US3295838A - Conditioner for premoistening dry powders - Google Patents

Conditioner for premoistening dry powders Download PDF

Info

Publication number
US3295838A
US3295838A US393009A US39300964A US3295838A US 3295838 A US3295838 A US 3295838A US 393009 A US393009 A US 393009A US 39300964 A US39300964 A US 39300964A US 3295838 A US3295838 A US 3295838A
Authority
US
United States
Prior art keywords
conditioner
venturi section
section
venturi
powders
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
US393009A
Inventor
Thomas E Ban
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.)
Mcdowell Wellman Engineering Co
Original Assignee
Mcdowell Wellman Engineering 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 Mcdowell Wellman Engineering Co filed Critical Mcdowell Wellman Engineering Co
Priority to US393009A priority Critical patent/US3295838A/en
Application granted granted Critical
Publication of US3295838A publication Critical patent/US3295838A/en
Assigned to DRAVO CORPORATION, A CORP. OF PA reassignment DRAVO CORPORATION, A CORP. OF PA ASSIGNS THE ENTIRE INTEREST AS OF MAY 15, 1980 Assignors: MCDOWELL-WELLMAN COMPANY
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/28—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic using special binding agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
    • B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
    • B01F25/721—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles for spraying a fluid on falling particles or on a liquid curtain
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/14—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic in rotating dishes or pans

Definitions

  • this invention relates to a conditioner or apparatus for premoistening dry powders.
  • premoistening in order to facilitate handling and subsequent operations such as pelletizing where additional moisture is added to effect a binding together of smaller particles to form green pellets.
  • preconditioning with moisture can be accomplished to a certain extent through use of well-known types of blenders such as pug mills and ribbon blenders.
  • these devices have certain disadvantages concerning maintenance and power requirements of moving mechanical parts.
  • mechanical devices generally do not enable complete dispersion of moisture with dry powder.
  • Pellets usually are quite uniformly spherical, and have an average particle size such that 90% of the batch has a substantially uniform particle size in the range of from about 4 inch to about /2 inch diameter.
  • green in reference to pellets or aggregates is meant the moist, unfired particles.
  • the green aggregates, of this invention have random particle sizes larger than the particle size of the dry powder, e.g. 100 mesh to about 200 mesh in average diameter.
  • This invention concerns a new conditioner or apparatus having a venturi type spray chamber for premoistening solids with a fine moisture spray in the throat of the venturi section.
  • the advantage of this type of device is substantially uniform blending of water or liquid medium with the powders in the absence of moving parts.
  • the annexed drawing shows a cross sectional view of one embodiment of a conditioner for premoistening dry powders.
  • this invention is in a conditioner for premoistening dry powder.
  • the conditioner is characterized by a venturi spray chamber which is vetrically disposed.
  • the dry powders are fed into the upper open extremity of the conditioner by any suitable feeding means.
  • Means for moi-stening the dry powders including a conical spray are located in the throat section of the venturi section.
  • means for vibrating the spray chamber to more uniformly blend the aqueous medium with the water insoluble dry powders.
  • means for aggregating the moistened dry powders are also provided.
  • the conditioner 2 has a restricted throat section 4 which joins an upper truncated cone 6 with a lower truncated cone 8.
  • the surfaces of the upper and lower cones converge towards the throat section 4.
  • the upper cone 6 is preferably smaller than the lower cone 8. Adjacent the upper extremity of the cone 6 and extending i from a single location.
  • a tubular feed portion indicated at 10 is rigidly supported in spaced relation to a rotating table feeder 44. Located in the feed tube 10 are means for feeding the dry powders through the up-. per open extremity of the cone 6.
  • the means for feeding is a rotating star gate feeder generally indicated at 12.
  • the star gate feeder 12 is located in a ibulbed portion 14 of the feed tube 10.
  • the feeder 12 is composed of a plurality of radially extending blades; for example, blades 16 which extend from a hub which rotates on a pin 20.
  • the feeder 12 can be rotated at variable speeds thus permitting the material to be fed into the conditioner 2 at different rates of speed with proportional amounts of water to provide an accurately blended mass or material.
  • the conditioner 2 is resiliently supported from the stationary feeder tube 10 by a plurality of resilient springs coacting therebetween, for example, springs 22 and 24, and a bellows-type seal indicated at 26. It should be noted that a foam rubber joint could be substituted for the bellows-type seal.
  • a downwardly directed spray 28 through which water, from a source carried through pipes indicated at 30, is forced.
  • Located around the outer surface of the lower cone 8 are a plurality of vibrators; for example, vibrators 3'2 and 34.
  • the vibrators are located near the center of gravity of the conditioner 2 to produce a more even vibrating action.
  • Adjacent the lower extremity of the cone 8, and, extending therefrom, is a circular bin collar indicated at 36.
  • the collar 36 is resiliently supported by or mounted to the open extremity of the lower cone 8 by a plurality of springs coacting therebetween, for example, springs 38 and 40 and a bellows type seal indicated at 42.
  • springs 38 and 40 and the bellows, seal 42 may be similar to the springs22, 24 and the bellows seal 26.
  • a similar foam rubber joint may be substituted for the bellowsseal 42.
  • a rotating table feeder 44 Adjacent the lower annular extremity of collar 36 is a rotating table feeder 44.
  • the table 44 has a diameter larger than the diameter of the collar 36.
  • Eccentrically mounted on theta'ble 44 is a cone 46, which has its apex extending into the collar 36.
  • the rotatingtable 44 and cone 46 are used to aggregate the moistened powders. As the moistened powderslhit the sides of thefrotating cone 46 and roll down its sloped'surfaces, they, have a snow balling effect which aggregates the moistened particles into larger particles of random size.
  • the table 44 is mounted on a centrally disposed shaft 48 which is rotated by any conventional rotating means, e.g. motor 50 and belt 52.
  • the aggregated moistened powders begin to accumulate on the rotating table 44 they are forced through the annular space indicated at 54, between the lower annular extremity of the bin 36 and the top of the table 44. Also, a single opening can be used within the bin section 54 to enable aggregated powders to emit The aggregated powders fall from the rotating table 44 into bins or UJPOII conveyors and are then taken to storage areas.
  • the dry powders are fed into the upper extremity of the tubular portion 10 down into the star feeder 12.
  • the rotating star feeder forces the dry powders into the conditioner or venturi section 2.
  • the dry powders pass through the throat section 4 of the conditioner 2 they are moistened with water which is sprayed from the conical spray 28.
  • the vibrating of the conditioner 2 helps blend the dry powders with the 'moisture as well as keeping the moistened particles from sticking to the sides of the conditioner 2.
  • the moistened powders then fall upon the rotating table 44 and cone 46, which have a particle size increasing effect upon the moistened powders.
  • the aggregated powders are then forced through the annular space indicated at 54 onto either conveyors or into bins where they are stored.
  • the vibrators for example, vibrators 32 and 34 located on the lower cone 8, cause the conditioner 2 to vibrate in relation to the fixed tubular feeder portion 10.
  • the vibrating motion as indicated keeps the particles from sticking to the inner surfaces of the cone and bin as well as permit-ting a complete homogenization of moisture with the powders.
  • the inner conical surfaces of the venturi section are preferably waxed so that material build up will not occur. In place of waxing, the inner surfaces of the conical sections may be lined 'with a non-adhesive liner, e.g. a sheeting coated with a non-adhesive resinous material such as polytetrafiuoroethylene.
  • a new and novel conditioner having a venturi spray chamber for premoistening relatively small particle size solids with a -fine moisture spray in the throat 'of the venturi section.
  • the vibrating conditioner substantially eliminates build up of the moisturized particles in the tube as well as permitting a complete homogenization of moisture with the powders in the absence of moving parts.
  • a conditioner for premoistening dry powder com prising :
  • i(c) means for moistening the dry powder at the throat section of the venturi section
  • said aggregating means including a circular bin resiliently supported by the venturi section whereby the circular bin is movable relative to the venturi section.
  • the conditioner of claim 1 including adjacent the lower extremity of said circular bin and in spaced relation thereto, a rotating table having a diameter larger than the diameter of the circular bin, and having eccentrically mounted thereon, a cone whose apex extends into the bin, said rotating table and cone designed to aggregate the moistened particles as it rotates.
  • the means for feeding the dry powders to the venturi section includes a fixed tubular portion, containing a feeder, said portion resiliently secured to the upper open extremity of the venturi section to support the venturi section and permit vibration'of the venturi section relative to the tubular portion.
  • the conditioner of claim 4, wherein the means for vibrating the venturi section includes a plurality of vibrators secured to the venturi section intermediate the throat and lower extremity of the venturi section.
  • the conditioner of claim 8 including a plurality of sprays located in the throat section for moistening the powders.

Description

Jan. 3, 1967 T, E. BAN
CONDITIONER FOR PREMOISTENING DRY POWDERS Filed Aug. 24, 1964 INVENTOR. THOMAS E. BAN
ATTORNEYS United States Patent Ohio Filed Aug. 24, 1964, Ser. No. 393,009 9 Claims. (Cl. 2592) This application is a continuation-in-part of my copending application Serial No. 375,180, filed June 15, 1964, now abandoned.
As indicated this invention relates to a conditioner or apparatus for premoistening dry powders.
Many forms of dried powders require premoistening in order to facilitate handling and subsequent operations such as pelletizing where additional moisture is added to effect a binding together of smaller particles to form green pellets. Generally, preconditioning with moisture can be accomplished to a certain extent through use of well-known types of blenders such as pug mills and ribbon blenders. However, these devices have certain disadvantages concerning maintenance and power requirements of moving mechanical parts. Also, mechanical devices generally do not enable complete dispersion of moisture with dry powder.
Pellets usually are quite uniformly spherical, and have an average particle size such that 90% of the batch has a substantially uniform particle size in the range of from about 4 inch to about /2 inch diameter. By the term green in reference to pellets or aggregates, is meant the moist, unfired particles. In general, the green aggregates, of this invention have random particle sizes larger than the particle size of the dry powder, e.g. 100 mesh to about 200 mesh in average diameter.
This invention concerns a new conditioner or apparatus having a venturi type spray chamber for premoistening solids with a fine moisture spray in the throat of the venturi section. The advantage of this type of device is substantially uniform blending of water or liquid medium with the powders in the absence of moving parts.
To the accomplishment of the foregoing and related ends, said invention, then, consists of the means hereinafter fully described and particularly pointed out in the appended claims, the following description and annexed drawings setting forth in detail a certain illustrative embodiment of the invention, such disclosed means constituting, however, but one of the various forms in which the principle of this invention may be' employed.
The annexed drawing shows a cross sectional view of one embodiment of a conditioner for premoistening dry powders.
Briefly stated, this invention is in a conditioner for premoistening dry powder. The conditioner is characterized by a venturi spray chamber which is vetrically disposed. The dry powders are fed into the upper open extremity of the conditioner by any suitable feeding means. Means for moi-stening the dry powders including a conical spray are located in the throat section of the venturi section. Also provided are means for vibrating the spray chamber to more uniformly blend the aqueous medium with the water insoluble dry powders. Also provided, are means for aggregating the moistened dry powders.
Referring more particularly to the drawing, there is shown a conditioner venturi spray chamber generally indicated at 2. The conditioner 2 has a restricted throat section 4 which joins an upper truncated cone 6 with a lower truncated cone 8. The surfaces of the upper and lower cones converge towards the throat section 4. The upper cone 6 is preferably smaller than the lower cone 8. Adjacent the upper extremity of the cone 6 and extending i from a single location.
3,295,838 Patented Jan. 3, 1967 therefrom is a tubular feed portion indicated at 10. The feed portion 10 is rigidly supported in spaced relation to a rotating table feeder 44. Located in the feed tube 10 are means for feeding the dry powders through the up-. per open extremity of the cone 6. In the preferred embodiment of the invention the means for feeding is a rotating star gate feeder generally indicated at 12. The star gate feeder 12 is located in a ibulbed portion 14 of the feed tube 10. The feeder 12 is composed of a plurality of radially extending blades; for example, blades 16 which extend from a hub which rotates on a pin 20. The feeder 12 can be rotated at variable speeds thus permitting the material to be fed into the conditioner 2 at different rates of speed with proportional amounts of water to provide an accurately blended mass or material.
The conditioner 2 is resiliently supported from the stationary feeder tube 10 by a plurality of resilient springs coacting therebetween, for example, springs 22 and 24, and a bellows-type seal indicated at 26. It should be noted that a foam rubber joint could be substituted for the bellows-type seal. In the throat section of the conditioner 2, is located a downwardly directed spray 28 through which water, from a source carried through pipes indicated at 30, is forced. Located around the outer surface of the lower cone 8 are a plurality of vibrators; for example, vibrators 3'2 and 34. Preferably the vibrators are located near the center of gravity of the conditioner 2 to produce a more even vibrating action. Adjacent the lower extremity of the cone 8, and, extending therefrom, is a circular bin collar indicated at 36. The collar 36 is resiliently supported by or mounted to the open extremity of the lower cone 8 by a plurality of springs coacting therebetween, for example, springs 38 and 40 and a bellows type seal indicated at 42. It should be noted that the springs 38 and 40 and the bellows, seal 42 may be similar to the springs22, 24 and the bellows seal 26. Also a similar foam rubber joint may be substituted for the bellowsseal 42. i t
Adjacent the lower annular extremity of collar 36 is a rotating table feeder 44. The table 44 has a diameter larger than the diameter of the collar 36. Eccentrically mounted on theta'ble 44 is a cone 46, which has its apex extending into the collar 36. The rotatingtable 44 and cone 46 are used to aggregate the moistened powders. As the moistened powderslhit the sides of thefrotating cone 46 and roll down its sloped'surfaces, they, have a snow balling effect which aggregates the moistened particles into larger particles of random size. The table 44 is mounted on a centrally disposed shaft 48 which is rotated by any conventional rotating means, e.g. motor 50 and belt 52. As the aggregated moistened powders begin to accumulate on the rotating table 44 they are forced through the annular space indicated at 54, between the lower annular extremity of the bin 36 and the top of the table 44. Also, a single opening can be used within the bin section 54 to enable aggregated powders to emit The aggregated powders fall from the rotating table 44 into bins or UJPOII conveyors and are then taken to storage areas.
In operation the dry powders are fed into the upper extremity of the tubular portion 10 down into the star feeder 12. The rotating star feeder forces the dry powders into the conditioner or venturi section 2. As the dry powders pass through the throat section 4 of the conditioner 2 they are moistened with water which is sprayed from the conical spray 28. The vibrating of the conditioner 2 helps blend the dry powders with the 'moisture as well as keeping the moistened particles from sticking to the sides of the conditioner 2. The moistened powders then fall upon the rotating table 44 and cone 46, which have a particle size increasing effect upon the moistened powders. The aggregated powders are then forced through the annular space indicated at 54 onto either conveyors or into bins where they are stored.
The vibrators, for example, vibrators 32 and 34 located on the lower cone 8, cause the conditioner 2 to vibrate in relation to the fixed tubular feeder portion 10. The springs and bellows joint connecting the lower cone 8 with the collar bin 36, permit the collar bin 36 tovibrate relative to the cone 8. The vibrating motion as indicated keeps the particles from sticking to the inner surfaces of the cone and bin as well as permit-ting a complete homogenization of moisture with the powders. The inner conical surfaces of the venturi section are preferably waxed so that material build up will not occur. In place of waxing, the inner surfaces of the conical sections may be lined 'with a non-adhesive liner, e.g. a sheeting coated with a non-adhesive resinous material such as polytetrafiuoroethylene.
In the cases of pelletizing processes where precision blending of moisture with dry powders is a requisite, the feed rates of dried pellets are controlled. In cases of building a single model with a wide range of capacities, it may be advisable to have a whole series of conical sprays within the venturi throat section to permit selection of specific sprays to be utilized for specific feed rates of solids from the star gate feeder.
Thus there has been provided a new and novel conditioner, having a venturi spray chamber for premoistening relatively small particle size solids with a -fine moisture spray in the throat 'of the venturi section. The vibrating conditioner substantially eliminates build up of the moisturized particles in the tube as well as permitting a complete homogenization of moisture with the powders in the absence of moving parts.
Other modes of applying the principle of this invention may be employed instead of those specifically set forth above, changes being made as regards the details herein disclosed, provided the elements set forth in any of the following claims, or the equivalent of such be employed.
It is, therefore, particularly pointed out and distinctly claimed as the invention:
. 1. A conditioner for premoistening dry powder com prising:
(a) a vertically disposed venturi section having open extremities, in which dry powder is conditioned;
(b) means for feeding dry powder through the upper open extremity of the section;
i(c) means for moistening the dry powder at the throat section of the venturi section;
(d) means for vibrating the venturi section; and
(e) means for aggregating the moistened dry powder adjacent the lower extremity of the venturi section,
said aggregating means including a circular bin resiliently supported by the venturi section whereby the circular bin is movable relative to the venturi section.
2. The conditioner of claim 1, including adjacent the lower extremity of said circular bin and in spaced relation thereto, a rotating table having a diameter larger than the diameter of the circular bin, and having eccentrically mounted thereon, a cone whose apex extends into the bin, said rotating table and cone designed to aggregate the moistened particles as it rotates.
3. The conditioner of claim 2, wherein the means for feeding the dry powders to the venturi section includes a fixed tubular portion, containing a feeder, said portion resiliently secured to the upper open extremity of the venturi section to support the venturi section and permit vibration'of the venturi section relative to the tubular portion.
4. The conditioner of claim 3, wherein the means for moistening the dry powders includes a downwardly directed spray located in the throat section of the venturi section.
5. The conditioner of claim 4, wherein the means for vibrating the venturi section includes a plurality of vibrators secured to the venturi section intermediate the throat and lower extremity of the venturi section.
6. The conditioner of claim 5, wherein the inner surface of the lower truncated tubular portion of the venturi section is waxed to prevent material build up on such surface.
7. The conditioner of claim 5, wherein the inner surface of the lower truncated tubular portion of the venturi section is lined with polytetrafluoroethylene.
8. The conditioner of claim 7, including a bellows type joint for resiliently securing the venturi section to the parts adjacent its upper and lower extremities.
9. The conditioner of claim 8, including a plurality of sprays located in the throat section for moistening the powders.
References Cited by the Examiner UNITED STATES PATENTS 1,138,457 5/ 1915 Dahlrneyer. 2,116,708 5/1938 Niekamp.
2,914,797 12/1959 Cavanagh 181 3,167,259 l/ 1965 Pitchford 2592 X 3,202,281 8/ 1965 Weston 2594 X 3,226,092 112/ 1965 Graham et a1. 259-2 WALTER A. 'SCHEEL, Primary Examiner.
J. M. BELL, Assistant Examiner.

Claims (1)

1. A CONDITIONER FOR PREMOISTENING DRY POWDER COMPRISING: (A) A VERTICALLY DISPOSED VENTURI SECTION HAVING OPEN EXTREMITIES, IN WHICH DRY POWDER IS CONDITIONED; (B) MEANS FOR FEEDING DRY POWDER THROUGH THE UPPER OPEN EXTREMITY OF THE SECTION; (C) MEANS FOR MOISTENING THE DRY POWDR AT THE THROAT SECTION OF THE VENTURI SECTION; (D) MEANS FOR VIBRATING THE VENTURI SECTION; AND (E) MEANS FOR AGGREGATING THE MOISTENED DRY POWDER ADJACENT THE LOWER EXTREMITY OF THE VENTURI SECTION, SAID AGGREGATING MEANS INCLUDING A CIRCULAR BIN RESILIENTLY SUPPORTED BY THE VENTURI SECTION WHEREBY THE CIRCULAR BIN IS MOVABLE RELATIVE TO THE VENTURI SECTION.
US393009A 1964-08-24 1964-08-24 Conditioner for premoistening dry powders Expired - Lifetime US3295838A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US393009A US3295838A (en) 1964-08-24 1964-08-24 Conditioner for premoistening dry powders

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US393009A US3295838A (en) 1964-08-24 1964-08-24 Conditioner for premoistening dry powders

Publications (1)

Publication Number Publication Date
US3295838A true US3295838A (en) 1967-01-03

Family

ID=23552924

Family Applications (1)

Application Number Title Priority Date Filing Date
US393009A Expired - Lifetime US3295838A (en) 1964-08-24 1964-08-24 Conditioner for premoistening dry powders

Country Status (1)

Country Link
US (1) US3295838A (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3445090A (en) * 1967-02-04 1969-05-20 Loedige Wilhelm Screw mixer
US3712593A (en) * 1970-04-03 1973-01-23 Fischer Ag Georg Method of and device for continuous preparation of granular material, such as foundry sand
US3966975A (en) * 1970-12-21 1976-06-29 Aktieselskabet Niro Atomizer Method for producing agglomerated powders and apparatus for performing the method
US4564298A (en) * 1984-05-15 1986-01-14 Union Oil Company Of California Hydrofoil injection nozzle
US4722300A (en) * 1986-03-10 1988-02-02 Beacon Industries, Inc. Automatic feeder for pets and other animals
US4867930A (en) * 1981-10-14 1989-09-19 Alfrey Norval K Priller method
FR2654647A1 (en) * 1989-11-20 1991-05-24 Elf Isolation MIXER FOR THE IMPREGNATION IN THE MASS OF PARTICLES BY A BINDER.
US5019302A (en) * 1986-03-12 1991-05-28 Washington University Technology Associates, Inc. Method for granulation
US5100592A (en) * 1986-03-12 1992-03-31 Washington University Technology Associated, Inc. Method and apparatus for granulation and granulated product
WO1993003831A1 (en) * 1991-08-16 1993-03-04 Veag Vereinigte Energiewerke Aktiengesellschaft Method and device for wetting power-station filter ash
FR2703268A1 (en) * 1993-03-29 1994-10-07 Armoa Apparatus for moistening powdery materials, especially those of the type having hydraulic (water-based) binders
US5813754A (en) * 1996-03-13 1998-09-29 Matrix Master, Inc. Vibration input to moving aqueous cemetitious slurry
US6015225A (en) * 1996-03-13 2000-01-18 Matrix Master Inc. Vibration input to moving aqueous cementitious slurry
US20060221764A1 (en) * 2005-03-17 2006-10-05 Everett Steve E Method and system for preparing input material for structural building blocks
US20070297272A1 (en) * 2004-07-30 2007-12-27 Werner Kempter Method for Mixing a Plastic Granulate With an Additive and Mixing Device for Carrying Out Said Method and Device Provided With Said Mixing Device
US20120091223A1 (en) * 2010-10-19 2012-04-19 Jinghai Yi Nanoparticle Aerosol Generator

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1138457A (en) * 1915-01-13 1915-05-04 Karl Otto Dahlmeyer Jar-molding machine.
US2116708A (en) * 1936-01-11 1938-05-10 Master Electric Co Apparatus for compacting concrete and the like
US2914797A (en) * 1956-09-25 1959-12-01 Outario Res Foundation Pellet making means and method
US3167259A (en) * 1961-03-08 1965-01-26 Arthur H Pitchford Method and apparatus for grinding and/or blending
US3202281A (en) * 1964-10-01 1965-08-24 Weston David Method for the flotation of finely divided minerals
US3226092A (en) * 1962-05-09 1965-12-28 Graham Geoffroy Spray-type processing columns with pulsed continuous phase

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1138457A (en) * 1915-01-13 1915-05-04 Karl Otto Dahlmeyer Jar-molding machine.
US2116708A (en) * 1936-01-11 1938-05-10 Master Electric Co Apparatus for compacting concrete and the like
US2914797A (en) * 1956-09-25 1959-12-01 Outario Res Foundation Pellet making means and method
US3167259A (en) * 1961-03-08 1965-01-26 Arthur H Pitchford Method and apparatus for grinding and/or blending
US3226092A (en) * 1962-05-09 1965-12-28 Graham Geoffroy Spray-type processing columns with pulsed continuous phase
US3202281A (en) * 1964-10-01 1965-08-24 Weston David Method for the flotation of finely divided minerals

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3445090A (en) * 1967-02-04 1969-05-20 Loedige Wilhelm Screw mixer
US3712593A (en) * 1970-04-03 1973-01-23 Fischer Ag Georg Method of and device for continuous preparation of granular material, such as foundry sand
US3966975A (en) * 1970-12-21 1976-06-29 Aktieselskabet Niro Atomizer Method for producing agglomerated powders and apparatus for performing the method
US4867930A (en) * 1981-10-14 1989-09-19 Alfrey Norval K Priller method
US4564298A (en) * 1984-05-15 1986-01-14 Union Oil Company Of California Hydrofoil injection nozzle
US4722300A (en) * 1986-03-10 1988-02-02 Beacon Industries, Inc. Automatic feeder for pets and other animals
US5100592A (en) * 1986-03-12 1992-03-31 Washington University Technology Associated, Inc. Method and apparatus for granulation and granulated product
US5019302A (en) * 1986-03-12 1991-05-28 Washington University Technology Associates, Inc. Method for granulation
EP0434477A1 (en) * 1989-11-20 1991-06-26 Efisol Mixer for impregnating particles in a mass with a binding material
US5073032A (en) * 1989-11-20 1991-12-17 Efisol Mixing device for bulk impregnation of particulate matter by a binder
FR2654647A1 (en) * 1989-11-20 1991-05-24 Elf Isolation MIXER FOR THE IMPREGNATION IN THE MASS OF PARTICLES BY A BINDER.
AU628684B2 (en) * 1989-11-20 1992-09-17 Efisol, Societe Anonyme Mixing device for bulk impregnation of particulate matter by a binder
TR26614A (en) * 1991-08-16 1995-03-15 Ver Energiewerke Ag METHODS AND FACILITIES USING FILTER TOWER IN THERMAL POWER PLANTS
WO1993003831A1 (en) * 1991-08-16 1993-03-04 Veag Vereinigte Energiewerke Aktiengesellschaft Method and device for wetting power-station filter ash
FR2703268A1 (en) * 1993-03-29 1994-10-07 Armoa Apparatus for moistening powdery materials, especially those of the type having hydraulic (water-based) binders
US5813754A (en) * 1996-03-13 1998-09-29 Matrix Master, Inc. Vibration input to moving aqueous cemetitious slurry
US6015225A (en) * 1996-03-13 2000-01-18 Matrix Master Inc. Vibration input to moving aqueous cementitious slurry
US20070297272A1 (en) * 2004-07-30 2007-12-27 Werner Kempter Method for Mixing a Plastic Granulate With an Additive and Mixing Device for Carrying Out Said Method and Device Provided With Said Mixing Device
US20060221764A1 (en) * 2005-03-17 2006-10-05 Everett Steve E Method and system for preparing input material for structural building blocks
US20120091223A1 (en) * 2010-10-19 2012-04-19 Jinghai Yi Nanoparticle Aerosol Generator
US8881997B2 (en) * 2010-10-19 2014-11-11 West Virginia University Nanoparticle aerosol generator

Similar Documents

Publication Publication Date Title
US3295838A (en) Conditioner for premoistening dry powders
CN109126602B (en) Powder-liquid continuous mixer and continuous metering mixing production line
JPS5951329B2 (en) Mixing method and equipment for fine particulate components
US3051454A (en) Mixing apparatus
US3894882A (en) Agglomerating powders
CN206064345U (en) For the granulating disc of haydite production
US4112517A (en) Mixing apparatus
JP4603688B2 (en) Densification of bulk material
US3162428A (en) Process for mixing and wetting solid materials
US3345683A (en) Inclined-dish granulator and separator
US3397067A (en) Flour product and method of making
US4165823A (en) Dispensing apparatus
US3912231A (en) Apparatus for treating and mixing particles
JPH0727476A (en) Treatment apparatus of moistened granular material
JPS6032490B2 (en) mixing device
US2674522A (en) Apparatus for pelletizing carbon black
US3712593A (en) Method of and device for continuous preparation of granular material, such as foundry sand
US2263118A (en) Apparatus for pelleting carbon black
US3228115A (en) Apparatus for aggregating difficult to aggregate materials
JPS6055175B2 (en) Mixer/granulator
US3315589A (en) Pellet forming apparatus
US4174937A (en) Powder agglomerator and its method of use
US3357798A (en) Centrifugal apparatus for obtaining chemical reactions
JPH10296069A (en) Granulating device
JPS632212B2 (en)