of colloid and paint base whilethei other conduits may receive regulated quantities of pigment in aqueous suspension.
  • the present invention is particularly directed to either continuous or batch operation.
  • the present invention utilizes one of the principles of the co-pending application referred to, namely that the mixing of fresh charges of material should take place in the presence of a bulk supply of previously formed end product, in order to produce the most satisfactory results.
  • the combination with a container for holding a bulk supply of the mixed end product, of a plurality of open ended conduits disposed in said container below the duits disposed in said container below the normal level of said bulk supply, inlets in-- dividual to each conduit for introducing fresh charges of materials to be mixed, agitator elements mounted in each conduit adapted to force the mass therein downwardly, separate agitating means positioned in the open central space between the conduits adapted to impart an upward movement to the bulk supply, and means for withdrawing regulated quantities of the mixed product, said separate agitating means being adapted to rotate at a relatively lower speed than the agitating elements in the conduits.
  • the combination with an enlarged container for holding a bulk supply of end product, of a plurality of separated mixing zones disposed therein, charging means communicating with each separate mixing zone for introducing fresh charges of materials to be mixed, means for causing admixture of material from said bulk supply with said fresh charges, and means for withdrawing regulated quantities of the mixed end product from the bulk supply.

Landscapes

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

Description

Jan. 20, 1931. C, QVERBURY I 1,789,320 r APPARATUS FOR MIXING MATERIALS Original Filed bee. 7 1925 2 Sheets-Sheet 1 li /9 L Jan. 20, 1931. F. c. OVERBURY 1,789,320
I APPARATUS FOR MIXINGMATERIALS I Original Filed Dec. 7, 1925 2 Sheets-Sheet '2 Patented, Jan. 20, 1931 UNITED STATES FREDERICK C. OVERBURY; OF HILLSIDALE PATENT OFFICE NEW JERSEY, ASSIGNOR TO THE FLINT- APPARATUS FOR MIXING MATERIALS Application filed December 7, 1925, Serial No.'73,609.' Renewed January 16, 1980.
This invention relates to process and ap-* paratus for mixing materials, and refers more particularly to a process and apparatus 5 for producing emulsions. and mixtures there- -'5' of, and is more specifically directed to a device in which relatively large quantities of emulsion and mixtures thereof can be produced, with a high rate of production. The invention is also designed to accommodate a plurality of streams of material undergoing simultaneous emulsification. By dividing these streams instead of introducing a combined stream, better emulsification and finer dispersion will result. The apparatus is also designed to provide better means of controlling the temperatures than may be affected' with present types of apparatus.
The present application is in part an improvement on theprocess and apparatus described in co-pending application filed jointly in the name of Frederick C. Overbury and Lester Kirschbraun, Serial No. 343,392on December 9th, 1919.
Briefly, the improvements in the present invention comprise a plurality of open ended mixing or emulsifying conduits preferably equi-spaced from each other and supportedin an enlarged chamber in which a bulk supply of the end product is maintained. Agitating elements are mounted in the individual conduits, each conduit having separate inlets for the materials tote mixed or emulsi-n fied therein.
3 cross sectional view of the improved apparatus. Fig. 2 is a top plan view of Fig. 1, eliminating the gears and bearing support therefor, for the sake of clearness- Fig. 3 is a cross sectional side elevational view of a somewhat modified type of apparatus.
Referring more in detail to the drawings, 1 designates a main chamber or vessel for containing a bulk supply of the end product having aclosed base 2 and open to the atmosphere at its upper end. A plurality of open ended conduits are mounted within the vessel 1, their lower open ends being spaced away from the base 2 and supported by means of the supports 4, and their upper ends dis posed below the normal level ofthe bulk sup--' In the drawings, Fig. 1 is a diagrammatic terial' ply of end product in the container. There may be any number of these open ended conduits 3 preferably equi-spaced from each other. The conduits are preferably pro-" 'vided with jackets 5 for-the purpose of per- ".understood of course, that there may be any number of these propeller or agitator blades and that they may be spaced at varying dis tances from each other, although itis-pref erable to provide propeller'blades having an upward pitch: The'enlarged 'gear7 isadapted to mesh with thesmal-lpinion gears 9 t0 drive the propeller shafts '10. One of these propeller shafts 10 is mounted in each of the conduits 3 and-is also provided intermediate its lengthflwith propellergior agitator .7 blades 11.; 7 The container 1 is also provided with a jacket 12 for theintroduction of a cooling or' heating medium. The bearings 13 for the shafts6 and 10 may be supported on the bracket support. 14 mounted above the container'.
The particular form of drive shown, constitut'es' amechanical advantage over present t'vpes of e'quipment, in that the main driving 'sliaft 6 need not operate at as high a speed asjthe. auxiliary driving shafts 10, being regulated by the ratio between gears 7 and 9. The propellers 11 on the shafts 10 are so disposed and pitched as to force introduced 1 thereto downwardly through the conduits 3 and upwardly in the direction of the arrows into the space between the conduits 3 and the walls of the .container'l. The propeller blades 8 on the 95 other hand are pitched so as to cause an upward flow of the mixture between the conduits 3, particularly in the central section between said conduits. In this central s ace referred to, and disposed circumferentially the ma- I about the sha-ft fi'is placed a coil adapted quantities of the waterproofing material be introduced through the pipe through the pipe jacket 5 in the last conduit.
insulating the mass action. In order therefore, to assist this 15 and the jackets 5' to have circulated therethrough a heating or cooling medium in order to regulate and.
maintam a predetermined or efiicient operating temperature within the mass. An inlet pipe 16 communicates 5 for the purpose of introducing the heating or cooling medium, this particular jacket discharging said heating or cooling medium into the cooling coil 15, which cooling coil discharges said heating or cooling medium into another jacket 5, and from this jacket through the connectingpipes 17- into the The heating or cooling medium may then be withdrawn through the discharge pipe 18., It is understood of course, that the travel and circulation of the heating or cooling medium described, is purely diagrammatic, and that any other means of introducing said cooling or heating medium may be employed.
One of the objections to the present types of mixing and emulsifying equipment of the general character desciibed where a heavy pasty product is manufactured, is the difiiculty of maintaining a predetermined range of low temperatures where such low'temperatures .are required. A considerable amount of heat is generated in the present types of equipment due to friction of the propeller, and it becomes difiicult to absorb this heat partially for the reason that the pasty mass in flowing along the walls of the vessel 1. tends to deposit on said walls by the cooling action of thewall andth'ereby from further cooling cooling action, the coils and 12 are provided so that by the propulsive action of propellers 8 the mixed mass is caused to flow constantly between and about the coils 15.
. The mixer is provided with the drawofi 19 which may be provided with the knife valve or gate 20, and a plurality of pipes 21 and 22 1 are provided discharging into each oithe conduits 3, preferably two for each conother or others may be used merely as a secondary mixing device by refraining from introducmg any new materials to be emulsified.
with one of the jackets 'tus shown and described Also, the present invention contemplates the simultaneous emulsification of two or more difierent types of waterproofing material, for example, in one or more conduits, one type of waterproofing material such for instance, as asphalt, may be undergoing emulsification while simultaneously. in another or others, a different type of waterproofing materialsuch for instance, as a resinous pitch may be undergoing emulsification, so that *the finished product will have difierent constituents as its internal phase. It is also obvious that the differentconduits may be supplied with different types of emulsifying agent'such as different kinds of clay, bentonite or other colloid. The addition of va-- rious fillers, coloring agents and fibres may also be made by employing one or more of the conduits 3 for this purpose. while emulsification is taking place in an adjacent conduit or conduits. Y
Now briefly describing Fig. 3, the apparatus there described, is similar to theapparain Figs. 1 and 2, including as part ofthe mixing unit an additional mixing chamber23 in which rotates the driving shaft 24 provided with the propeller or agitator blades 25 and'having a sprocket 26 at its upper end, which sprocket is driven by means of the sprocket chain 27 meshin t with a similar sprocket 28 mounted on the hearing 4 of shaft 6. The mixed or emulsified mass will flow upwardly into the space 29 and eventually over the wall of the conduit 23. Fillers, pigments, fibres and other materials may be introduced to the conduit 23 through the inlet pipe 30, the intermediate mixture being agitated and thoroughly incorporated together by meansof the propeller blades 35 in this auxiliary conluo duit 23 and withdrawn through the outlet 19 controlled by valve 20.
By the use of the apparatus shown in Fig. 3, it is possible to roduce as a continuous operation, an emulsified mixture containing a filler or pigment, or the'like.
"no It 1s under-v stood of course, that I do not wish to-limit myself to the manufacture'of emulsions, as the process and apparatus may be advantageously employed for producing dispersions and emulsions of various types, and is also adapted for preparing many other products in which it becomes necessary to mix a plurality of ingredients at substantially the same time, or 1n substantially the same place. It will be apparent that by providing a plurality of small conduits 3, the invention lends itself not only to a simple emulsification and mixing, but further to additional admixtures with other materials, while undergoing emulsification. I
For example, in using the present invention for producing emulsion paints, one or more of the conduits 3 may be used to produce an emulsion, that is, such conduits may receive regulated quantities of colloid and paint base whilethei other conduits may receive regulated quantities of pigment in aqueous suspension.
The present invention is particularly directed to either continuous or batch operation.
The present invention utilizes one of the principles of the co-pending application referred to, namely that the mixing of fresh charges of material should take place in the presence of a bulk supply of previously formed end product, in order to produce the most satisfactory results.
I claim as my invention:
1. In an apparatus of the character described, the combination with an enlarged container for holding a bulk supply of end product, of a plurality of open ended conduits disposed in said container below the normal level of said bulk supply, agitating elements individual to each conduit, charging means communicating with each conduit for introducing materials to be mixed, means for efiecting passage of material from said bulk supply to said conduits, and means for withdrawing regulated quantities of the mixed end product from the bulk supply.
2..In an apparatus of the character described, the combination with a container for holding a bulk supply of the mixed end product, of a plurality of open ended conduits disposed in said container below the duits disposed in said container below the normal level of said bulk supply, inlets in-- dividual to each conduit for introducing fresh charges of materials to be mixed, agitator elements mounted in each conduit adapted to force the mass therein downwardly, separate agitating means positioned in the open central space between the conduits adapted to impart an upward movement to the bulk supply, and means for withdrawing regulated quantities of the mixed product, said separate agitating means being adapted to rotate at a relatively lower speed than the agitating elements in the conduits.
5. In an apparatus of the character described, the combination with an enlarged container for holding a bulk supply of end product, of a plurality of separated mixing zones disposed therein, charging means communicating with each separate mixing zone for introducing fresh charges of materials to be mixed, means for causing admixture of material from said bulk supply with said fresh charges, and means for withdrawing regulated quantities of the mixed end product from the bulk supply.
FREDERICK C. OVERBURY.
normal level of said bulk supply, agitating elements individual to each conduit, ch arging means communicating with each conduit for introducing materials to be mixed, means for transferring material from said bulk supply to said conduits, means for withdrawing regulated quantities of the mixed end product, and means for regulating the temperature of the bulk supply and th ma terials being mixed, including a closed conduit through which is passed a heating or cooling medium, positioned in the bulk supply.-, 1
3. In an apparatus for producmg dispersions, the combination with a container for holding a bulk supply of mixed end product, of a plurality of equi-spaced open ended conduits disposed in said container below the normal level of said bulk supply, in-
4. In an apparatus for producing dispersions, the combination with a container for 2 holding a bulk supply of mixed end product,
- of a plurality of equi-spaced open ended con-
US73609A 1925-12-07 1925-12-07 Apparatus for mixing materials Expired - Lifetime US1789320A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US73609A US1789320A (en) 1925-12-07 1925-12-07 Apparatus for mixing materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US73609A US1789320A (en) 1925-12-07 1925-12-07 Apparatus for mixing materials

Publications (1)

Publication Number Publication Date
US1789320A true US1789320A (en) 1931-01-20

Family

ID=22114719

Family Applications (1)

Application Number Title Priority Date Filing Date
US73609A Expired - Lifetime US1789320A (en) 1925-12-07 1925-12-07 Apparatus for mixing materials

Country Status (1)

Country Link
US (1) US1789320A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2429316A (en) * 1942-10-26 1947-10-21 Infilco Inc Process and apparatus for improving clarification of turbid liquids by use of partially thickened sludge
US2950171A (en) * 1955-06-07 1960-08-23 Union Chimique Belge Sa Process and apparatus for the manufacture of phosphoric acid
US3083538A (en) * 1958-10-06 1963-04-02 George E Gross Apparatus for maintaining a body of water free of ice
US4190617A (en) * 1978-08-07 1980-02-26 Hope Henry F Mixing pump system
US4415267A (en) * 1982-06-03 1983-11-15 Hill Francis K Apparatus for mixing and application of paving compositions
US4515482A (en) * 1983-08-11 1985-05-07 The Upjohn Company Sterile suspension and solution holding and mixing tank
WO1995013512A1 (en) * 1993-11-12 1995-05-18 Edwin Eisenegger Process for the thermal treatment of a pourable solid material, a mixing device for carrying this out and a material produced by this process
US6641296B1 (en) * 1997-04-24 2003-11-04 Jean-Luc Jouvin Method for mixing alginate using a rotatable elliptical bowl

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2429316A (en) * 1942-10-26 1947-10-21 Infilco Inc Process and apparatus for improving clarification of turbid liquids by use of partially thickened sludge
US2950171A (en) * 1955-06-07 1960-08-23 Union Chimique Belge Sa Process and apparatus for the manufacture of phosphoric acid
US3083538A (en) * 1958-10-06 1963-04-02 George E Gross Apparatus for maintaining a body of water free of ice
US4190617A (en) * 1978-08-07 1980-02-26 Hope Henry F Mixing pump system
US4415267A (en) * 1982-06-03 1983-11-15 Hill Francis K Apparatus for mixing and application of paving compositions
US4515482A (en) * 1983-08-11 1985-05-07 The Upjohn Company Sterile suspension and solution holding and mixing tank
WO1995013512A1 (en) * 1993-11-12 1995-05-18 Edwin Eisenegger Process for the thermal treatment of a pourable solid material, a mixing device for carrying this out and a material produced by this process
US6641296B1 (en) * 1997-04-24 2003-11-04 Jean-Luc Jouvin Method for mixing alginate using a rotatable elliptical bowl

Similar Documents

Publication Publication Date Title
US1911644A (en) overbury
US2249263A (en) Apparatus for treating oils
US1789320A (en) Apparatus for mixing materials
US1351352A (en) Emulsifier
US1297171A (en) Apparatus for the treatment of one liquid with another.
US3925243A (en) Apparatus for the manufacture of emulsions
US2115408A (en) Apparatus for the manufacture of colored glass
US1836754A (en) Apparatus for preparing paving compositions
US2628080A (en) Jacketed conical blender
US2348473A (en) Method of treating chocolate and similar materials
US3108060A (en) Loop reactor and process for sulfonating asphalt
US1988766A (en) Process and apparatus for producing asphalt
US1603546A (en) Apparatus for making emulsions
US2019112A (en) Process for fusing materials
US2077226A (en) Mixer
US1790967A (en) auerbach
US2079565A (en) Machine for mixing plastic material
US1701164A (en) Mixing apparatus and process
US1166139A (en) Mixing apparatus.
US2217182A (en) Apparatus for and method of circulating molten glass in a feeding container
US1935190A (en) Process and apparatus for mixing gases with liquids
US765975A (en) Apparatus for the preparation of tar macadam.
US1774205A (en) Process and apparatus for producing dispersions
US1809672A (en) Apparatus for mixing liquids
US1309175A (en) Beating and aerating process and apparatus