US3601321A - Process for preparing granular denture cleanser - Google Patents

Process for preparing granular denture cleanser Download PDF

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Publication number
US3601321A
US3601321A US815635A US3601321DA US3601321A US 3601321 A US3601321 A US 3601321A US 815635 A US815635 A US 815635A US 3601321D A US3601321D A US 3601321DA US 3601321 A US3601321 A US 3601321A
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United States
Prior art keywords
composition
granular
oversized
particles
granules
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Expired - Lifetime
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US815635A
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English (en)
Inventor
Jordan B Barth
Philip A Ouellette
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PHILIP A OUELLETTE
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PHILIP A OUELLETTE
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    • 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
    • B01J2/22—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by pressing in moulds or between rollers
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/02—Cosmetics or similar toiletry preparations characterised by special physical form
    • A61K8/0216—Solid or semisolid forms
    • A61K8/022—Powders; Compacted Powders
    • A61K8/0225—Granulated powders
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q11/00—Preparations for care of the teeth, of the oral cavity or of dentures; Dentifrices, e.g. toothpastes; Mouth rinses
    • A61Q11/02—Preparations for deodorising, bleaching or disinfecting dentures
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
    • A61K2800/20—Chemical, physico-chemical or functional or structural properties of the composition as a whole
    • A61K2800/22—Gas releasing
    • A61K2800/222—Effervescent

Definitions

  • the process comprises homogenizing and levigating the powdered components of the composition, extruding the composition mixture into a dense sheet of material and grinding the sheet of material into granules of a desired particle size. Granules of the desired size are then separated from oversized and undersized particles and collected as product while the oversized and undersized particles are reprocessed.
  • This invention relates to granular denture cleansing compositions, and more particularly to a process for preparing granular denture cleansing compositions which when dissolved in water remove stains, plaque, food particles, and the like from removable dentures.
  • Denture cleanser soak formulas of the effervescent, gas liberating-type have generally been prepared as powders and tablets in preference to the granular form because of certain attendant disadvantages in the conventional prior art methods of granulation.
  • One method of granulating requires the formation of a paste or slurry of the material, and drying and pulverizing to form a granular product whose shelf life as an effervescent and gas liberating agent is limited because of exposure during the several steps to wetting agents, drying temperatures and oxidative conditions. This process, known as wet granulation, requires long processing times, many consecutive steps and costly equipment, power consumption and floor space. Wet granulations were found to be ineffective for the preparation of the product, presumably because the oxidizing agents reduced the amounts of granules formed.
  • Another method consists of incorporating a granulating agent, for example, a polar organic compound having an alcoholic hydroxyl group as its only polar radical, into a flowable paste of the composition and thereafter aerating and mixing the paste until nodules form in a partially solidified mass which is subsequently aged until it rigidifies after which time the mass is granulated.
  • a third method involves merely mixing the anhydrous components of the composition with a binding agent, such as a high molecular weight polyvinylpyrrolidone (PVP).
  • PVP high molecular weight polyvinylpyrrolidone
  • the former procedure necessitates costly equipment, extensive handling by workers and consequently, a high manufacturing cost.
  • both the former method and the latter method make use of an adulterant in the final composi tion; Many binding agents, except PVP, were found to react with the oxidizing agents, and are therefore, unacceptable.
  • denture cleansing compositions continue to be powders and tablets, notwithstanding the fact that powder and denture cleansers are highly susceptible to caking when placed in a moisture laden atmosphere as commonly exists in bathrooms, and that tablet forms of denture cleansers are generally more expensive to manufacture due to the final molding step in the manufacturing process.
  • the molding of the tablets further requires the addition of lubricating agents to the composition.
  • tablets are inherently not readily capable of fast effervescing when placed in an aqueous solution because of their slow breakdown and poor solubility in water, and therefore the well-known technique of adding carbonating agents, such as tartaric acid and sodium carbonate or bicarbonate, to the tablet composition is commonly employed to increase effervescence.
  • the great quantity of a carbonating agent or agents used in the tablets compositions has a serious disadvantage such that when used with oxygen liberating components the cleansing properties of the composition are impaired and tablets with short shelf lives are obtained. Further, a tablet containing citric acid and N HCO still takes longer to dissolve than the granules because of surface area effects.
  • the exposure of effervescing compositions to moisture impairs the ability of the powder to bubble when placed in water which therefore reduces the ability of the components of the composition to disperse quickly and uniformly throughout the solution medium and thus the cleansing action of the composition is lowered.
  • the addition of various agents to such compositions to reduce the aforementioned problems may form scumming and unclear, cloudy solutions of the composition in water.
  • a further object of this invention resides in the provision of a process for preparing a denture cleanser of the effervescent, gas liberating-type which does not require the use of wetting agents, caking preventatives, binding or granulating agents, and which process produces a granular denture cleanser which shows no tendency to form a scum, and provides clear, noncloudy solutions when added to water.
  • a process for producing a free flowing granular denture cleansing composition of the highly effervescent, gas liberating type includes the conventional organic acid and metal carbonate or bicarbonate, the various components are combined in a manner which will prevent all of the foregoing problems attendant upon powdered and tablet forms of denture cleansers as well as the granulated forms which have heretofore been prepared.
  • the several dry components of the denture cleansing composition are first mixed together as powders, the components include for example an organic acid or other substance which reacts to evolve carbon dioxide when dissolved in water, a compound which releases oxygen upon addition to water and various other substances including minor proportions of a detergent, a dye, and/or flavoring agents.
  • the powders are combined and homogenized before feeding to a device which partially compresses and deaerates the mixture.
  • the thus pretreated mixture is fed between two compression or compaction rolls which are closely spaced to one another and which rotate in opposite directions toward the direction which the composition, now densified into a sheet, travels.'This sheet of compacted material is broken first into chips and flake s and then into finely divided particles of the predetermined range of desired sizes by subjecting to the grinding action of revolving rotary blades.
  • the particulate material is screened to remove dust and other contaminants and then sorted into particles of the desired size which constitutes the finished product and the oversized and undersized granules which do not conform to the desired size.
  • the oversized and undersized granules may be recycled back into the original feed system.
  • FIG. 1 is a front elevational view partly in section of an apparatus which will produce the granular denture cleansing composition in accordance with the process of this invention, parts, being broken away to show other parts in detail;
  • FIG. 2 is a side elevational view partly in section of the apparatus shown in FIG. 1, parts being broken away to show other parts in detail;
  • FIG. 3 is a top plan view partly in section in of the apparatus seen in FIG. 1, parts being broken away to show other parts in detail;
  • FIG. 4 is a fragmentary rear elevational view of the apparatus seen in FIG. 1 and taken along the plane of line 4-4 in FIG. 2; and,
  • FIG. 5 is a diagrammatic view of a modification of the process performed by the apparatus shown in FIG. 1, showing the addition of several intermediate steps in the process for producing the granular denture cleansing composition in accordance with this invention.
  • reference numeral is generally used to designate the preferred type of apparatus to be used in carrying out the process of the invention.
  • the several components of the denture cleansing composition are fed to the apparatus in dry powdered form at the lower hopper 12 and then into the main flow stream of the system, designated by the direction of arrow 14, where the mixture of powders is homogenized and levigated as it travels along its path under the pressure created by a columnated backup of material in conduits l6, l8 and 20.
  • the feed is then carried to a second hopper 22 from which it falls by gravity onto a rotating horizontal feed screw 24 which transports the preprocessed composition to a rotating vertical screw 26 for compressing and deaerating the composition prior to granulating it.
  • the material falls into the gap created between two closely spaced pressurized compression rolls 28 rotating clockwise and counterclockwise, respectively, so that adjacent the space therebetween they are both moving in a downward direction.
  • a continuous narrow sheet of dense compacted material flows from beneath the compression rolls 28 and is then subjected to a grinding action by rotary blades revolving about the central axis of shaft 30 whereby the material is first broken into chips and flakes before forming granules of a size within a predetermined range of sizes.
  • Main flow stream 14 comprises a series of connecting conduits l6, l8 and 20.
  • the powdered components of the denture cleansing composition are initially fed to lower hopper l2 and fall by gravity onto a rotating horizontal screw 44 at the bottom of hopper 12 which extends into conduit 16.
  • Conduit 16 communicates with vertical conduit 18 containing another screw 46 rotating therein.
  • Rotating screws 44 and 46 serve to blend the mixture of components and as material is continuously fed to the system the increased pressure of material within conduits 16 and 18 causes the column of material to rise until it reaches the top of conduit 18 and fall through conduit 20 into hopper 22.
  • a bucket elevator can be employed.
  • the new homogenized mixture of components is swept onto rotating horizontal screw 24 and through conduit 48 into which screw 24 extends and finally is subjected to the shearing and compacting action of vertical screw 26 rotating within conduit 50.
  • the thus preprocessed mixture falls from the bottom 52 of conduit 50 into the gap 54 created by the closely spaced pair of compression rolls 28 which are under externally applied air pressure exerted by piston 56 which in one embodiment is regulated by a hydraulic actuator. As the thoroughly levigated mixture passes between the pressurized rotating rolls 28 it is compacted into a very dense sheet of material.
  • the sheet of material is then subjected to the grinding action of rotary blades, not seen, revolving about the axis of shaft 30 which is driven by motor 57.
  • the sheet is broken into chips and flakes of the composition and then into smaller granular size particles within a desired range of sizes.
  • the granules are able to pass through the holes in screen 32 whereas the larger size particles remain behind to be further broken down to the desired particle size.
  • the particles of denture cleansing composition are classified by sorter 36 into granular product of the desired particle size and the oversized and undersized particles, Product passes from sorter 36 through outlet 42 into a suitable collection vessel, not shown.
  • the oversized and undersized particles leave sorter 36 through outlet 38 and reenter the main flow stream 14 through conduit 40 for further processing.
  • the described apparatus occupies a minimum of plant floor space. Furthermore, the process is one which requires relatively little handling by the operator in that powdered material is merely fed into hopper 12 and granular product is removed at outlet 42. Therefore, notwithstanding the maintenance of the apparatus and the control of the feed rate, piston pressure, etc. by turning the appropriate knob 58 or pushing the correct button 60 on control panel 62, the operative steps to be handled by personnel are limited to the barest minimum. Finally, the cost of equipment is nominal because it is paid back through the other savings to the manufacturer in a relatively short period of time.
  • FIG. 5 there is seen a diagrammatic of another apparatus for preparing the granular denture cleansing composition by a modified form of the apparatus.
  • the several components of the composition are fed to the system in powdered form through a hopper 64 and into the main flow stream designated by reference numeral 66, comprising conduits 67, 68 and 70.
  • Conduits 66 and 68 contain rotating screws, not seen, which thoroughly blend and homogenize the components of the mixture.
  • the partially processed mixture then enters hopper 72 and falls onto rotating horizontal screw 74, disposed at the bottom of hopper 72, which extends into conduit 76 that communicates with conduit 78 containing rotating vertical screw 80.
  • Horizontal screw 74 feeds the mixture to vertical screw 80 at a controlled rate, whereupon vertical screw 80 precompresses and deaerates the mixture by shear forces. Closely spaced revolving compression rolls 82 under pressure applied by piston 84 force the material downwardly while the pressure compacts the mixture into a dense sheet of material 83. Subsequently, the sheet falls onto rotary blades 86 revolving in the direction of arrow 87 where it undergoes a preliminary chopping action which breaks the sheet into flakes and larger than granule size particles. These prebroken particles of material are more finely ground by a second set of rotary blades 88 rotating in the direction of arrow 89 in which operation granular sized particles are formed.
  • Screen 90 permits only the granular sized particles to pass through it and the flakes or larger particles remain behind to be further broken down.
  • the granular sized particles are ready to be classified by sorter 94 into granules of a size within a predetermined range of permissible sizes, i.e.., the product, and granules which are oversized or undersized.
  • Sorter 94 consists of screens 96 and 98, screen 96 having a mesh size which allows the maximum permissible size of product granule to pass through it.
  • a granular denture cleansing composition prepared by the method of this invention is free flowing and dustless. It dissolves quickly in water to form an effervescing solution which will cleanse removable dentures soaking in the solution.
  • One such composition that has been successfully prepared by this process consists of 21.50 percent by weight of tartaric acid, 34.14 percent by weight of sodium bicarbonate, 28.00 percent by weight of oxone (KHSO 15.00 percent by weight of NaBO .H b02, 0.10 percent by weight of the sodium salt of an alkyl benzene sulfonate, 1.25 percent by weight of a flavor mix consisting of 1.00 percent magnesium carbonate and 0.25 percent flavor oils, and 0.01 percent by weight of a red dye.
  • a process for preparing a granular composition for cleaning dentures which composition efiervesces and liberates oxygen upon dissolution in water comprising the steps of feeding the components of said composition through a cylinder containing a screw rotating therein for compressing and deaerating said components in powdered form, extruding said composition into a dense sheet of material, breaking said dense sheet of material into chips and flakes, grinding said chips and flakes by rotary blades into granules of approximately the desired particle size, and then sorting the granular product of desired particle size from oversized and undersized particles of said composition.

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Epidemiology (AREA)
  • Oral & Maxillofacial Surgery (AREA)
  • Birds (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Cosmetics (AREA)
  • Dental Preparations (AREA)
  • Glanulating (AREA)
US815635A 1969-04-14 1969-04-14 Process for preparing granular denture cleanser Expired - Lifetime US3601321A (en)

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US81563569A 1969-04-14 1969-04-14

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US (1) US3601321A (da)
BE (1) BE748386A (da)
CH (1) CH505623A (da)
DE (1) DE2014651A1 (da)
DK (1) DK128879B (da)
FR (1) FR2043282A5 (da)
GB (1) GB1292519A (da)
NL (1) NL7005369A (da)
ZA (1) ZA701807B (da)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992013633A1 (de) * 1991-02-11 1992-08-20 Paul Gerteis Verfahren und vorrichtung zum kontinuierlichen mechanischen umformen von teilchenförmigen stoffen
US5263650A (en) * 1991-05-09 1993-11-23 Kao Corporation Process for producing high bulk density granular detergent
US5405091A (en) * 1992-08-17 1995-04-11 F. L. Smidth & Co., A/S Method for grinding of material
US5509612A (en) * 1991-02-11 1996-04-23 Gerteis; Paul Process and device for the continuous shaping of particulate materials
WO1997017939A1 (en) * 1995-11-11 1997-05-22 The Procter & Gamble Company Silicone containing powders
US5667158A (en) * 1995-05-23 1997-09-16 Glaxo Wellcome Inc. Automated blend reclaim system for pharmaceutical tablet compression machine
US6274122B1 (en) * 1999-01-07 2001-08-14 Mclaughlin Gerald Device and method using dry mixtures for whitening teeth
US6440926B1 (en) * 1997-04-14 2002-08-27 The Procter & Gamble Company Effervescent compositions and dry effervescent granules
US20030099603A1 (en) * 2001-03-19 2003-05-29 Jayanth Rajaiah Polybutene containing denture cleanser compositions
US20040131561A1 (en) * 2001-03-14 2004-07-08 Mclaughlin Gerald Strips for treating teeth
US20050006491A1 (en) * 2003-06-16 2005-01-13 Jung-Ming Lin Method of increasing the raining amounts in the desert and the apparatus thereof
US20110220745A1 (en) * 2008-11-05 2011-09-15 Polibiotech Srl Dry granulation in a gas stream
CN102696588A (zh) * 2012-06-08 2012-10-03 上海市农药研究所 用挤压法生产农药水分散粒剂的方法及装置
CN108480021A (zh) * 2018-04-18 2018-09-04 肖叶 一种用于制药的高效粉碎机
US11346825B2 (en) * 2019-09-30 2022-05-31 Industrial Test Systems, Inc. Arsenic analysis

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2614219B1 (fr) * 1987-04-23 1993-07-09 Materiels Annexes Dialyse Procede de fabrication de granules destines a la preparation de solutions de dialyse et installation pour sa mise en oeuvre.
US5855869A (en) * 1996-12-31 1999-01-05 Rhodia Inc. Microparticulate abrasives
WO1998035751A1 (en) * 1997-02-14 1998-08-20 J.M. Huber Corp. Method of making a silica carrier for liquid and product
CN102896035A (zh) * 2012-09-29 2013-01-30 中国电器科学研究院有限公司 一种粉末涂料片料的磨粉设备
CN113101869B (zh) * 2021-04-22 2022-10-11 广东嘉美好生态科技有限公司 一种自动化生物肥料造粒机

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2461089A (en) * 1944-06-22 1949-02-08 Smidth Leonard Process of forming granulated synthetic resin compositions
US3114930A (en) * 1961-03-17 1963-12-24 American Cyanamid Co Apparatus for densifying and granulating powdered materials

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2461089A (en) * 1944-06-22 1949-02-08 Smidth Leonard Process of forming granulated synthetic resin compositions
US3114930A (en) * 1961-03-17 1963-12-24 American Cyanamid Co Apparatus for densifying and granulating powdered materials

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5509612A (en) * 1991-02-11 1996-04-23 Gerteis; Paul Process and device for the continuous shaping of particulate materials
WO1992013633A1 (de) * 1991-02-11 1992-08-20 Paul Gerteis Verfahren und vorrichtung zum kontinuierlichen mechanischen umformen von teilchenförmigen stoffen
US5263650A (en) * 1991-05-09 1993-11-23 Kao Corporation Process for producing high bulk density granular detergent
US5405091A (en) * 1992-08-17 1995-04-11 F. L. Smidth & Co., A/S Method for grinding of material
US5667158A (en) * 1995-05-23 1997-09-16 Glaxo Wellcome Inc. Automated blend reclaim system for pharmaceutical tablet compression machine
WO1997017939A1 (en) * 1995-11-11 1997-05-22 The Procter & Gamble Company Silicone containing powders
US6440926B1 (en) * 1997-04-14 2002-08-27 The Procter & Gamble Company Effervescent compositions and dry effervescent granules
US6274122B1 (en) * 1999-01-07 2001-08-14 Mclaughlin Gerald Device and method using dry mixtures for whitening teeth
US20070077533A1 (en) * 2001-03-14 2007-04-05 Mclaughlin Gerald Strips for treating teeth
US20040131561A1 (en) * 2001-03-14 2004-07-08 Mclaughlin Gerald Strips for treating teeth
US20030099603A1 (en) * 2001-03-19 2003-05-29 Jayanth Rajaiah Polybutene containing denture cleanser compositions
US20050006491A1 (en) * 2003-06-16 2005-01-13 Jung-Ming Lin Method of increasing the raining amounts in the desert and the apparatus thereof
US20110220745A1 (en) * 2008-11-05 2011-09-15 Polibiotech Srl Dry granulation in a gas stream
US8590818B2 (en) * 2008-11-05 2013-11-26 Polibiotech Srl Dry granulation in a gas stream
CN102696588A (zh) * 2012-06-08 2012-10-03 上海市农药研究所 用挤压法生产农药水分散粒剂的方法及装置
CN102696588B (zh) * 2012-06-08 2016-03-16 上海市农药研究所 用挤压法生产农药水分散粒剂的方法及装置
CN108480021A (zh) * 2018-04-18 2018-09-04 肖叶 一种用于制药的高效粉碎机
US11346825B2 (en) * 2019-09-30 2022-05-31 Industrial Test Systems, Inc. Arsenic analysis

Also Published As

Publication number Publication date
FR2043282A5 (da) 1971-02-12
GB1292519A (en) 1972-10-11
CH505623A (de) 1971-04-15
NL7005369A (da) 1970-10-16
DE2014651A1 (de) 1970-10-15
DK128879B (da) 1974-07-22
ZA701807B (en) 1971-10-27
BE748386A (fr) 1970-09-16

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