DE4037866C2 - Continuous fluidized bed process for gentle drying of temperature-sensitive, moist products - Google Patents
Continuous fluidized bed process for gentle drying of temperature-sensitive, moist productsInfo
- Publication number
- DE4037866C2 DE4037866C2 DE19904037866 DE4037866A DE4037866C2 DE 4037866 C2 DE4037866 C2 DE 4037866C2 DE 19904037866 DE19904037866 DE 19904037866 DE 4037866 A DE4037866 A DE 4037866A DE 4037866 C2 DE4037866 C2 DE 4037866C2
- Authority
- DE
- Germany
- Prior art keywords
- temperature
- fluidized bed
- moist
- product
- products
- 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 - Fee Related
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/32—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
- F26B3/34—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
- F26B3/343—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects in combination with convection
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
- F26B3/08—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
Description
Kontinuierliches Wirbelschichtverfahren zur schonenden Trocknung von temperaturempfindlichen feuchten Produkten, wobei die feuchten Produkte in das fluidisierte Wirbelgut in einem Wirbelbetttrockner (= feuchtes, zu trocknendes Produkt) eindosiert und bei Temperaturen unterhalb der Siede temperatur des Lösungsmittels getrocknet werden, die Steuerung der Pro dukttemperatur in der Wirbelschicht durch den Massenstrom und die Tempera tur des Wirbelgases sowie durch den Massenstrom des Produktes erfolgt, die Abführung der Brüden des Lösungsmittels durch das Wirbelgas erfolgt und die getrockneten Endprodukte aus der Wirbelschicht ausgetragen werden.Continuous fluidized bed process for gentle drying of temperature sensitive wet products, the wet products in the fluidized fluidized material in a fluidized bed dryer (= moist, too drying product) and at temperatures below the boiling point temperature of the solvent can be dried, the control of the Pro product temperature in the fluidized bed through the mass flow and the tempera Turbine of the fluidizing gas and by the mass flow of the product, The vapors of the solvent are removed by the fluidizing gas and the dried end products are discharged from the fluidized bed.
Zur Trocknung von temperaturempfindlichen, feuchten Produkten kommen bekannte Verfahren, wie beispielsweise konvektive Trocknungsverfahren oder Vakuumtrocknungsverfahren zum Einsatz.Come to dry temperature-sensitive, moist products known processes, such as, for example, convective drying processes or Vacuum drying process used.
Beide Verfahren haben jedoch verschiedene Nachteile.However, both methods have different disadvantages.
Des weiteren wird in der Dissertation von T. Köblitz, Universität Erlangen-Nürnberg, Jahr 1984, "Die schonende Trocknung von temperatur empfindlichen Granulaten im Hochfrequenzfeld" beschrieben.Furthermore, in the dissertation by T. Köblitz, University Erlangen-Nürnberg, year 1984, "The gentle drying of temperature sensitive granules in the radio frequency field ".
Hierbei wird die schonende Trocknung von temperaturempfindlichen Pharma produkten mit einem Hochfrequenzfeld in einem Vibrationsfließbild bei kleinen Schütthöhen - ≦ 20 mm - aufgezeigt.This involves gentle drying of temperature-sensitive pharmaceuticals products with a high-frequency field in a vibration flow diagram small dumping heights - ≦ 20 mm - shown.
Die Wirbelschicht wird hierbei mechanisch erzeugt und ein durch die wirbelnde Produktschicht hindurch geleiteter Gasstrom dient ausschließlich zur schnellen Abfuhr der Brüden.The fluidized bed is generated mechanically and by the swirling product layer gas flow passed through serves exclusively for quick evacuation of the brothers.
Dieses Verfahren hat jedoch folgende Nachteile:
der konvektive Trocknungsanteil bei der Trocknung fehlt,
der geringe Gasstrom dient nur zur Brüdenabfuhr,
eine definierte Steuerung der Produkttemperatur in der Wirbelschicht ist
nicht möglich,
die Wirbelschicht wird ausschließlich über Vibration - mechanischer
Energieeintrag - erzeugt und
es können nur sehr kleine Schichthöhen gefahren werden, da sonst die
Gefahr der Überhitzung des zu trocknenden Produkts mit den bekannten
Nachteilen für die Produktqualität gegeben ist.However, this method has the following disadvantages:
the convective part of the drying process is missing,
the low gas flow only serves to remove the vapors,
Defined control of the product temperature in the fluidized bed is not possible
the fluidized bed is generated exclusively via vibration - mechanical energy input - and
only very small layer heights can be used, since otherwise there is a risk of the product to be dried overheating with the known disadvantages for the product quality.
Es stellte sich daher die Aufgabe, ein Verfahren zu entwickeln, das eine schonende Trocknung von temperaturempfindlichen Produkten in der Wirbel schicht - bei Vermeidung der oben aufgezeigten Nachteile - ermöglicht.It was therefore the task to develop a method that gentle drying of temperature-sensitive products in the vortex layer - while avoiding the disadvantages shown above - enables.
Diese Aufgabe wird in Verbindung mit den Merkmalen des Oberbegriffs des Anspruchs 1 erfindungsgemäß dadurch gelöst, daß die Trocknung durch dielektrische Erwärmung der feuchten Produkte mittels eines Hochfrequenz feldes und die Temperaturführung über die Wirbelgaseintrittstemperatur erfolgt.This object is achieved in connection with the features of the preamble of claim 1 in that the drying by dielectric heating of the moist products by means of a high frequency field and the temperature control over the fluidizing gas inlet temperature he follows.
Ein Ausführungsbeispiel der Erfindung mit den wesentlichen, erfinderischen Merkmalen ist in der Zeichnung dargestellt und wird im folgenden näher beschrieben.An embodiment of the invention with the essential, inventive Features are shown in the drawing and will be described in more detail below described.
Die Zeichnung zeigt einen Wirbelbetttrockner 1 mit dem fluidisierten Wirbelgut 2 (= feuchtes, zu trocknendes Produkt). Das Wirbelgas 3 wird über einen Wärmetauscher 4 erwärmt und über einen Verteilerboden 1a im Wirbelbetttrockner verteilt. Durch den Filter 1b hindurch verlassen Wirbelgas 5 und mitgeführte Brüden des Lösungsmittels den Wirbelbett trockner. Eintritt des feuchten, zu trocknenden Produktes in den Wirbel betttrockner und Abzug des getrockneten Produktes aus dem Wirbelbett trockner erfolgen über Rohrleitungen und bekannte Förderorgane 6 und 7. Der Wirbelbetttrockner ist innerhalb einer Einrichtung 8 zur Erzeugung eines Hochfrequenzfeldes angeordnet. Mittels dieses Hochfrequenzfeldes wird erfindungsgemäß durch dielektrische Erwärmung das feuchte Produkt getrocknet.The drawing shows a fluidized bed dryer 1 with the fluidized fluidized material 2 (= moist product to be dried). The fluidizing gas 3 is heated via a heat exchanger 4 and distributed in the fluidized bed dryer via a distributor base 1 a. Through the filter 1 b fluidizing gas 5 and entrained vapors of the solvent leave the fluid bed dryer. Entry of the moist product to be dried into the fluidized bed dryer and removal of the dried product from the fluidized bed dryer take place via pipelines and known conveying elements 6 and 7 . The fluidized bed dryer is arranged within a device 8 for generating a high-frequency field. Using this high-frequency field, the moist product is dried according to the invention by dielectric heating.
Die oben aufgezeigte kontinuierliche Fahrweise unterscheidet sich im Ver gleich zur diskontinuierlichen Fahrweise nur dadurch, daß das zu trock nende Produkt nicht in das fluidisierte Wirbelgut eindosiert sind, sondern in dem Wirbelbetttrockner vorgelegt wird.The continuous driving style shown above differs in Ver equal to the discontinuous driving style only in that it is too dry product are not metered into the fluidized fluidized bed, but rather is placed in the fluidized bed dryer.
Es versteht sich von selbst, daß bei großtechnischen Produktionsanlagen nicht der gesamte Wirbelbetttrockner in ein Hochfrequenzfeld eingebettet wird, sondern die dielektrische Erwärmung der feuchten Produkte mittels handelsüblicher Magnetrons - angeordnet im eigentlichen Wirbelbettraum - erreicht wird.It goes without saying that in large-scale production plants not the entire fluid bed dryer is embedded in a high-frequency field is, but the dielectric heating of the moist products by means of commercially available magnetrons - arranged in the actual fluidized bed room - is achieved.
Claims (2)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19904037866 DE4037866C2 (en) | 1990-11-28 | 1990-11-28 | Continuous fluidized bed process for gentle drying of temperature-sensitive, moist products |
FR9114550A FR2669718B1 (en) | 1990-11-28 | 1991-11-26 | CONTINUOUS PROCESS IN A TURBULENT LAYER FOR DRYING WITH THE MANAGEMENT OF WET PRODUCTS SENSITIVE TO TEMPERATURE. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19904037866 DE4037866C2 (en) | 1990-11-28 | 1990-11-28 | Continuous fluidized bed process for gentle drying of temperature-sensitive, moist products |
Publications (2)
Publication Number | Publication Date |
---|---|
DE4037866A1 DE4037866A1 (en) | 1992-06-04 |
DE4037866C2 true DE4037866C2 (en) | 2000-05-18 |
Family
ID=6419095
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19904037866 Expired - Fee Related DE4037866C2 (en) | 1990-11-28 | 1990-11-28 | Continuous fluidized bed process for gentle drying of temperature-sensitive, moist products |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE4037866C2 (en) |
FR (1) | FR2669718B1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107300298A (en) * | 2017-07-28 | 2017-10-27 | 安徽科浦环保科技有限公司 | A kind of fluidized drying device of formaldehyde absorbing particle |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3528179A (en) * | 1968-10-28 | 1970-09-15 | Cryodry Corp | Microwave fluidized bed dryer |
DE2431522A1 (en) * | 1974-07-01 | 1976-01-22 | Kloeckner Humboldt Deutz Ag | PROCEDURE FOR CONTINUOUS DRYING OF WET, GRAINY AND / OR LITTLE GOODS AND DEVICE FOR PERFORMING THE PROCESS |
CH615269A5 (en) * | 1976-07-26 | 1980-01-15 | Buehler Ag Geb | Method and device for treating bulk material, in particular for expelling water from and drying farinaceous products |
GB2049899B (en) * | 1979-05-01 | 1983-03-30 | Ici Ltd | Process for drying vinyl chloride polymer wet cake and drier therefor |
DE3204690C2 (en) * | 1982-02-11 | 1983-12-08 | Glatt GmbH, 7851 Binzen | Drying device for powdery or granular pharmaceutical goods |
CH676879A5 (en) * | 1988-06-03 | 1991-03-15 | Glatt Maschinen & Apparatebau | |
DE3916479C1 (en) * | 1989-05-20 | 1990-08-30 | Otto Dr.Rer.Nat. Moebus | Drying biological and pharmaceutical prods. etc. - includes drying prods. on a porous floor in an evacuable tank using overhead microwave heater |
US4967486A (en) * | 1989-06-19 | 1990-11-06 | Glatt Gmbh | Microwave assisted fluidized bed processor |
-
1990
- 1990-11-28 DE DE19904037866 patent/DE4037866C2/en not_active Expired - Fee Related
-
1991
- 1991-11-26 FR FR9114550A patent/FR2669718B1/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
NICHTS ERMITTELT * |
Also Published As
Publication number | Publication date |
---|---|
FR2669718B1 (en) | 1998-01-23 |
DE4037866A1 (en) | 1992-06-04 |
FR2669718A1 (en) | 1992-05-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2029267B1 (en) | Process and apparatus for continuous polymerization of polymer in solid phase | |
DE3516966C2 (en) | Process for treating a particulate material and device for carrying out the process | |
US5522156A (en) | Drying apparatus and method | |
EP0371971B1 (en) | Bubble layer chamber | |
DE7705004U1 (en) | DEVICE FOR REMOVING AN EVAPORATIVE LIQUID FROM A GAS FLOW, E.G. IN A TREATMENT PROCESS BASED ON THE SPIRAL STRATEGY PRINCIPLE | |
WO1992016468A1 (en) | Process for calcining moist gypsum | |
DE3546129C2 (en) | Process for drying a solid | |
DE2943528A1 (en) | METHOD FOR THERMAL TREATMENT, ESPECIALLY DRYING OR DRYING TO CALCINATE | |
EP0792188B1 (en) | Method of and apparatus for drying blood plasma | |
DE4037866C2 (en) | Continuous fluidized bed process for gentle drying of temperature-sensitive, moist products | |
AT504996B1 (en) | METHOD AND DEVICE FOR DRYING CRYSTALLINE CARBOXYLIC ACIDS | |
DE3504950C2 (en) | ||
EP0151782B1 (en) | Process and apparatus for treating a powder or a granulate by applying heat | |
DE4111726A1 (en) | METHOD FOR MECHANICALLY CLEANING FOUNDRY SAND | |
DE2522592A1 (en) | HEATING DEVICE FOR PIPE SECTIONS MADE OF PLASTIC | |
EP0781741B1 (en) | Sludge treatment process | |
DE4404813C1 (en) | Process for fluidised-bed drying of sludge and fluidised-bed dryer for carrying out the process | |
DE2840496C2 (en) | Device for carrying out reactions between solids and gases or vapors in the fluidized bed | |
DE1454847B1 (en) | Process for the two-stage drying of piece-shaped plastics | |
DE3815726A1 (en) | Process and apparatus for the thermal treatment of substances and mixtures of substances in a fluidised bed | |
DE632705C (en) | Method and device for shaping, drying, heating and prebaking adhesive materials | |
DE1604883C (en) | Ring jet dryer for caked, wet, powdery material | |
CH652893A5 (en) | Treatment of extracted soya bean flakes | |
DE4028112C2 (en) | ||
DE3400399A1 (en) | Process and apparatus for the drying of thermolabile materials which are liable to cake |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
8110 | Request for examination paragraph 44 | ||
D2 | Grant after examination | ||
8364 | No opposition during term of opposition | ||
8339 | Ceased/non-payment of the annual fee |