US2292897A - Method and apparatus for mixing - Google Patents
Method and apparatus for mixing Download PDFInfo
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- US2292897A US2292897A US374833A US37483341A US2292897A US 2292897 A US2292897 A US 2292897A US 374833 A US374833 A US 374833A US 37483341 A US37483341 A US 37483341A US 2292897 A US2292897 A US 2292897A
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- air
- materials
- nozzles
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- propeller
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/402—Mixers using gas or liquid agitation, e.g. with air supply tubes comprising supplementary stirring elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/40—Mixers using gas or liquid agitation, e.g. with air supply tubes
- B01F33/406—Mixers using gas or liquid agitation, e.g. with air supply tubes in receptacles with gas supply only at the bottom
Definitions
- This invention relates to the mixing and blending of finely divided pulverulent materials, such as ground cement raw materials, cement, and the like. More particularly, the invention is concerned with a novel method by which-such materials may be mixed and blended. for the purpose of rendering and maintaining them homogeneous and an apparatus by which the method may be advantageously practised.
- Finely divided pulverulent materials must frequently be mixed and blended, as, for example,
- the present invention is directed to the provision of a method for mixing and blending pul vverulent materials which overcomes the disadvantages of the methods heretofore-used, and it involves introduction of air into the materials in an amount sufiicient to render them fluent and the formation and maintenance of circulating currents within a body of the materials insuch fluent condition. dered fluent in a preliminary operation and the circulating currents then set up within a body of the materials or, if desired, the-devices for introducing the air and for setting up and main-
- the materials may be renintroduced into the body of materials therein and, preferably, the nozzles are supplied with air by control means operable to change the points of air introduction, as desired.
- the propellers set up circulating currents within the body of materials in the container and by changing the points of air introduction and altering the direction of rotation of the propellers, the paths of the currents may be changed so that a thorough mixing and blending of thecontents of the container are obtained.
- Fig. 1 is a vertical section throughone form of apparatus by which the new method may be practised;
- Fig. 2 is a sectional view on the line 22 of is Fig. 3 is a fragmentary vertical sectional view of a modified construction
- Fig. 4 is a sectional view on the line 4-4 of v Fig. 5 is a sectional view through one form of air nozzle that may be employed;
- Figs. 6 to 10, inclusive are diagrammatic vertical sectional views showing difierent arrangements of the propellers and air nozzles that may be employed;
- Figs. 11 and 12 are vertical sectional views of different forms of apparatus constituting modifications'of that illustrated in Fig. 1.
- taining the currents may be started simultaneously.
- the introduction of air may be discontinued after the materials have reached the fluent conditioner the introduction of air may be continued for the purpose of setting up and maintaining additional currents.
- the method may be employed either to mix materials or'to maintain already mixed materials in homogeneous condition and the mixing operation may, if desired, be carried on during the charging and discharging of the container.
- the new method may be advantageously practised by means of an apparatus which includes a container, such as a silo, which is provided with one or more propellers mounted for rotation within the container in contact with the material therein and driven by means capable of revers-' ing the direction of rotation of the propellers.
- the container is also provided with a plurality
- the apparatus illustrated in Fig. 1 comprises a. silo having a cylindrical wall 20 and a conical bottom 2.! provided with a discharge outlet 22.
- the silo is provided with a suitable inlet opening (not shown) and extending through the top wall 23 thereof is a shaft 24 mounted in bearings in a frame 25.
- the shaft is driven in any suitable way, as by means of a gear wheel 26, and at its lower end, carries a propeller 21.. lying within the body of materials 28 within the silo.
- Extending through the bottom of the silo are air pipes 29 leading to nozzles 30 and, in the construction shown, there are four circular sets of nozzles, with the nozzles of the difierent sets lying in different levels.
- the pipes 29 of the nozzles of each set are connected by circular supply pipes 3
- the line 32 leads to the circular pipes for the innermost set of nozzles and the'second set outwardly therefrom, while the pipe 33 supplies the second and fourth circular pipes starting from the center.
- the lines 32, 33 are provided with control valves 34, 34a and beyond the con- I. and, at the same time, the propeller is started.
- air nozzles 55' are mounted in sets to introduce air at the bottom of the container 56 and propellers 51 and 66 are mounted to rotate on horizontal axes within the body of material in the container.
- Propeller 5'! lies near the bottom of the container and propeller 63 at a higher level.
- a circulating current may be set up along the path indicated by the arrows and by reversing the direction of rotation of the propellers and supplying air to sets of nozzles alternately, thedirection of flow and the paths of the outward from the center are active.
- valve 340 is closed and valve 34 is opened. Thereafter, upwardly flowing currents are established in the body of materials in line with the nozzles of the first and third sets outward from the center, the material flowing upward along such paths being caused to flow down through the center of the body by the propeller.
- a variation in current flow may also be obtained by reversing the direction of rotation of the propeller and in practise, the direction of ro-'- tation of the propeller is periodically changed and the valves 34, 34a are alternately opened and closed.
- the valves may be replaced by an automatic air distributor which periodically changes the flow from one air supply line to the other.
- the silo has a flat bottom 39 through which pass pipes 40 terminating in nozzles 4
- the nozzles are arranged in sets 42a, 42b, 42c, 42d, each set occupy ng a quadrant, and the nozzles in the several sets are supplied through lines 43 leading to a distributor 44 supplied by compressed air by a compressor 45, an oil and water separator 46 being interposed in the supply line between the compressor and distributor.
- the distributor operates to supply air to the sets of nozzles in different ways, as, for example, air may be supplied firstto the sets 42a and 42b and thereafter to the sets 42c and 42d, or, if desired,
- the sets 42a and 420 may be supplied at the same time, after which, the nozzles in the sets 42b and 42d become active.
- a shaft 41 mounted in bearings on a bracket 46 attached to the wall of the silo, extends through the wall of the silo and carries a propeller 49 on its inner end. Outside the silo, the shaft is provided with a gear wheel 50 by which it may be driven and, during the operation of the apparatus, the propeller is rotated, first in one direction and then the other, and air is supplied to the sets of nozzles in alternation so that circulating currents within the body of materials are set up and the direction of the currents and their paths are varied from time to time.
- the nozzles employed in the various forms of apparatus are preferably so constructed that the air enters the material in a state of fine division and one type of nozzle suitable for the purpose is illustrated in Fig. 5.
- the nozzle comprises a pair of metal plates 5
- a plurality of propellers 62 are mounted on a horizontal shaft 63 near the bottom of the container and other propellers 64, 65 are mounted for r0- tation on horizontal axes at diflerent levels upward therefrom.
- the variations in the circulating flow may be obtained by varying the action of the propellers and altering the points of introduction of the air.
- the apparatus is similar to that illustrated in Fig. 1, except that the propeller 68 is mounted in a shaft 69 which is movable vertically so that the position of the propeller within the body of materials may be changed as desired.
- the apparatus includes a container consisting of a container body 10 and a pipe system.
- the container body has a conical bottom provided with sets of air nozzles II to which air may be supplied in difierent ways as described above.
- the body has an opening at the top and a pipe 12 extends down into the body of materials through the opening.
- a pipe 13 Leading upward from the opening is a pipe 13 connected by pipes 14 which lead to openings in the side wall of the body at difl'erent levels.
- Within the pipe 13 is a propeller I5 and by the action of the propeller and of the air injected through the nozzle ll, material may be drawn upward through the pipes. l2, 13 from the interior of the body and returned thereto at different points through the pipes".
- the container body 16 has a conical bottom on which are mounted air nozzles".
- the top of the body has an opening through which extends a pipe "containing a propeller 19.
- Within the body are vertical pipes so starting at different levels with an annular strip of fllm or similar porous 7 and leading upward to a casing 8
- the upper end of pipe is then connected by pipes 82 which discharge through openings in the container body top.
- the propeller assisted by air injected through the nozzles 11, causes an upward flow oi the material through the pipes 88 and the material passes through casing 8
- the propeller may be reversed so that materials flow upwardly through the pipes 82 and return through the pipes 88.
- the mixing and blending of the material are eflected economically, since only small quantities of air are needed and the propulsion of the fluid-like aerated material-does not involve large power consumption.
- the material in contact with the materials and effective to produce circulating'currents within the body, a plurality of concentric sets of nozzles in the lower portion of the container for introducing air into the body of materials therein, and means for supplying air to each set of nozzles, each 01' said air-supplying means being independently controlled.
- a method of mixing dry pulverulent mate- 'in, aerated condition and capable of flowing means being independently rials which comprises aerating the materials to render them fluent by introducing air into a body of thematerials' at a number of points distributed throughout the area 01! the lower portion of the body of materials, mechanically and pneumati- Y cally propelling the aerated and fluent materials, the mechanical propelling force being applied in a direction and at such point or points as to maintain circulating currents of the aerated ma- .terials within the body thereof, and periodically altering the paths of said circulating currents by changing the direction in which the mechanical and pneumatic propelling forces act: upon the materials.
- Apparatus for mixing pulverulent materials which comprises a container for a body of the materials, a shaft mounted for rotation within the container, a propeller mounted-on the shaft within the container and adapted to rotate in contact with the materials and being effective to produce circulating currents within the body, a mounting for ,the shaft permitting it to be moved longitudinally so that the position of the propeller within the container may be varied, a plurality of concentric sets of nozzles in the lower portion of the container for introducing air into the body of materials therein, and means for 1 supplying air to each set of nozzles, each of said air-supplying means being independently controlled.
- Apparatus for mixing pulverulent materials in. aerated condition and capable of flowing which comprises a container for a body-of the materials, a propeller within the container rotating in contact with the materials and effective to produce circulating currents within the body, a plurality of sets of nozzles in the lower portion of the container for introducing air into the body of materials therein, and means for supplying air to each set of nozzles, each of said air-supplying controlled.
Description
Aug. 11', 1942. v N. NIELSEN 2,292,897
METHOD AND APPARATUS FOR MIXING Filed Jan. 17, 1941 2 Sheets-Sheet 1 NVENTOR ATTORNEY)" Aug-11,1942 N. NIELSEN 2,292,897
METHOD AND APPARATUS FOR MIXING Filed Jan. 17, 1941 2 Sheets-Sheet 2 ATTORN EYf Patented Aug. 11, 1942 METHOD APPARATUS FOR MIXING Niels Nielsen, Copenhagen, Denmark, asslgnor to F. 1;. Smidth & Co., New York, N. Y., a corporation of New Jersey Application January 17, 1941, Serial No. 374,833
In Great Britain February 13, 1940 4 Claims.
This invention relates to the mixing and blending of finely divided pulverulent materials, such as ground cement raw materials, cement, and the like. More particularly, the invention is concerned with a novel method by which-such materials may be mixed and blended. for the purpose of rendering and maintaining them homogeneous and an apparatus by which the method may be advantageously practised.
Finely divided pulverulent materials must frequently be mixed and blended, as, for example,
. in the preparation of a mixture of ground cement raw materials suitable for burning into clinker. Heretofore such materials have been mixed either pneumatically or mechanically and both methods are objectionable. If the mixing is carried on entirely by aeration of the materials,-
the large quantities of air required make the process uneconomical, while if the operation is carried on mechanically, as by means of agitating devices, the necessary apparatus is so large as to be expensive and complicated.
The present invention is directed to the provision of a method for mixing and blending pul vverulent materials which overcomes the disadvantages of the methods heretofore-used, and it involves introduction of air into the materials in an amount sufiicient to render them fluent and the formation and maintenance of circulating currents within a body of the materials insuch fluent condition. dered fluent in a preliminary operation and the circulating currents then set up within a body of the materials or, if desired, the-devices for introducing the air and for setting up and main- The materials may be renintroduced into the body of materials therein and, preferably, the nozzles are supplied with air by control means operable to change the points of air introduction, as desired. The propellers set up circulating currents within the body of materials in the container and by changing the points of air introduction and altering the direction of rotation of the propellers, the paths of the currents may be changed so that a thorough mixing and blending of thecontents of the container are obtained.
For a better understanding of the invention,
reference may be had to the accompanying drawings, in which Fig. 1 is a vertical section throughone form of apparatus by which the new method may be practised;
Fig. 2 is a sectional view on the line 22 of is Fig. 3 is a fragmentary vertical sectional view of a modified construction;
Fig. 4 is a sectional view on the line 4-4 of v Fig. 5 is a sectional view through one form of air nozzle that may be employed;
Figs. 6 to 10, inclusive, are diagrammatic vertical sectional views showing difierent arrangements of the propellers and air nozzles that may be employed; and
Figs. 11 and 12 are vertical sectional views of different forms of apparatus constituting modifications'of that illustrated in Fig. 1.
taining the currents may be started simultaneously. In either case, the introduction of air may be discontinued after the materials have reached the fluent conditioner the introduction of air may be continued for the purpose of setting up and maintaining additional currents. The method may be employed either to mix materials or'to maintain already mixed materials in homogeneous condition and the mixing operation may, if desired, be carried on during the charging and discharging of the container.
The new method may be advantageously practised by means of an apparatus which includes a container, such as a silo, which is provided with one or more propellers mounted for rotation within the container in contact with the material therein and driven by means capable of revers-' ing the direction of rotation of the propellers. The container is also provided with a plurality The apparatus illustrated in Fig. 1 comprises a. silo having a cylindrical wall 20 and a conical bottom 2.! provided with a discharge outlet 22. The silo is provided with a suitable inlet opening (not shown) and extending through the top wall 23 thereof is a shaft 24 mounted in bearings in a frame 25. The shaft is driven in any suitable way, as by means of a gear wheel 26, and at its lower end, carries a propeller 21.. lying within the body of materials 28 within the silo.
Extending through the bottom of the silo are air pipes 29 leading to nozzles 30 and, in the construction shown, there are four circular sets of nozzles, with the nozzles of the difierent sets lying in different levels. The pipes 29 of the nozzles of each set are connected by circular supply pipes 3| supplied with air by lines 32 and 33. The line 32 leads to the circular pipes for the innermost set of nozzles and the'second set outwardly therefrom, while the pipe 33 supplies the second and fourth circular pipes starting from the center. The lines 32, 33 are provided with control valves 34, 34a and beyond the con- I. and, at the same time, the propeller is started.
The introduction of air through all of the nozzles continues until the material reaches the desired fluent condition and, thereafter, one of the control valves is 'shut and air flows through only two the sets of nozzles. As illustrated in Fig. 1, air is being introduced through the line 33 so that the nozzles in the second and fourth sets material 63 clamped between the plates alon their periphery. The plate 6| has a central opening 54 and air is supplied through the opening to the space between the plates, whence it escapes through the felt.
In the apparatus illustrated in Fig. 6, air nozzles 55' are mounted in sets to introduce air at the bottom of the container 56 and propellers 51 and 66 are mounted to rotate on horizontal axes within the body of material in the container. Propeller 5'! lies near the bottom of the container and propeller 63 at a higher level. With this arrangement, a circulating current may be set up along the path indicated by the arrows and by reversing the direction of rotation of the propellers and supplying air to sets of nozzles alternately, thedirection of flow and the paths of the outward from the center are active. The introduction of air through these nozzles, together with the action of the propeller, causes the formation of currents within the body of material, as indicated by the arrows, and after such currents have been established and maintained for a suitable period, valve 340 is closed and valve 34 is opened. Thereafter, upwardly flowing currents are established in the body of materials in line with the nozzles of the first and third sets outward from the center, the material flowing upward along such paths being caused to flow down through the center of the body by the propeller. A variation in current flow may also be obtained by reversing the direction of rotation of the propeller and in practise, the direction of ro-'- tation of the propeller is periodically changed and the valves 34, 34a are alternately opened and closed. If desired, the valves may be replaced by an automatic air distributor which periodically changes the flow from one air supply line to the other.
In the construction illustrated in Figs. 3 and 4, the silo has a flat bottom 39 through which pass pipes 40 terminating in nozzles 4|. The nozzles are arranged in sets 42a, 42b, 42c, 42d, each set occupy ng a quadrant, and the nozzles in the several sets are supplied through lines 43 leading to a distributor 44 supplied by compressed air by a compressor 45, an oil and water separator 46 being interposed in the supply line between the compressor and distributor. The distributor operates to supply air to the sets of nozzles in different ways, as, for example, air may be supplied firstto the sets 42a and 42b and thereafter to the sets 42c and 42d, or, if desired,
' the sets 42a and 420 may be supplied at the same time, after which, the nozzles in the sets 42b and 42d become active.
A shaft 41, mounted in bearings on a bracket 46 attached to the wall of the silo, extends through the wall of the silo and carries a propeller 49 on its inner end. Outside the silo, the shaft is provided with a gear wheel 50 by which it may be driven and, during the operation of the apparatus, the propeller is rotated, first in one direction and then the other, and air is supplied to the sets of nozzles in alternation so that circulating currents within the body of materials are set up and the direction of the currents and their paths are varied from time to time.
The nozzles employed in the various forms of apparatus are preferably so constructed that the air enters the material in a state of fine division and one type of nozzle suitable for the purpose is illustrated in Fig. 5. The nozzle comprises a pair of metal plates 5| and 52 bolted together .the materials may be circulated along diflerent paths within the body in the container by changing the direction of rotation of the propellers, the angular position of shaft 6|, and the points of introduction of the air.
In the construction shown in Fig. 8, a plurality of propellers 62 are mounted on a horizontal shaft 63 near the bottom of the container and other propellers 64, 65 are mounted for r0- tation on horizontal axes at diflerent levels upward therefrom. Here again, the variations in the circulating flow may be obtained by varying the action of the propellers and altering the points of introduction of the air.
In the construction shown in Fig. 9, there are four propellers 66 rotating on horizontal axes and lying on the vertical center line of the container, one above the other. Between the propellers, bailles 6'1 are provided to control the path of the circulating currents.
In the construction shown in Fig. .10, the apparatus is similar to that illustrated in Fig. 1, except that the propeller 68 is mounted in a shaft 69 which is movable vertically so that the position of the propeller within the body of materials may be changed as desired.
In the Fig. 11 construction, the apparatus includes a container consisting of a container body 10 and a pipe system. The container body has a conical bottom provided with sets of air nozzles II to which air may be supplied in difierent ways as described above. The body has an opening at the top and a pipe 12 extends down into the body of materials through the opening. Leading upward from the opening is a pipe 13 connected by pipes 14 which lead to openings in the side wall of the body at difl'erent levels. Within the pipe 13 is a propeller I5 and by the action of the propeller and of the air injected through the nozzle ll, material may be drawn upward through the pipes. l2, 13 from the interior of the body and returned thereto at different points through the pipes".
In the construction shown in Fig. 12, the container body 16 has a conical bottom on which are mounted air nozzles". The top of the body has an opening through which extends a pipe "containing a propeller 19. Within the body are vertical pipes so starting at different levels with an annular strip of fllm or similar porous 7 and leading upward to a casing 8| from which the pipe I8 leads. The upper end of pipe "is then connected by pipes 82 which discharge through openings in the container body top.
With'this arrangement, the propeller, assisted by air injected through the nozzles 11, causes an upward flow oi the material through the pipes 88 and the material passes through casing 8|, pipe I8, and pipes 82 to be returned to the top of the body of materials within the container. By varying the supply of air to the nozzle, variations inthe flow of material in the circulating streams may be, effected ,and by extending pipes 82 down through the top oi the container and into the body of material therein, the propeller may be reversed so that materials flow upwardly through the pipes 82 and return through the pipes 88.
With all of the constructions illustrated, the mixing and blending of the material are eflected economically, since only small quantities of air are needed and the propulsion of the fluid-like aerated material-does not involve large power consumption. In some instances, the material in contact with the materials and effective to produce circulating'currents within the body, a plurality of concentric sets of nozzles in the lower portion of the container for introducing air into the body of materials therein, and means for supplying air to each set of nozzles, each 01' said air-supplying means being independently controlled.
2. A method of mixing dry pulverulent mate- 'in, aerated condition and capable of flowing means being independently rials which comprises aerating the materials to render them fluent by introducing air into a body of thematerials' at a number of points distributed throughout the area 01! the lower portion of the body of materials, mechanically and pneumati- Y cally propelling the aerated and fluent materials, the mechanical propelling force being applied in a direction and at such point or points as to maintain circulating currents of the aerated ma- .terials within the body thereof, and periodically altering the paths of said circulating currents by changing the direction in which the mechanical and pneumatic propelling forces act: upon the materials.
3. Apparatus for mixing pulverulent materials which comprises a container for a body of the materials, a shaft mounted for rotation within the container, a propeller mounted-on the shaft within the container and adapted to rotate in contact with the materials and being effective to produce circulating currents within the body, a mounting for ,the shaft permitting it to be moved longitudinally so that the position of the propeller within the container may be varied, a plurality of concentric sets of nozzles in the lower portion of the container for introducing air into the body of materials therein, and means for 1 supplying air to each set of nozzles, each of said air-supplying means being independently controlled.
4. Apparatus for mixing pulverulent materials in. aerated condition and capable of flowing which comprises a container for a body-of the materials, a propeller within the container rotating in contact with the materials and effective to produce circulating currents within the body, a plurality of sets of nozzles in the lower portion of the container for introducing air into the body of materials therein, and means for supplying air to each set of nozzles, each of said air-supplying controlled.
NIELS NIELSEN.
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GB2292897X | 1940-02-13 |
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US2292897A true US2292897A (en) | 1942-08-11 |
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US374833A Expired - Lifetime US2292897A (en) | 1940-02-13 | 1941-01-17 | Method and apparatus for mixing |
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Cited By (62)
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US2419097A (en) * | 1944-05-22 | 1947-04-15 | Stratford Dev Corp | Process for catalytically reacting gaseous material |
US2429701A (en) * | 1945-07-05 | 1947-10-28 | Paul E Sippel | Mixing machine |
US2478707A (en) * | 1944-07-25 | 1949-08-09 | Standard Oil Dev Co | Catalytic reactor |
US2502778A (en) * | 1946-07-31 | 1950-04-04 | Reliable Plastics Company Ltd | Apparatus for homogeneously combining finely divided substances |
US2532224A (en) * | 1949-02-03 | 1950-11-28 | Reliable Plastics Company Ltd | Apparatus for combining finely divided substances |
US2539288A (en) * | 1947-05-27 | 1951-01-23 | Forest B Van Horn | Spraying apparatus with adjustable booms |
US2609185A (en) * | 1949-07-04 | 1952-09-02 | F S Smidth & Co | Method and apparatus for increasing fluidity of material |
US2631969A (en) * | 1949-02-08 | 1953-03-17 | Standard Oil Co | Mineral oil treating system |
US2665035A (en) * | 1948-12-27 | 1954-01-05 | Huron Portland Cement Company | Aerating device for pulverulent material |
US2706910A (en) * | 1952-01-15 | 1955-04-26 | Henry A Sinski | Determination of the filling power of fluffy bodies |
US2797530A (en) * | 1954-08-17 | 1957-07-02 | Pangborn Corp | Sluriator |
US2806298A (en) * | 1951-07-17 | 1957-09-17 | Rossi Giovanni | Process and device for the treatment of substances in small pieces, by means of a fluid |
DE1027966B (en) * | 1953-07-29 | 1958-04-10 | Peters Ag Claudius | Process for mixing and homogenizing dry powdery substances, partly pneumatically |
US2837319A (en) * | 1954-07-30 | 1958-06-03 | Mcbean Res Corp | Sauerkraut processing apparatus |
US2844361A (en) * | 1955-06-28 | 1958-07-22 | Fuller Co | Method and apparatus for blending pulverulent material |
DE1057425B (en) * | 1953-09-17 | 1959-05-14 | Moeller Johannes | Method and device for the pneumatic mixing of powdery material stored in silos |
DE1057856B (en) * | 1954-12-07 | 1959-05-21 | Kloeckner Humboldt Deutz Ag | Pneumatic mixer for powdery or fine-grained goods |
DE1076089B (en) * | 1953-09-24 | 1960-02-25 | Stamicarbon | Process for generating the state of suspension in a mass of coarse material with simultaneous generation of systematic circulation currents in the suspended mass |
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DE1124330B (en) * | 1955-01-15 | 1962-02-22 | Klinger K G | Method and device for mixing and homogenizing dusty or flour-like material |
US3024500A (en) * | 1960-03-28 | 1962-03-13 | David E Lawson | Apparatus for dry mixing of material |
US3053642A (en) * | 1958-08-05 | 1962-09-11 | Exxon Research Engineering Co | Distributing gas to fluidized beds |
US3073070A (en) * | 1960-10-12 | 1963-01-15 | William H Mead | Abrasive blasting system |
US3073576A (en) * | 1959-05-16 | 1963-01-15 | Kloeckner Humboldt Deutz Ag | Pneumatic mixer for pulverulent or fine-granular material |
US3106385A (en) * | 1960-04-26 | 1963-10-08 | Du Pont | Method and apparatus for solids blending |
US3117027A (en) * | 1960-01-08 | 1964-01-07 | Wisconsin Alumni Res Found | Apparatus for coating particles in a fluidized bed |
DE1163781B (en) * | 1957-10-16 | 1964-02-27 | Drahomir Sokol | Fluidized bed reactor |
US3148865A (en) * | 1960-11-02 | 1964-09-15 | Gouverneur Talc Company Inc | Pneumatic conveying and conditioning method and apparatus |
US3167454A (en) * | 1959-12-24 | 1965-01-26 | Zenith Radio Corp | Fluidized-bed type of coating apparatus |
US3204942A (en) * | 1963-02-18 | 1965-09-07 | Babcock & Wilcox Co | Distributor for pneumatically transported particle-form material |
US3233584A (en) * | 1958-07-18 | 1966-02-08 | Polymer Corp | Coating process and apparatus |
DE1218911B (en) * | 1956-06-15 | 1966-06-08 | Telegraph Construction And Mai | Method and apparatus for dip coating an article by fluidized bed sintering |
US3328894A (en) * | 1965-01-15 | 1967-07-04 | Hupp Corp | Coffee roasting apparatus |
US3329506A (en) * | 1966-01-24 | 1967-07-04 | Hupp Corp | Method for roasting coffee and similar particulate solids |
US3345181A (en) * | 1966-01-24 | 1967-10-03 | Hupp Corp | Method for roasting coffee beans and similar particulate solids |
US3345180A (en) * | 1965-01-15 | 1967-10-03 | Hupp Corp | Coffee roasting method |
US3364053A (en) * | 1963-10-12 | 1968-01-16 | Polymer Corp | Method of coating articles |
US3371425A (en) * | 1964-06-23 | 1968-03-05 | Vickers Zimmer Ag | Apparatus for reducing the sojourn times in fluidized beds |
US3394468A (en) * | 1965-06-14 | 1968-07-30 | Glatt Werner | Container for the reception of a pulverulent or granular feed for treatment in a hot air dryer |
US3518777A (en) * | 1968-01-29 | 1970-07-07 | Motomi Kono | Heat exchange apparatus for fluidizing particulate material |
US3653639A (en) * | 1971-02-04 | 1972-04-04 | Whirl Air Flow Corp | High pressure air and liquid blending method and apparatus for discrete materials |
US3656717A (en) * | 1969-08-28 | 1972-04-18 | Polysius Ag | Process and apparatus for the continuous pneumatic treatment of fine material |
US3671018A (en) * | 1970-11-19 | 1972-06-20 | Union Carbide Corp | Bubble-blending particulate solids |
US3773297A (en) * | 1969-09-18 | 1973-11-20 | Portec Inc | Device for fluidizing stored material |
US3945615A (en) * | 1972-10-19 | 1976-03-23 | A. Ahlstrom Osakeyhtio | Continuous method and device for withdrawing particulate material from a container |
US3953003A (en) * | 1974-06-06 | 1976-04-27 | Aluterv Aluminiumipari Tervezo Vallalat | Tank provided with pneumatic mixing pipe |
US3957448A (en) * | 1974-12-16 | 1976-05-18 | Standard Oil Company | Divided horizontal reactor for the vapor phase polymerization of monomers at different hydrogen levels |
US3965083A (en) * | 1974-12-16 | 1976-06-22 | Standard Oil Company | Process for the vapor phase polymerization of monomers in a horizontal, quench-cooled, stirred-bed reactor using essentially total off-gas recycle and melt finishing |
US3971768A (en) * | 1974-12-16 | 1976-07-27 | Standard Oil Company (Indiana) | Vapor phase reactor off-gas recycle system for use in the vapor state polymerization of monomers |
US3999750A (en) * | 1975-12-08 | 1976-12-28 | Perkins Willis E | Artificial snowfall producing apparatus |
US4129701A (en) * | 1974-12-16 | 1978-12-12 | Standard Oil Company (Indiana) | Horizontal reactor for the vapor phase polymerization of monomers |
US4491549A (en) * | 1981-08-22 | 1985-01-01 | Hoechst Aktiengesellschaft | Device for dispersing a second phase in a first phase |
US4494932A (en) * | 1983-02-18 | 1985-01-22 | Cooper Lasersonics, Inc. | Dental cleaning apparatus and method |
US5632100A (en) * | 1993-11-17 | 1997-05-27 | Niro Holding A/S | Process and a spray drying apparatus for producing an agglomerated powder |
US5961000A (en) * | 1996-11-14 | 1999-10-05 | Sanfilippo; James J. | System and method for filling and sealing containers in controlled environments |
US6148540A (en) * | 1995-12-30 | 2000-11-21 | Nara Machinery Co., Ltd. | Pulverized body drying method and apparatus |
US20060067160A1 (en) * | 2004-09-30 | 2006-03-30 | Koetas Joseph P | Apparatus for forming a polishing pad having a reduced striations |
US20110017786A1 (en) * | 2008-03-17 | 2011-01-27 | Uhde Gmbh | Method and device for metered removal of a fine-grained to coarse-grained solid material or solid material mixture from a storage container |
CN106390651A (en) * | 2016-06-08 | 2017-02-15 | 福建铁拓机械有限公司 | Integrated tail gas and waste powder treating apparatus of complete set of equipment for regeneration and stirring of asphalt |
KR20200002988A (en) | 2017-06-12 | 2020-01-08 | 미츠비시 히타치 파워 시스템즈 가부시키가이샤 | Axial flow rolling machine |
RU214406U1 (en) * | 2022-07-15 | 2022-10-26 | Общество с ограниченной ответственностью "Плазмохимические технологии" | Device for mixing and homogenizing single-walled carbon nanotubes |
-
1941
- 1941-01-17 US US374833A patent/US2292897A/en not_active Expired - Lifetime
Cited By (64)
Publication number | Priority date | Publication date | Assignee | Title |
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US2419097A (en) * | 1944-05-22 | 1947-04-15 | Stratford Dev Corp | Process for catalytically reacting gaseous material |
US2478707A (en) * | 1944-07-25 | 1949-08-09 | Standard Oil Dev Co | Catalytic reactor |
US2429701A (en) * | 1945-07-05 | 1947-10-28 | Paul E Sippel | Mixing machine |
US2502778A (en) * | 1946-07-31 | 1950-04-04 | Reliable Plastics Company Ltd | Apparatus for homogeneously combining finely divided substances |
US2539288A (en) * | 1947-05-27 | 1951-01-23 | Forest B Van Horn | Spraying apparatus with adjustable booms |
US2665035A (en) * | 1948-12-27 | 1954-01-05 | Huron Portland Cement Company | Aerating device for pulverulent material |
US2532224A (en) * | 1949-02-03 | 1950-11-28 | Reliable Plastics Company Ltd | Apparatus for combining finely divided substances |
US2631969A (en) * | 1949-02-08 | 1953-03-17 | Standard Oil Co | Mineral oil treating system |
US2609185A (en) * | 1949-07-04 | 1952-09-02 | F S Smidth & Co | Method and apparatus for increasing fluidity of material |
US2806298A (en) * | 1951-07-17 | 1957-09-17 | Rossi Giovanni | Process and device for the treatment of substances in small pieces, by means of a fluid |
US2706910A (en) * | 1952-01-15 | 1955-04-26 | Henry A Sinski | Determination of the filling power of fluffy bodies |
DE1027966B (en) * | 1953-07-29 | 1958-04-10 | Peters Ag Claudius | Process for mixing and homogenizing dry powdery substances, partly pneumatically |
DE1057425B (en) * | 1953-09-17 | 1959-05-14 | Moeller Johannes | Method and device for the pneumatic mixing of powdery material stored in silos |
DE1076089B (en) * | 1953-09-24 | 1960-02-25 | Stamicarbon | Process for generating the state of suspension in a mass of coarse material with simultaneous generation of systematic circulation currents in the suspended mass |
US2837319A (en) * | 1954-07-30 | 1958-06-03 | Mcbean Res Corp | Sauerkraut processing apparatus |
US2797530A (en) * | 1954-08-17 | 1957-07-02 | Pangborn Corp | Sluriator |
DE1057856B (en) * | 1954-12-07 | 1959-05-21 | Kloeckner Humboldt Deutz Ag | Pneumatic mixer for powdery or fine-grained goods |
DE1124330B (en) * | 1955-01-15 | 1962-02-22 | Klinger K G | Method and device for mixing and homogenizing dusty or flour-like material |
US2844361A (en) * | 1955-06-28 | 1958-07-22 | Fuller Co | Method and apparatus for blending pulverulent material |
DE1218911B (en) * | 1956-06-15 | 1966-06-08 | Telegraph Construction And Mai | Method and apparatus for dip coating an article by fluidized bed sintering |
DE1095637B (en) * | 1956-06-25 | 1960-12-22 | Polysius Gmbh | Mixing device |
DE1163781B (en) * | 1957-10-16 | 1964-02-27 | Drahomir Sokol | Fluidized bed reactor |
US3233584A (en) * | 1958-07-18 | 1966-02-08 | Polymer Corp | Coating process and apparatus |
US3053642A (en) * | 1958-08-05 | 1962-09-11 | Exxon Research Engineering Co | Distributing gas to fluidized beds |
US2964299A (en) * | 1959-02-10 | 1960-12-13 | Ici Ltd | Mixing apparatus |
US3073576A (en) * | 1959-05-16 | 1963-01-15 | Kloeckner Humboldt Deutz Ag | Pneumatic mixer for pulverulent or fine-granular material |
US3167454A (en) * | 1959-12-24 | 1965-01-26 | Zenith Radio Corp | Fluidized-bed type of coating apparatus |
US3117027A (en) * | 1960-01-08 | 1964-01-07 | Wisconsin Alumni Res Found | Apparatus for coating particles in a fluidized bed |
US3024500A (en) * | 1960-03-28 | 1962-03-13 | David E Lawson | Apparatus for dry mixing of material |
US3106385A (en) * | 1960-04-26 | 1963-10-08 | Du Pont | Method and apparatus for solids blending |
US3073070A (en) * | 1960-10-12 | 1963-01-15 | William H Mead | Abrasive blasting system |
US3148865A (en) * | 1960-11-02 | 1964-09-15 | Gouverneur Talc Company Inc | Pneumatic conveying and conditioning method and apparatus |
US3204942A (en) * | 1963-02-18 | 1965-09-07 | Babcock & Wilcox Co | Distributor for pneumatically transported particle-form material |
US3364053A (en) * | 1963-10-12 | 1968-01-16 | Polymer Corp | Method of coating articles |
US3371425A (en) * | 1964-06-23 | 1968-03-05 | Vickers Zimmer Ag | Apparatus for reducing the sojourn times in fluidized beds |
US3345180A (en) * | 1965-01-15 | 1967-10-03 | Hupp Corp | Coffee roasting method |
US3328894A (en) * | 1965-01-15 | 1967-07-04 | Hupp Corp | Coffee roasting apparatus |
US3394468A (en) * | 1965-06-14 | 1968-07-30 | Glatt Werner | Container for the reception of a pulverulent or granular feed for treatment in a hot air dryer |
US3345181A (en) * | 1966-01-24 | 1967-10-03 | Hupp Corp | Method for roasting coffee beans and similar particulate solids |
US3329506A (en) * | 1966-01-24 | 1967-07-04 | Hupp Corp | Method for roasting coffee and similar particulate solids |
US3518777A (en) * | 1968-01-29 | 1970-07-07 | Motomi Kono | Heat exchange apparatus for fluidizing particulate material |
US3656717A (en) * | 1969-08-28 | 1972-04-18 | Polysius Ag | Process and apparatus for the continuous pneumatic treatment of fine material |
US3773297A (en) * | 1969-09-18 | 1973-11-20 | Portec Inc | Device for fluidizing stored material |
US3671018A (en) * | 1970-11-19 | 1972-06-20 | Union Carbide Corp | Bubble-blending particulate solids |
US3653639A (en) * | 1971-02-04 | 1972-04-04 | Whirl Air Flow Corp | High pressure air and liquid blending method and apparatus for discrete materials |
US3945615A (en) * | 1972-10-19 | 1976-03-23 | A. Ahlstrom Osakeyhtio | Continuous method and device for withdrawing particulate material from a container |
US3953003A (en) * | 1974-06-06 | 1976-04-27 | Aluterv Aluminiumipari Tervezo Vallalat | Tank provided with pneumatic mixing pipe |
US3957448A (en) * | 1974-12-16 | 1976-05-18 | Standard Oil Company | Divided horizontal reactor for the vapor phase polymerization of monomers at different hydrogen levels |
US3965083A (en) * | 1974-12-16 | 1976-06-22 | Standard Oil Company | Process for the vapor phase polymerization of monomers in a horizontal, quench-cooled, stirred-bed reactor using essentially total off-gas recycle and melt finishing |
US3971768A (en) * | 1974-12-16 | 1976-07-27 | Standard Oil Company (Indiana) | Vapor phase reactor off-gas recycle system for use in the vapor state polymerization of monomers |
US4129701A (en) * | 1974-12-16 | 1978-12-12 | Standard Oil Company (Indiana) | Horizontal reactor for the vapor phase polymerization of monomers |
US3999750A (en) * | 1975-12-08 | 1976-12-28 | Perkins Willis E | Artificial snowfall producing apparatus |
US4491549A (en) * | 1981-08-22 | 1985-01-01 | Hoechst Aktiengesellschaft | Device for dispersing a second phase in a first phase |
US4494932A (en) * | 1983-02-18 | 1985-01-22 | Cooper Lasersonics, Inc. | Dental cleaning apparatus and method |
US5632100A (en) * | 1993-11-17 | 1997-05-27 | Niro Holding A/S | Process and a spray drying apparatus for producing an agglomerated powder |
US6148540A (en) * | 1995-12-30 | 2000-11-21 | Nara Machinery Co., Ltd. | Pulverized body drying method and apparatus |
US5961000A (en) * | 1996-11-14 | 1999-10-05 | Sanfilippo; James J. | System and method for filling and sealing containers in controlled environments |
US20060067160A1 (en) * | 2004-09-30 | 2006-03-30 | Koetas Joseph P | Apparatus for forming a polishing pad having a reduced striations |
US7275856B2 (en) * | 2004-09-30 | 2007-10-02 | Rohm And Haas Electronic Materials Cmp Holdings, Inc. | Apparatus for forming a polishing pad having a reduced striations |
US20110017786A1 (en) * | 2008-03-17 | 2011-01-27 | Uhde Gmbh | Method and device for metered removal of a fine-grained to coarse-grained solid material or solid material mixture from a storage container |
US8646664B2 (en) * | 2008-03-17 | 2014-02-11 | Thyssenkrupp Uhde Gmbh | Method and device for the metered removal of a fine to coarse-grained solid matter or solid matter mixture from a storage container |
CN106390651A (en) * | 2016-06-08 | 2017-02-15 | 福建铁拓机械有限公司 | Integrated tail gas and waste powder treating apparatus of complete set of equipment for regeneration and stirring of asphalt |
KR20200002988A (en) | 2017-06-12 | 2020-01-08 | 미츠비시 히타치 파워 시스템즈 가부시키가이샤 | Axial flow rolling machine |
RU214406U1 (en) * | 2022-07-15 | 2022-10-26 | Общество с ограниченной ответственностью "Плазмохимические технологии" | Device for mixing and homogenizing single-walled carbon nanotubes |
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