US2648609A - Method of applying coatings to edible tablets or the like - Google Patents

Method of applying coatings to edible tablets or the like Download PDF

Info

Publication number
US2648609A
US2648609A US71997A US7199749A US2648609A US 2648609 A US2648609 A US 2648609A US 71997 A US71997 A US 71997A US 7199749 A US7199749 A US 7199749A US 2648609 A US2648609 A US 2648609A
Authority
US
United States
Prior art keywords
tablets
air
coating
screen
chamber
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
US71997A
Inventor
Dale E Wurster
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.)
Wisconsin Alumni Research Foundation
Original Assignee
Wisconsin Alumni Research Foundation
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 Wisconsin Alumni Research Foundation filed Critical Wisconsin Alumni Research Foundation
Priority to US71997A priority Critical patent/US2648609A/en
Application granted granted Critical
Publication of US2648609A publication Critical patent/US2648609A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/20Pills, tablets, discs, rods
    • A61K9/28Dragees; Coated pills or tablets, e.g. with film or compression coating
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61JCONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
    • A61J3/00Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms
    • A61J3/005Coating of tablets or the like
    • 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
    • Y10S159/00Concentrating evaporators
    • Y10S159/03Fluidized bed

Definitions

  • My invention relates, generally, to methods of and means for applying coatings, and it has particular relation to the coating of medicinal tablets, chewing gum, candy, nuts, etc.
  • T support the tablets in air in a coating chamber and to coat the same While they are so positioned; to support the tablets in an upwardly flowing air stream; to heat the air prior to its contact with the tablets to dr the coating thereon; to cause the air to flow in a turbulent fashion and tumble the tablets so that they may be coated uniformly; to move the tablets downwardly on a bias transversely of the air stream while they are being coated; to introduce the coating material into the air stream under neath its initial contact point with the tablets; to introduce individually into the air stream different coating materials; and to direct a current of air upwardly in the coating chamber along its inner surface to prevent the coating material from impinging thereon.
  • Figure l is a longitudinal sectional view of a coating mechanism constructed in accordance with my invention.
  • Figure 2 is a View partly in section and partly in elevation at an enlarged scale showing in more detail the construction of the manifold which directs air upwardly along the inner surface of the coating chamber;
  • Figure 3 is a top plan View of the rotating disc which causes the air to flow in a turbulent fashion. 7
  • the reference character I'll designates a vertically positioned coatin chamber which may be formed of metal or glass.
  • the coating chamber Ill preferably has a circular cross section, and it may be of conical, modified conical, or cylindrical shape as may be desired. Near its lower end there is provided an entrance I I for the tablets to be coated.
  • An inlet tube [2 communicates with the entrance and slides l3 and 14 are positioned therein to permit the introduction of the tablets to be coated into the chamber Ill in batches.
  • a screen I which extends transversely thereacross and on a bias so that the tablets to be coated and while they are being coated move across the chamber Ill and downwardly to an exit ['6 with which an outlet tube ll communicates.
  • the tube Il may discharge into a polishing pan or similar receptacle.
  • Slides l8 and It may be provided in the outlet tube I! for. controlling the flow of the coated tablets theretln'ough in batches similar to the manner in which they are permitted to flow onto the screen l5 by the slides l3 and M.
  • are positioned in the lower end of the chamber Ill below the screen l5 and are directed upwardly to suppl an air stream flowing upwardly in the chamber H) of sufiicient velocity to maintain the uncoated and partially coated tablets slightly out of contact with the screen l5.
  • may be connected by conduits 2B and 2
  • the tablets be supported in the air stream which flows uD- wardly through the coating chamber I0 but also it is desirable that they be tumbled so as to coat the same more uniformly.
  • the flow of air through the coating chamber II] is arranged so that, in place of it being a streamlined flow, it is a turbulent flow.
  • a disc 22 is provided which may be rotated at a constant speed by a motor 23. As shown more clearly in Figure 3 the disc 22 has circular rows 24, 25, 26, and 21 of perforations through which the air from the jets 20 and 2
  • register with the circular rows 24, 25, 26, and 21 of perforations so that the air from the former is d rected byv the row of perforations individual thereto.
  • the rows 24 and 21 of the perforations are inclined inwardly while the row 25 ofperforations is inclined outwardly.
  • the remaining row 26 extends Vertically through the disc 22.
  • an electric heater element 28 in the form of a grid, may be positioned immediately above the rotating disc 22. It will be understood that the heater element 28 maybe connected for energization to a suitable Current source and that the degree of heat can be varied by varying the amount of current fl g.
  • the material for coating the tablets may be supplied through conduits 30, 3
  • and 32 terminates in a nozzle 33 which, as shown in Figure 1, is directed against the tablets near the upper edge of the screen l5 so that the coating material is supplied to the tablets as soon as they pass through the entrance II.
  • various coating materials can be supplied.
  • the conduit is arranged to have powdered lactose blown therethrough.
  • carries an acacia solution, while the conduit 32 may carry a sugar solution. It will be understood that these particular materials are mentioned for illustrative purposes only and that other coating materials can be used as may be desired.
  • Certain of the coating materials may tend to adhere to the inner surface of the coating chamber Ill particularly in the immediate vicinity of the screen l5.
  • a ringlike manifold 34 may be positioned just above the screen I5.
  • the manifold 34 has outwardly and upwardly directed openings or apertures 35 which cause air supplied to the manifold 34 from a suitable source of compressed air to flow in the directions indicated by the arrows 36 over the inner surface of the chamber In for preventing the coating material from engaging the same.
  • a screen 31 may be provided at the upper end of the coating chamber II] to prevent the escape of tablets in the event that the pressure supplied through the jets 20 and 2
  • An exhaust tube 38 connects the coating chamber II) to a suitable recovery and exhaust chamber as will be understood readily.
  • the motor 23 is energized to drive the disc 22 at the desired speed.
  • Air under pressure is supplied through the conduits 20' and 2
  • This air pressure also is adjusted so that when the tablets are fully coated it will be insufficient to maintain them above the screen l5 at the lower end thereof adjacent the exit [6.
  • the current flowing through the heating element 28 is adjusted so that the coating applied to the tablets above the screen I5 is dried satisfactorily.
  • and 32 are arranged and adjusted so that the desired proportions will be applied to the tablets at rates which will provide the desired thickness of coating.
  • Air is supplied to the manifold 34, it being understood that the pressure at the apertures 35 therein is slightly greater than the air pressure at the air jets 20 and 2
  • the slide I3 is raised to permit a charge of uncoated tablets to flow downwardly through the inlet tube I2 against the slide Id.
  • the slide I3 is closed and then the slide I4 is opened.
  • the uncoated tablets flow through the entrance II onto the upper end of the screen I5 and are immediately lifted thereabove and tumbled.
  • the slide I8 is opened and they are allowed to dischargethrough the exit l6 into the outlet tube II. Thereafter the slide 18 is closed and the slide I9 is opened to permit the coated tablets to be discharged into the polishing pan or other receptacle as may be desired.

Description

Aug. 11, 1953 D. E. WURSTER METHOD OF APPLYING COATINGS TO EDIBLE TABLETS OR THE LIKE Filed Jan. 21, 1949 RECOVER Y Alva Ex HA us 1- AIR Duscmme: ALONG WALL OF COMPRESSED OUTLET To Pou SHING PAN IN V EN TOR.
Patented Aug. 11, 1953 METHOD OF APPLYING COATINGS TO EDIBLE TABLETS OR THE LIKE Dale E. Wurster, Madison, Wis., assignor to Wisconsin Alumni Research Foundation, Madison, W1s., a corporation of Wisconsin Application January 21, 1949, Serial No. 71,997
6 Claims. 1
My invention relates, generally, to methods of and means for applying coatings, and it has particular relation to the coating of medicinal tablets, chewing gum, candy, nuts, etc.
Among the objects of my invention are: T support the tablets in air in a coating chamber and to coat the same While they are so positioned; to support the tablets in an upwardly flowing air stream; to heat the air prior to its contact with the tablets to dr the coating thereon; to cause the air to flow in a turbulent fashion and tumble the tablets so that they may be coated uniformly; to move the tablets downwardly on a bias transversely of the air stream while they are being coated; to introduce the coating material into the air stream under neath its initial contact point with the tablets; to introduce individually into the air stream different coating materials; and to direct a current of air upwardly in the coating chamber along its inner surface to prevent the coating material from impinging thereon.
Other objects of my invention will, in part, be obvious and in part appear hereinafter.
This invention is disclosed in the embodiment thereof shown in the accompanying drawing and it comprises the features of construction, combination of elements, arrangement of parts and method steps which will be set forth in detail hereinafter and the scope of the application of which will be indicated in the appended claims.
For a more complete understanding of the nature and scope of my invention, reference can be had to the following detailed description, taken together with the accompanying drawing, in which:
Figure l is a longitudinal sectional view of a coating mechanism constructed in accordance with my invention;
Figure 2 is a View partly in section and partly in elevation at an enlarged scale showing in more detail the construction of the manifold which directs air upwardly along the inner surface of the coating chamber; and
Figure 3 is a top plan View of the rotating disc which causes the air to flow in a turbulent fashion. 7
Referring now particularly to the drawing, it will be observed that the reference character I'll designates a vertically positioned coatin chamber which may be formed of metal or glass. The coating chamber Ill preferably has a circular cross section, and it may be of conical, modified conical, or cylindrical shape as may be desired. Near its lower end there is provided an entrance I I for the tablets to be coated. An inlet tube [2 communicates with the entrance and slides l3 and 14 are positioned therein to permit the introduction of the tablets to be coated into the chamber Ill in batches.
Within the chamber In there is a screen I which extends transversely thereacross and on a bias so that the tablets to be coated and while they are being coated move across the chamber Ill and downwardly to an exit ['6 with which an outlet tube ll communicates. The tube Il may discharge into a polishing pan or similar receptacle. Slides l8 and It may be provided in the outlet tube I! for. controlling the flow of the coated tablets theretln'ough in batches similar to the manner in which they are permitted to flow onto the screen l5 by the slides l3 and M.
It is desirable that the uncoated and partially coated tablets above the screen l5 be supported in air so that they can be evenly coated. For this purpose air jets 20 and 2| are positioned in the lower end of the chamber Ill below the screen l5 and are directed upwardly to suppl an air stream flowing upwardly in the chamber H) of sufiicient velocity to maintain the uncoated and partially coated tablets slightly out of contact with the screen l5. The air jets 20 and 2| may be connected by conduits 2B and 2| to a suitable. source of compressed air, the pressure of which is adjusted so as to maintain the uncoated and partially coated tablets slightly above the screen l5 to be coated in a manner to be described presently.
Not only is it desirable that the tablets be supported in the air stream which flows uD- wardly through the coating chamber I0 but also it is desirable that they be tumbled so as to coat the same more uniformly. For this purpose the flow of air through the coating chamber II] is arranged so that, in place of it being a streamlined flow, it is a turbulent flow. For this purpose a disc 22 is provided which may be rotated at a constant speed by a motor 23. As shown more clearly in Figure 3 the disc 22 has circular rows 24, 25, 26, and 21 of perforations through which the air from the jets 20 and 2| flows. As shown in Figure l the air jets 20 and 2| register with the circular rows 24, 25, 26, and 21 of perforations so that the air from the former is d rected byv the row of perforations individual thereto. Also as shown in Figure 1 the rows 24 and 21 of the perforations are inclined inwardly while the row 25 ofperforations is inclined outwardly. The remaining row 26 extends Vertically through the disc 22. The several air streams thus directed by the perforations 24, 25, 26, and 2'! impinge on the uncoated and partially coated tablets above the screen IS in a turbulent fashion and cause them to be tumbled so that they can be evenly and completely coated with the coating material.
With a view to drying quickly the coating material on the tablets, provision is made for heating the air as it passes upwardly through the chamber ll) underneath the screen [5. For this purpose an electric heater element 28, in the form of a grid, may be positioned immediately above the rotating disc 22. It will be understood that the heater element 28 maybe connected for energization to a suitable Current source and that the degree of heat can be varied by varying the amount of current fl g.
therethrough.
The material for coating the tablets may be supplied through conduits 30, 3| and 32, the number being determined by the number of different coating materials to be employed. Each of the conduits 30, 3| and 32 terminates in a nozzle 33 which, as shown in Figure 1, is directed against the tablets near the upper edge of the screen l5 so that the coating material is supplied to the tablets as soon as they pass through the entrance II. It will be understood that various coating materials can be supplied. As illustrated in Figure 1, the conduit is arranged to have powdered lactose blown therethrough. The conduit 3| carries an acacia solution, while the conduit 32 may carry a sugar solution. It will be understood that these particular materials are mentioned for illustrative purposes only and that other coating materials can be used as may be desired.
Certain of the coating materials may tend to adhere to the inner surface of the coating chamber Ill particularly in the immediate vicinity of the screen l5. In order to prevent this a ringlike manifold 34 may be positioned just above the screen I5. As shown in Figure 2 the manifold 34 has outwardly and upwardly directed openings or apertures 35 which cause air supplied to the manifold 34 from a suitable source of compressed air to flow in the directions indicated by the arrows 36 over the inner surface of the chamber In for preventing the coating material from engaging the same.
At the upper end of the coating chamber II] a screen 31 may be provided to prevent the escape of tablets in the event that the pressure supplied through the jets 20 and 2| should be sufficiently great as to cause them to rise to this position. An exhaust tube 38 connects the coating chamber II) to a suitable recovery and exhaust chamber as will be understood readily.
In operation, the motor 23 is energized to drive the disc 22 at the desired speed. Air under pressure is supplied through the conduits 20' and 2| to the jets 20 and 2| respectively so that the uncoated and partially coated tablets on the screen I5 will be tumbled thereabove. This air pressure also is adjusted so that when the tablets are fully coated it will be insufficient to maintain them above the screen l5 at the lower end thereof adjacent the exit [6. The current flowing through the heating element 28 is adjusted so that the coating applied to the tablets above the screen I5 is dried satisfactorily. The coating materials supplied to the conduits 30, 3| and 32 are arranged and adjusted so that the desired proportions will be applied to the tablets at rates which will provide the desired thickness of coating. Air is supplied to the manifold 34, it being understood that the pressure at the apertures 35 therein is slightly greater than the air pressure at the air jets 20 and 2| so that the desired air flow takes place along the inner surface of the chamber [0 to prevent the coating material from impinging thereon.
Now, the slide I3 is raised to permit a charge of uncoated tablets to flow downwardly through the inlet tube I2 against the slide Id. The slide I3 is closed and then the slide I4 is opened. The uncoated tablets flow through the entrance II onto the upper end of the screen I5 and are immediately lifted thereabove and tumbled. At
4 the same time they are subjected to the atomized flow of coating materials from the nozzles 33 which are supplied individually by the conduits 30, 3| and 32 in the manner described. The partially coated tablets move transversely of the chamber .IO and downwardly on a bias but are still being tumbled above the screen l5 until the coating thereon is sufficiently heavy so that the upwardly flowing air stream is insufficient to maintain them out of contact with the screen '|5. When all of the tablets have been completely coated, the slide I8 is opened and they are allowed to dischargethrough the exit l6 into the outlet tube II. Thereafter the slide 18 is closed and the slide I9 is opened to permit the coated tablets to be discharged into the polishing pan or other receptacle as may be desired.
It will be obvious that certain changes can be made in the foregoing construction and method without departing from the spirit and scope of this invention. Accordingly, it is intended that all matter shown in the accompanying drawing and described hereinbefore shall be interpreted as illustrative and not in a limiting sense.
I claim as my invention:
1. The process of covering eatable tablets of the type of medicinal tablets, chewing gum, candy and nuts with a sugary coating which comprises: moving an air stream in a confined space upwardly past the eatable tablets with a force sufiicient to suspend them continuously therein, and introducing the sugary coating material into said air stream prior to its contact with the eatable tablets.
2. The invention, as set forth in claim 1, wherein the coating is wet on application and the air stream is heated to dry quickly the coating applied to the tablets.
3. The invention, as set forth in claim 2, wherein the air stream is turbulent to tumble the tablets whereby they receive a coating of uniform thickness.
4. The invention, as set forth in claim 1, wherein the tablets move downwardly on a bias transversely of the air stream while being coated.
5. The invention, as set forth in claim 4, wherein the coating material is introduced into the air stream at a position close to the initial contact point thereof with the tablets.
6. The invention, as set forth in claim 1, wherein the coating material comprises a plurality of different materials and they are introduced separately into the air stream.
DALE- E. WURSTE'R.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,473,165 Steigmeyer Nov. 6, 1923 1,546,922 Faber July 21, 1925 1,725,608 Zebulski Aug. 20, 1929 2,059,983 Dent et al. Nov. 3, 1936 2,259,879 Denning -1 Oct. 21, 1941 2,339,932 Kuhl Jan. 25, 1944 2,349,230 Thomas May 16, 1944 2,399,717 Arveson May 7, 1946 2,447,006 Gamson Aug. 17, 1948 2,459,836 Murphee Jan. 25, 1949 2,491,632 Wieder Dec. 20, 1949 2,493,198 Kelley, Jr. Jan. 3, 1950 2,498,405 Fader Feb. 21, .1950 2,536,168 Goggin Jan. 2, 1951 2,561,392
Marshall July 24, 1951

Claims (1)

1. THE PROCESS OF COVERING EATABLE TABLETS OF THE TYPE OF MEDICINAL TABLETS, CHEWING GUM, CANDY AND NUTS WITH A SUGARY COATING WHICH COMPRISES: MOVING AN AIR STREAM IN A CONFINED SPACE UPWARDLY PAST THE EATABLE TABLETS WITH A FORCE SUFFICIENT TO SUSPEND THEM CONTINUOUSLY THEREIN, AND INTRODUCING THE SUGARY COATING MATERIAL INTO SAID AIR STREAM PRIOR TO ITS CONTACT WITH THE EATABLE TABLETS.
US71997A 1949-01-21 1949-01-21 Method of applying coatings to edible tablets or the like Expired - Lifetime US2648609A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US71997A US2648609A (en) 1949-01-21 1949-01-21 Method of applying coatings to edible tablets or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US71997A US2648609A (en) 1949-01-21 1949-01-21 Method of applying coatings to edible tablets or the like

Publications (1)

Publication Number Publication Date
US2648609A true US2648609A (en) 1953-08-11

Family

ID=22104908

Family Applications (1)

Application Number Title Priority Date Filing Date
US71997A Expired - Lifetime US2648609A (en) 1949-01-21 1949-01-21 Method of applying coatings to edible tablets or the like

Country Status (1)

Country Link
US (1) US2648609A (en)

Cited By (68)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2799241A (en) * 1949-01-21 1957-07-16 Wisconsin Alumni Res Found Means for applying coatings to tablets or the like
US2833241A (en) * 1955-04-18 1958-05-06 George C Crowley Machine for coating spherical objects
US2844489A (en) * 1957-12-20 1958-07-22 Knapsack Ag Fluidized bed coating process
US3012900A (en) * 1957-04-26 1961-12-12 Phillips Petroleum Co Dusting particles of adhesive materials
US3089824A (en) * 1959-04-30 1963-05-14 Wisconsin Alumui Res Foundatio Granulating and coating process for uniform granules
US3097958A (en) * 1958-06-10 1963-07-16 Chain Belt Co Fluidized coating machine
US3112220A (en) * 1960-02-26 1963-11-26 Abbott Lab Method and apparatus for coating particles
US3145146A (en) * 1961-10-31 1964-08-18 Warner Lambert Pharmaceutical Modified mannitol for pharmaceutical tablets
US3152005A (en) * 1962-03-29 1964-10-06 Dow Chemical Co Process for the preparation of pelletized solids
DE1182394B (en) * 1961-11-01 1964-11-26 Foremost Dairies Inc Process for coating pharmaceutical tablets
US3253944A (en) * 1964-01-13 1966-05-31 Wisconsin Alumni Res Found Particle coating process
US3256111A (en) * 1964-12-04 1966-06-14 Abbott Lab Method for coating tablets
US3328256A (en) * 1963-05-27 1967-06-27 William E Gaunt Spherical beads and their production
US3361631A (en) * 1963-09-30 1968-01-02 Sandoz Ag Method of sugar coating pharmaceutical tablets
US3464926A (en) * 1965-04-26 1969-09-02 Pennwalt Corp Process for encapsulation
US3635752A (en) * 1969-11-04 1972-01-18 Monsanto Co Process for the preparation of glass-concentrate capsules in a polyvinyl chloride matrix
US3800740A (en) * 1972-12-14 1974-04-02 Int Nickel Co Apparatus for decomposition of metal carbonyls
US3849077A (en) * 1971-09-09 1974-11-19 Rhone Progil Continuous method for the recovery by condensation in the solid state of sublimable substances
US4100148A (en) * 1975-06-13 1978-07-11 Rutgerswerke Aktiengesellschaft Storage-stable, very quickly hardenable, one-component sealant based on mercapto-terminated polymers
US4338878A (en) * 1980-11-26 1982-07-13 United Technologies Corporation Fluidized bed with sloped aperture plate
US4615698A (en) * 1984-03-23 1986-10-07 Alza Corporation Total agent osmotic delivery system
US4675140A (en) * 1984-05-18 1987-06-23 Washington University Technology Associates Method for coating particles or liquid droplets
US4735015A (en) * 1983-11-25 1988-04-05 Basf Corporation Seed protective coating
US4772477A (en) * 1986-10-17 1988-09-20 Balchem Corporation Meat acidulant
US4803092A (en) * 1986-10-17 1989-02-07 Balchem Corporation Method of acidulating a comminuted meat product
US5095035A (en) * 1981-07-31 1992-03-10 Eby Iii George A Flavor stable zinc acetate compositions for oral absorption
US5098893A (en) * 1989-02-16 1992-03-24 Pafra Limited Storage of materials
US5190775A (en) * 1991-05-29 1993-03-02 Balchem Corporation Encapsulated bioactive substances
US5211896A (en) * 1991-06-07 1993-05-18 General Motors Corporation Composite iron material
US5254168A (en) * 1992-06-04 1993-10-19 Howard Littman Coating apparatus having opposed atomizing nozzles in a fluid bed column
US5350659A (en) * 1993-03-31 1994-09-27 Xerox Corporation Preparation of conductive toners using fluidized bed processing equipment
US5628945A (en) * 1992-08-03 1997-05-13 Riman; Richard E. Multicomponent powder mixing process and compositions produced thereby
WO2000062830A2 (en) * 1999-04-19 2000-10-26 Boston Scientific Limited Coating medical devices using air suspension
US6209479B1 (en) 1998-12-30 2001-04-03 Aeromatic-Fielder Ag Apparatus for coating tablets
US6224939B1 (en) * 1998-05-22 2001-05-01 Fuisz International Ltd. Method and apparatus for forming an encapsulated product matrix
US20010012847A1 (en) * 1996-11-12 2001-08-09 Lam Andrew C. Methods and devices for providing prolonged drug therapy
US6280683B1 (en) 1997-10-21 2001-08-28 Hoeganaes Corporation Metallurgical compositions containing binding agent/lubricant and process for preparing same
US6296842B1 (en) 2000-08-10 2001-10-02 Alkermes Controlled Therapeutics, Inc. Process for the preparation of polymer-based sustained release compositions
US6312521B1 (en) 1998-12-14 2001-11-06 Primera Foods Corporation Apparatus and process for coating particles
US6426210B1 (en) 1991-06-26 2002-07-30 Inhale Therapeutic Systems, Inc. Storage of materials
US6479065B2 (en) 2000-08-10 2002-11-12 Alkermes Controlled Therapeutics, Inc. Process for the preparation of polymer-based sustained release compositions
US20030062641A1 (en) * 2001-08-16 2003-04-03 Niraj Vasishtha Microencapsulation using electromagnetic energy and core and shell materials with different dielectric constants and dissipation factors
US6589560B2 (en) 1995-04-14 2003-07-08 Nektar Therapeutics Stable glassy state powder formulations
US20030165614A1 (en) * 2002-03-01 2003-09-04 Henrik Hansen Coating a medical implant using a pan coater
US20030220200A1 (en) * 2002-03-26 2003-11-27 Georgia-Pacific Resins, Inc. Slow release nitrogen root treatment
USRE38385E1 (en) * 1989-02-16 2004-01-13 Nektar Therapeutics Storage of materials
US6685775B1 (en) 2002-02-19 2004-02-03 Vector Corporation Wurster air diverter
US6730349B2 (en) 1999-04-19 2004-05-04 Scimed Life Systems, Inc. Mechanical and acoustical suspension coating of medical implants
US20040115315A1 (en) * 2002-08-02 2004-06-17 Camelot Damien Michel Andre Encapsulated crystalline lactic acid
US20040131791A1 (en) * 1998-12-30 2004-07-08 Kim Torben-Walter Process for coating small bodies, including tablets
US20050208132A1 (en) * 2002-07-29 2005-09-22 Gayatri Sathyan Methods and dosage forms for reducing side effects of benzisozazole derivatives
US7140874B2 (en) 2001-08-06 2006-11-28 Southwest Research Institute Method and apparatus for testing catalytic converter durability
US20070160674A1 (en) * 2004-03-18 2007-07-12 Kitii Corporation Method for producing calcium component powder containing oil-soluble substance
US20080256782A1 (en) * 2007-04-18 2008-10-23 Ward Terence G Methods for forming a magnet in a rotor
US20080299305A1 (en) * 2004-04-07 2008-12-04 Urea Casale S.A. Fluid Bed Granulation Process
US20090061068A1 (en) * 2005-07-15 2009-03-05 Clive Edward Marshman Iron Fortified Food Product and Additive
US7744925B2 (en) 1994-12-02 2010-06-29 Quadrant Drug Delivery Limited Solid dose delivery vehicle and methods of making same
US20100189878A1 (en) * 2009-01-26 2010-07-29 Teva Pharmaceutical Industries Ltd. Processes for coating a carrier with microparticles
US7966745B2 (en) * 2003-06-26 2011-06-28 Urea Casale S.A. Fluid bed granulation process and apparatus
US8541028B2 (en) 2004-08-04 2013-09-24 Evonik Corporation Methods for manufacturing delivery devices and devices thereof
US8728528B2 (en) 2007-12-20 2014-05-20 Evonik Corporation Process for preparing microparticles having a low residual solvent volume
WO2014159318A1 (en) 2013-03-14 2014-10-02 Hoeganaes Corporation Methods for solventless bonding of metallurgical compositions
US9393192B2 (en) 2002-07-29 2016-07-19 Alza Corporation Methods and dosage forms for controlled delivery of paliperidone and risperidone
WO2018045103A1 (en) 2016-08-30 2018-03-08 Allergan, Inc. Method of manufacturing coated beads
WO2021119271A1 (en) 2019-12-10 2021-06-17 Capsugel Belgium Nv Particles containing a lipid matrix core and active ingredient
WO2021154774A1 (en) 2020-01-29 2021-08-05 Lonza Consumer Health Inc. Joint health composition and use thereof in healthy mammals
WO2023150113A1 (en) 2022-02-02 2023-08-10 Lonza Greenwood Llc Fast acting joint health composition and use thereof
WO2023172430A1 (en) 2022-03-07 2023-09-14 Lonza Greenwood Llc Method and composition for improving skin health

Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1473165A (en) * 1922-12-04 1923-11-06 Steigmeyer Frederick Seed-conditioning apparatus
US1546922A (en) * 1925-07-21 Process oe desiccation
US1725608A (en) * 1929-08-20 Process and apparatus for coating granular material
US2059983A (en) * 1932-06-27 1936-11-03 Gen Plastics Inc Method of coating abrasive particles
US2259879A (en) * 1937-10-25 1941-10-21 F E Schundler & Co Inc Lightweight mineral material
US2339932A (en) * 1941-04-10 1944-01-25 Standard Oil Dev Co Chemical process
US2349230A (en) * 1940-04-15 1944-05-16 Shell Dev Apparatus for the preparation of catalysts
US2399717A (en) * 1941-11-01 1946-05-07 Standard Oil Co Production of dust coated materials
US2447006A (en) * 1946-02-23 1948-08-17 Great Lakes Carbon Corp Production of sulfo compositions
US2459836A (en) * 1942-12-11 1949-01-25 Standard Oil Dev Co Controlling reaction temperatures
US2491632A (en) * 1944-09-09 1949-12-20 Stauffer Chemical Co Methods of producing insecticidal compositions containing relatively small quantities of 2,2-bis(p-chlorophenyl) - 1,1,1 - trichlorethane
US2493198A (en) * 1947-01-07 1950-01-03 North American Cement Corp Process for producing lightweight aggregates
US2498405A (en) * 1946-03-11 1950-02-21 Jeffrey Mfg Co Continuous vibrating reaction chamber
US2536168A (en) * 1947-09-29 1951-01-02 Clark & Clark Co Amphetamine chewing gum
US2561392A (en) * 1945-08-11 1951-07-24 Donald E Marshall Process and apparatus for treating solutions to recover and coat solid particles

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1546922A (en) * 1925-07-21 Process oe desiccation
US1725608A (en) * 1929-08-20 Process and apparatus for coating granular material
US1473165A (en) * 1922-12-04 1923-11-06 Steigmeyer Frederick Seed-conditioning apparatus
US2059983A (en) * 1932-06-27 1936-11-03 Gen Plastics Inc Method of coating abrasive particles
US2259879A (en) * 1937-10-25 1941-10-21 F E Schundler & Co Inc Lightweight mineral material
US2349230A (en) * 1940-04-15 1944-05-16 Shell Dev Apparatus for the preparation of catalysts
US2339932A (en) * 1941-04-10 1944-01-25 Standard Oil Dev Co Chemical process
US2399717A (en) * 1941-11-01 1946-05-07 Standard Oil Co Production of dust coated materials
US2459836A (en) * 1942-12-11 1949-01-25 Standard Oil Dev Co Controlling reaction temperatures
US2491632A (en) * 1944-09-09 1949-12-20 Stauffer Chemical Co Methods of producing insecticidal compositions containing relatively small quantities of 2,2-bis(p-chlorophenyl) - 1,1,1 - trichlorethane
US2561392A (en) * 1945-08-11 1951-07-24 Donald E Marshall Process and apparatus for treating solutions to recover and coat solid particles
US2447006A (en) * 1946-02-23 1948-08-17 Great Lakes Carbon Corp Production of sulfo compositions
US2498405A (en) * 1946-03-11 1950-02-21 Jeffrey Mfg Co Continuous vibrating reaction chamber
US2493198A (en) * 1947-01-07 1950-01-03 North American Cement Corp Process for producing lightweight aggregates
US2536168A (en) * 1947-09-29 1951-01-02 Clark & Clark Co Amphetamine chewing gum

Cited By (112)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2799241A (en) * 1949-01-21 1957-07-16 Wisconsin Alumni Res Found Means for applying coatings to tablets or the like
US2833241A (en) * 1955-04-18 1958-05-06 George C Crowley Machine for coating spherical objects
US3012900A (en) * 1957-04-26 1961-12-12 Phillips Petroleum Co Dusting particles of adhesive materials
US2844489A (en) * 1957-12-20 1958-07-22 Knapsack Ag Fluidized bed coating process
US3097958A (en) * 1958-06-10 1963-07-16 Chain Belt Co Fluidized coating machine
US3089824A (en) * 1959-04-30 1963-05-14 Wisconsin Alumui Res Foundatio Granulating and coating process for uniform granules
US3112220A (en) * 1960-02-26 1963-11-26 Abbott Lab Method and apparatus for coating particles
US3145146A (en) * 1961-10-31 1964-08-18 Warner Lambert Pharmaceutical Modified mannitol for pharmaceutical tablets
DE1182394B (en) * 1961-11-01 1964-11-26 Foremost Dairies Inc Process for coating pharmaceutical tablets
US3152005A (en) * 1962-03-29 1964-10-06 Dow Chemical Co Process for the preparation of pelletized solids
US3328256A (en) * 1963-05-27 1967-06-27 William E Gaunt Spherical beads and their production
US3361631A (en) * 1963-09-30 1968-01-02 Sandoz Ag Method of sugar coating pharmaceutical tablets
US3253944A (en) * 1964-01-13 1966-05-31 Wisconsin Alumni Res Found Particle coating process
US3256111A (en) * 1964-12-04 1966-06-14 Abbott Lab Method for coating tablets
US3464926A (en) * 1965-04-26 1969-09-02 Pennwalt Corp Process for encapsulation
US3635752A (en) * 1969-11-04 1972-01-18 Monsanto Co Process for the preparation of glass-concentrate capsules in a polyvinyl chloride matrix
US3849077A (en) * 1971-09-09 1974-11-19 Rhone Progil Continuous method for the recovery by condensation in the solid state of sublimable substances
US3800740A (en) * 1972-12-14 1974-04-02 Int Nickel Co Apparatus for decomposition of metal carbonyls
US4100148A (en) * 1975-06-13 1978-07-11 Rutgerswerke Aktiengesellschaft Storage-stable, very quickly hardenable, one-component sealant based on mercapto-terminated polymers
US4338878A (en) * 1980-11-26 1982-07-13 United Technologies Corporation Fluidized bed with sloped aperture plate
US5095035A (en) * 1981-07-31 1992-03-10 Eby Iii George A Flavor stable zinc acetate compositions for oral absorption
US4735015A (en) * 1983-11-25 1988-04-05 Basf Corporation Seed protective coating
US4615698A (en) * 1984-03-23 1986-10-07 Alza Corporation Total agent osmotic delivery system
US4675140A (en) * 1984-05-18 1987-06-23 Washington University Technology Associates Method for coating particles or liquid droplets
US4772477A (en) * 1986-10-17 1988-09-20 Balchem Corporation Meat acidulant
US4803092A (en) * 1986-10-17 1989-02-07 Balchem Corporation Method of acidulating a comminuted meat product
USRE39497E1 (en) * 1989-02-16 2007-02-27 Nektar Therapeutics Storage of materials
US5098893A (en) * 1989-02-16 1992-03-24 Pafra Limited Storage of materials
USRE37872E1 (en) * 1989-02-16 2002-10-08 Inhale Therapeutics Systems, Inc. Storage of materials
USRE38385E1 (en) * 1989-02-16 2004-01-13 Nektar Therapeutics Storage of materials
US5190775A (en) * 1991-05-29 1993-03-02 Balchem Corporation Encapsulated bioactive substances
US6013286A (en) * 1991-05-29 2000-01-11 Balchem Corporation Encapsulated bioactive substances
US5591373A (en) * 1991-06-07 1997-01-07 General Motors Corporation Composite iron material
US5211896A (en) * 1991-06-07 1993-05-18 General Motors Corporation Composite iron material
US6426210B1 (en) 1991-06-26 2002-07-30 Inhale Therapeutic Systems, Inc. Storage of materials
US6825031B2 (en) 1991-06-26 2004-11-30 Nektar Therapeutics Storage of materials
US5254168A (en) * 1992-06-04 1993-10-19 Howard Littman Coating apparatus having opposed atomizing nozzles in a fluid bed column
US5628945A (en) * 1992-08-03 1997-05-13 Riman; Richard E. Multicomponent powder mixing process and compositions produced thereby
US5350659A (en) * 1993-03-31 1994-09-27 Xerox Corporation Preparation of conductive toners using fluidized bed processing equipment
US7785631B2 (en) 1994-12-02 2010-08-31 Quadrant Drug Delivery Limited Solid dose delivery vehicle and methods of making same
US7744925B2 (en) 1994-12-02 2010-06-29 Quadrant Drug Delivery Limited Solid dose delivery vehicle and methods of making same
US7780991B2 (en) 1994-12-02 2010-08-24 Quadrant Drug Delivery Limited Solid dose delivery vehicle and methods of making same
US6589560B2 (en) 1995-04-14 2003-07-08 Nektar Therapeutics Stable glassy state powder formulations
US8629179B2 (en) 1996-11-12 2014-01-14 Alza Corporation Methods and devices for providing prolonged drug therapy
US9000038B2 (en) 1996-11-12 2015-04-07 Alza Corporation Methods and devices for providing prolonged drug therapy
US8163798B2 (en) 1996-11-12 2012-04-24 Alza Corporation Methods and devices for providing prolonged drug therapy
US6930129B2 (en) 1996-11-12 2005-08-16 Alza Corporation Methods and devices for providing prolonged drug therapy
US6919373B1 (en) 1996-11-12 2005-07-19 Alza Corporation Methods and devices for providing prolonged drug therapy
US20050238709A1 (en) * 1996-11-12 2005-10-27 Alza Corporation Methods and devices for providing prolonged drug therapy
US20010012847A1 (en) * 1996-11-12 2001-08-09 Lam Andrew C. Methods and devices for providing prolonged drug therapy
US9029416B2 (en) 1996-11-12 2015-05-12 Alza Corporation Methods and devices for providing prolonged drug therapy
US20100093796A1 (en) * 1996-11-12 2010-04-15 Gupta Suneel K Methods and devices for providing prolonged drug therapy
US9144549B2 (en) 1996-11-12 2015-09-29 Alza Corporation Methods and devices for providing prolonged drug therapy
US20050025832A1 (en) * 1996-11-12 2005-02-03 Alza Corporation Methods and devices for providing prolonged drug therapy
US20050025831A1 (en) * 1996-11-12 2005-02-03 Alza Corporation Methods and devices for providing prolonged drug therapy
US6280683B1 (en) 1997-10-21 2001-08-28 Hoeganaes Corporation Metallurgical compositions containing binding agent/lubricant and process for preparing same
US6602315B2 (en) 1997-10-21 2003-08-05 Hoeganaes Corporation Metallurgical compositions containing binding agent/lubricant and process for preparing same
US6224939B1 (en) * 1998-05-22 2001-05-01 Fuisz International Ltd. Method and apparatus for forming an encapsulated product matrix
US6312521B1 (en) 1998-12-14 2001-11-06 Primera Foods Corporation Apparatus and process for coating particles
US6209479B1 (en) 1998-12-30 2001-04-03 Aeromatic-Fielder Ag Apparatus for coating tablets
US20040131791A1 (en) * 1998-12-30 2004-07-08 Kim Torben-Walter Process for coating small bodies, including tablets
US20040071892A1 (en) * 1998-12-30 2004-04-15 Aeromatic-Fielder Ag Process for coating bodies, including tablets
US7429407B2 (en) 1998-12-30 2008-09-30 Aeromatic Fielder Ag Process for coating small bodies, including tablets
US6730349B2 (en) 1999-04-19 2004-05-04 Scimed Life Systems, Inc. Mechanical and acoustical suspension coating of medical implants
US7407551B2 (en) 1999-04-19 2008-08-05 Boston Scientific Scimed, Inc. Mechanical and acoustical suspension coating of medical implants
WO2000062830A3 (en) * 1999-04-19 2000-12-28 Scimed Life Systems Inc Coating medical devices using air suspension
WO2000062830A2 (en) * 1999-04-19 2000-10-26 Boston Scientific Limited Coating medical devices using air suspension
US6368658B1 (en) 1999-04-19 2002-04-09 Scimed Life Systems, Inc. Coating medical devices using air suspension
US20040089230A1 (en) * 1999-04-19 2004-05-13 Schwarz Marlene C. Mechanical and acoustical suspension coating of medical implants
EP1649937A1 (en) * 1999-04-19 2006-04-26 Boston Scientific Limited Coating medical device using air suspension
US20110034993A1 (en) * 1999-04-19 2011-02-10 Boston Scientific Scimed, Inc. Coated medical implants
US6296842B1 (en) 2000-08-10 2001-10-02 Alkermes Controlled Therapeutics, Inc. Process for the preparation of polymer-based sustained release compositions
US6479065B2 (en) 2000-08-10 2002-11-12 Alkermes Controlled Therapeutics, Inc. Process for the preparation of polymer-based sustained release compositions
US7140874B2 (en) 2001-08-06 2006-11-28 Southwest Research Institute Method and apparatus for testing catalytic converter durability
US7625201B2 (en) 2001-08-06 2009-12-01 Southwest Research Institute Method and apparatus for testing catalytic converter durability
US20080070169A1 (en) * 2001-08-06 2008-03-20 Ingalls Melvin N Method and apparatus for testing catalytic converter durability
US20030062641A1 (en) * 2001-08-16 2003-04-03 Niraj Vasishtha Microencapsulation using electromagnetic energy and core and shell materials with different dielectric constants and dissipation factors
US6881482B2 (en) 2001-08-16 2005-04-19 Southwest Research Institute Microencapsulation using electromagnetic energy and core and shell materials with different dielectric constants and dissipation factors
US6685775B1 (en) 2002-02-19 2004-02-03 Vector Corporation Wurster air diverter
US20030165614A1 (en) * 2002-03-01 2003-09-04 Henrik Hansen Coating a medical implant using a pan coater
US20040023809A1 (en) * 2002-03-26 2004-02-05 Georgia-Pacific Resins, Inc. Slow release nitrogen coating
US7213367B2 (en) 2002-03-26 2007-05-08 Georgia-Pacific Resins, Inc. Slow release nitrogen seed coat
US6936573B2 (en) 2002-03-26 2005-08-30 Georgia-Pacific Resins, Inc. Slow release nitrogen root treatment
US6936681B1 (en) 2002-03-26 2005-08-30 Georgia Pacific Resins, Inc. Slow release nitrogen fertilizer
EP2839734A2 (en) 2002-03-26 2015-02-25 Koch Agronomic Services, LLC Slow release nitrogen seed coat
US20030228981A1 (en) * 2002-03-26 2003-12-11 Georgia-Pacific Resins, Inc. Slow release nitrogen seed coat
US6900162B2 (en) 2002-03-26 2005-05-31 Georgia-Pacific Resins, Inc. Slow release nitrogen coating
US20030220200A1 (en) * 2002-03-26 2003-11-27 Georgia-Pacific Resins, Inc. Slow release nitrogen root treatment
US9393192B2 (en) 2002-07-29 2016-07-19 Alza Corporation Methods and dosage forms for controlled delivery of paliperidone and risperidone
US20050208132A1 (en) * 2002-07-29 2005-09-22 Gayatri Sathyan Methods and dosage forms for reducing side effects of benzisozazole derivatives
US7687092B2 (en) 2002-08-02 2010-03-30 Purac Biochem B.V. Encapsulated crystalline lactic acid
US20040115315A1 (en) * 2002-08-02 2004-06-17 Camelot Damien Michel Andre Encapsulated crystalline lactic acid
US7966745B2 (en) * 2003-06-26 2011-06-28 Urea Casale S.A. Fluid bed granulation process and apparatus
US20080305170A9 (en) * 2004-03-18 2008-12-11 Kitii Corporation Method for producing calcium component powder containing oil-soluble substance
US20070160674A1 (en) * 2004-03-18 2007-07-12 Kitii Corporation Method for producing calcium component powder containing oil-soluble substance
US20080299305A1 (en) * 2004-04-07 2008-12-04 Urea Casale S.A. Fluid Bed Granulation Process
US8541028B2 (en) 2004-08-04 2013-09-24 Evonik Corporation Methods for manufacturing delivery devices and devices thereof
US20090061068A1 (en) * 2005-07-15 2009-03-05 Clive Edward Marshman Iron Fortified Food Product and Additive
US7730603B2 (en) * 2007-04-18 2010-06-08 Gm Global Technology Operations, Inc. Methods for forming a magnet in a rotor
US8613131B2 (en) 2007-04-18 2013-12-24 GM Global Technology Operations LLC Methods for forming a magnet in a rotor
US20080256782A1 (en) * 2007-04-18 2008-10-23 Ward Terence G Methods for forming a magnet in a rotor
US20100199489A1 (en) * 2007-04-18 2010-08-12 Gm Global Technology Operations, Inc. Methods for forming a magnet in a rotor
US8728528B2 (en) 2007-12-20 2014-05-20 Evonik Corporation Process for preparing microparticles having a low residual solvent volume
US20100189878A1 (en) * 2009-01-26 2010-07-29 Teva Pharmaceutical Industries Ltd. Processes for coating a carrier with microparticles
US8889213B2 (en) 2009-01-26 2014-11-18 Teva Pharmaceutical Industries Ltd. Processes for coating a carrier with microparticles
WO2010085780A1 (en) 2009-01-26 2010-07-29 Teva Pharmaceutical Industries Ltd. Processes for coating a carrier with microparticles
WO2014159318A1 (en) 2013-03-14 2014-10-02 Hoeganaes Corporation Methods for solventless bonding of metallurgical compositions
WO2018045103A1 (en) 2016-08-30 2018-03-08 Allergan, Inc. Method of manufacturing coated beads
WO2021119271A1 (en) 2019-12-10 2021-06-17 Capsugel Belgium Nv Particles containing a lipid matrix core and active ingredient
WO2021154774A1 (en) 2020-01-29 2021-08-05 Lonza Consumer Health Inc. Joint health composition and use thereof in healthy mammals
WO2023150113A1 (en) 2022-02-02 2023-08-10 Lonza Greenwood Llc Fast acting joint health composition and use thereof
WO2023172430A1 (en) 2022-03-07 2023-09-14 Lonza Greenwood Llc Method and composition for improving skin health

Similar Documents

Publication Publication Date Title
US2648609A (en) Method of applying coatings to edible tablets or the like
US2799241A (en) Means for applying coatings to tablets or the like
US3117027A (en) Apparatus for coating particles in a fluidized bed
US4148325A (en) Treatment of tobacco
US3253944A (en) Particle coating process
US5721012A (en) Method for continuously coating particulate material
US2986475A (en) Apparatus and method for coating discrete solids
US5376175A (en) Method and means for uniformly coating particulate material
US2862511A (en) Apparatus for liquid treatment of granular material
US6689417B2 (en) Method for coating and drying
US4275682A (en) Peanut seed treating machine
US4050406A (en) Coating machine for confectionery, pharmaceuticals and similar products
US2044744A (en) Method of and apparatus for treating fibrous, granular or other material in loose form
US4031270A (en) Method of flocking metal articles
US2625903A (en) Sugar sanding machine for confections and the like
US3548782A (en) Means for forming a continuous coating on particles
US1946566A (en) Method of conditioning spray dried products and apparatus therefor
KR102279882B1 (en) Functionality substance coating device on the surface of confectionery
US2957519A (en) Spray drying apparatus and method
US2142568A (en) Apparatus for and method of drying gelatinous substances
CA2466589A1 (en) Coating and drying apparatus
US3422792A (en) Apparatus for applying color coating and reflective glass beads to stone
US3037297A (en) Crop dryer
US2589400A (en) Drying apparatus
US1428526A (en) Process and apparatus for treating latex