EP1795842A1 - Vorrichtung zur Konditionierung von organischen Materialien - Google Patents
Vorrichtung zur Konditionierung von organischen Materialien Download PDFInfo
- Publication number
- EP1795842A1 EP1795842A1 EP06125432A EP06125432A EP1795842A1 EP 1795842 A1 EP1795842 A1 EP 1795842A1 EP 06125432 A EP06125432 A EP 06125432A EP 06125432 A EP06125432 A EP 06125432A EP 1795842 A1 EP1795842 A1 EP 1795842A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- conditioning
- thermodynamic medium
- conditioning chamber
- organic material
- 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.)
- Granted
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Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B3/00—Preparing tobacco in the factory
- A24B3/04—Humidifying or drying tobacco bunches or cut tobacco
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/10—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers
- F26B17/107—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers pneumatically inducing within the drying enclosure a curved flow path, e.g. circular, spiral, helical; Cyclone or Vortex dryers
Definitions
- Present invention relates to the apparatus for conditioning of organic materials.
- US patent no. 5 908 032 discloses a method and apparatus for expansion of tobacco, which is using a channel in a form of letter C, wherein tobacco is transported by hot gaseous medium.
- US patent no. 5 711 086 discloses an apparatus for continuous drying in a superheated steam.
- Apparatus disclosed comprises a drying chamber and an assembly of the conveyor belts transporting material being dried.
- Superheated steam is generated inside the drying chamber from the moisture coming from the material being dried, as a result of exposing the material to hot gas or the moisture is introduced into to the chamber from the external source of the superheated steam.
- US patent no. 4 044 780 discloses an apparatus for expanding in volume of the cut tobacco, the apparatus comprises first unit increasing tobacco temperature and humidity to the state where tobacco particles open. Such apparatus comprises additionally separate unit for creating a thin layer of opened organic material particles in the gas atmosphere and a unit for rapid cooling.
- US patent no. 6 185 843 discloses a dryer where the transport of the organic material is carried out using pneumatic means.
- the shape of the inlet channel is decreasing the contact of the tobacco particles with a internal surfaces of the transport channel.
- EP patent no. 1 033 081 discloses a method of expanding the food products or tobacco using superheated steam as transport medium.
- apparatus for conditioning of organic materials comprises supplying channel connected with an inlet gate leading to the spreader placed in the conditioning chamber, the conditioning chamber is connected with outlet gate. Further the conditioning chamber is provided with channels supplying thermodynamic medium, the conditioning chamber comprises also a set o nozzles giving to the thermodynamic medium angular motion, additionally the conditioning chamber comprises an outlet discharging thermodynamic medium outside the apparatus.
- Apparatus according the invention comprises nozzles having form of slots.
- Apparatus according to the invention comprises chamber provided with a spreader of the rotary type.
- the apparatus comprises inlet gate 1a transporting an organic material to the spreader 2 .
- Spreader 2 preferably is a spreader of the rotary type, which uses centrifugal force to throw an organic material into the conditioning chamber 8 with a high speed.
- Apparatus is additionally provided with the outlet gate 1b placed at the bottom of the apparatus for conditioning to discharge the organic material into the channel 7 and further outside the apparatus for conditioning.
- Apparatus for conditioning is further provided with unit 4 , 5 , 10 supplying the thermodynamic medium into the conditioning chamber and with outlet 3 discharging an excess of thermodynamic medium outside apparatus for conditioning.
- Thermodynamic medium is supplied through channels 4 , 5 from an external source (not shown) under pressure, preferably in a range of 100Pa to 1.0MPa, in particular in a range of 100Pa to 0.5MPa.
- Thermodynamic medium is directed by the set of nozzles in a form of slots 10, which additionally intensify the movement of the thermodynamic medium stream inside the conditioning chamber 8 and give to the flow of the thermodynamic medium angular movement of high speed.
- Thermodynamic medium is discharged from the conditioning chamber 8 through the outlet 3 .
- An organic material for example tobacco is introduced into the conditioning apparatus through the channel 6 and inlet gate 1a .
- An organic material gets on spreader 2 , for example rotary spreader, which throws an organic material to be conditioned into the conditioning chamber 8 , and give to the organic material particles required speed and direction.
- the organic material particles hit the stream of thermodynamic medium of parameters being essential for exchange of the heat and mass (for example water), and change direction under the inertial force, gravity and hydrodynamic forces.
- An organic material falls into a swirl motion and gets to the outlet gate 1b .
- the outlet gate 1b allows controllable discharging of the conditioned material outside the apparatus for conditioning.
- Apparatus for conditioning of organic material is supplied, via inlet channels 4 , 5 and set of nozzles in a form of slots 10 , with the thermodynamic medium of parameters defined by the person skilled in the art of organic material conditioning.
- Thermodynamic medium inside the conditioning chamber swirls, and the main component of the process stream (conditioning stream) is preferably parallel (tangential) to the walls of the chamber.
- the thermodynamic medium is a gas, preferably steam in any form, including superheated steam in the temperature of 120°C to 320°C, preferably in a range of 170°C to 270°C.
- Thermodynamic medium can be air, preferably hot air in the temperature of 80°C do 280°C.
- Thermodynamic medium may be also any combination of aerosols and/or chemical vapors, as well as gases, for example argon, nitrogen, carbon dioxide etc, which may favorably influence the conditioning process and/or give specific organoleptic properties to the conditioned material.
- An apparatus for conditioning may be supplied with different thermodynamic medium at the same time, for example if the thermodynamic medium is air alone, preferably low humidity air, than the apparatus for conditioning being a drier.
- Speed of drying increases with the increase of the relative speed between organic material and thermodynamic medium.
- the Nusselt number increases which intensifies exchange heat and mass (for example water) between thermodynamic medium and organic material. Described above process parameters can be controlled by adjusting speed of circulation for thermodynamic medium or by adjusting time period of exposing the organic material to thermodynamic medium.
- Thermodynamic medium could be chosen from the group comprising nitrogen, argon, carbon dioxide or other non reactive gas, then apart from intensive drying the thermodynamic medium can be heated to the temperature above ignition point of the organic material being dried, this allows not only drying but also allows expansion (swelling) of the organic material.
- thermodynamic medium is a steam with a small addition of air
- organic material after introducing into an apparatus is moistened to the point where no condensation appears. This leads to increase of the humidity of an organic material.
- the organic material can be expanded, and than dried to achieve final humidity.
- the additional steam can be supplied by additional set of nozzles (not shown) placed just behind the inlet gate 1a .
- An apparatus for conditioning of organic materials may be supplied with many different thermodynamic mediums in many different conditioning processes or can be supplied with many different thermodynamic mediums in a single conditioning process.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Catching Or Destruction (AREA)
- Working-Up Tar And Pitch (AREA)
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
- Soil Working Implements (AREA)
- Formation And Processing Of Food Products (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL06125432T PL1795842T3 (pl) | 2005-12-06 | 2006-12-05 | Urządzenie do kondycjonowania materiału pochodzenia roślinnego |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL378286A PL378286A1 (pl) | 2005-12-06 | 2005-12-06 | Urządzenie do kondycjonowania materiału pochodzenia roślinnego |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1795842A1 true EP1795842A1 (de) | 2007-06-13 |
EP1795842B1 EP1795842B1 (de) | 2010-04-07 |
Family
ID=37734933
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06125432A Not-in-force EP1795842B1 (de) | 2005-12-06 | 2006-12-05 | Vorrichtung zur Konditionierung von organischen Materialien |
Country Status (5)
Country | Link |
---|---|
US (1) | US20070125394A1 (de) |
EP (1) | EP1795842B1 (de) |
AT (1) | ATE463708T1 (de) |
DE (1) | DE602006013393D1 (de) |
PL (2) | PL378286A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9889978B2 (en) | 2013-12-17 | 2018-02-13 | Aptar Radolfzell Gmbh | Protective cap for a dispenser and dispenser for discharging pharmaceutical and/or cosmetic liquids |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018029536A1 (en) * | 2016-08-10 | 2018-02-15 | Gary Stephen Shuster | Vaporization improvements |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4532155A (en) * | 1983-08-08 | 1985-07-30 | G. D. Searle & Co. | Apparatus and process for coating, granulating and/or drying particles |
WO1989000014A1 (en) * | 1987-07-02 | 1989-01-12 | Gbe International Plc | Apparatus for expanding and/or drying particulate material |
EP0871003A1 (de) * | 1995-12-30 | 1998-10-14 | Nara Machinery Co., Ltd. | Verfahren und vorrichtung zur trocknung von pulverisierten material |
WO1999023898A1 (en) * | 1997-11-10 | 1999-05-20 | Idea S.N.C. Di Mastrolilli Anna E.C. | New machinery for casing and moistening tobacco |
US6158145A (en) * | 1998-02-27 | 2000-12-12 | Landon; Frank D. | Method for a high turbulence cyclonic dryer |
GB2355058A (en) * | 1999-09-25 | 2001-04-11 | J E Elsworth Ltd | Dryer having rotary base and stationary cylindrical walls for drying coated small particles |
WO2003047360A1 (en) * | 2001-12-03 | 2003-06-12 | Mars Incorporated | Coating and drying apparatus |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1667288A1 (de) * | 1967-01-25 | 1972-03-16 | Buettner Schilde Haas Ag | Vorrichtung fuer den Energie- oder/und Stoffaustausch mit Feststoffteilchen |
US3600817A (en) * | 1969-11-28 | 1971-08-24 | Siemens Ag | Processing apparatus for effecting interaction between, and subsequent separation or gaseous and solid or liquid particulate substances |
US4253474A (en) * | 1978-03-31 | 1981-03-03 | American Brands, Inc. | Method for expanding tobacco |
DE3108875A1 (de) * | 1981-03-09 | 1982-09-16 | Kraftwerk Union AG, 4330 Mülheim | Drehstroemungswirbler zur thermischen behandlung von feinkoernigem oder granulatfoermigem gut |
US4599809A (en) * | 1984-09-13 | 1986-07-15 | Shivvers, Incorporated | Grain dryer system |
US4791942A (en) * | 1986-08-01 | 1988-12-20 | The American Tobacco Company | Process and apparatus for the expansion of tobacco |
DE3869793D1 (de) * | 1987-01-27 | 1992-05-14 | Asahi Glass Co Ltd | Gaszufuehrungsrohr fuer die reaktive abscheidung aus der gasphase. |
EP0835066B1 (de) * | 1995-06-10 | 1999-09-29 | Rudolf Bichsel | Verfahren und vorrichtung zum puffen von nahrungsmitteln |
DE10038114A1 (de) * | 2000-08-04 | 2002-02-21 | Bat Cigarettenfab Gmbh | Verfahren und Vorrichtung zur Konditionierung von zerkleinerten Tabakmaterialien |
-
2005
- 2005-12-06 PL PL378286A patent/PL378286A1/pl not_active Application Discontinuation
-
2006
- 2006-12-05 EP EP06125432A patent/EP1795842B1/de not_active Not-in-force
- 2006-12-05 DE DE602006013393T patent/DE602006013393D1/de active Active
- 2006-12-05 AT AT06125432T patent/ATE463708T1/de not_active IP Right Cessation
- 2006-12-05 PL PL06125432T patent/PL1795842T3/pl unknown
- 2006-12-06 US US11/634,205 patent/US20070125394A1/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4532155A (en) * | 1983-08-08 | 1985-07-30 | G. D. Searle & Co. | Apparatus and process for coating, granulating and/or drying particles |
WO1989000014A1 (en) * | 1987-07-02 | 1989-01-12 | Gbe International Plc | Apparatus for expanding and/or drying particulate material |
EP0871003A1 (de) * | 1995-12-30 | 1998-10-14 | Nara Machinery Co., Ltd. | Verfahren und vorrichtung zur trocknung von pulverisierten material |
WO1999023898A1 (en) * | 1997-11-10 | 1999-05-20 | Idea S.N.C. Di Mastrolilli Anna E.C. | New machinery for casing and moistening tobacco |
US6158145A (en) * | 1998-02-27 | 2000-12-12 | Landon; Frank D. | Method for a high turbulence cyclonic dryer |
GB2355058A (en) * | 1999-09-25 | 2001-04-11 | J E Elsworth Ltd | Dryer having rotary base and stationary cylindrical walls for drying coated small particles |
WO2003047360A1 (en) * | 2001-12-03 | 2003-06-12 | Mars Incorporated | Coating and drying apparatus |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9889978B2 (en) | 2013-12-17 | 2018-02-13 | Aptar Radolfzell Gmbh | Protective cap for a dispenser and dispenser for discharging pharmaceutical and/or cosmetic liquids |
Also Published As
Publication number | Publication date |
---|---|
PL1795842T3 (pl) | 2010-09-30 |
DE602006013393D1 (de) | 2010-05-20 |
ATE463708T1 (de) | 2010-04-15 |
PL378286A1 (pl) | 2007-06-11 |
US20070125394A1 (en) | 2007-06-07 |
EP1795842B1 (de) | 2010-04-07 |
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