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 products

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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
Application number
DE19904037866
Other languages
German (de)
Other versions
DE4037866A1 (en
Inventor
Matthias Dietrich
Werner Liedy
Robert Bayer
Werner Goebel
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.)
BASF SE
Original Assignee
BASF SE
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 BASF SE filed Critical BASF SE
Priority to DE19904037866 priority Critical patent/DE4037866C2/en
Priority to FR9114550A priority patent/FR2669718B1/en
Publication of DE4037866A1 publication Critical patent/DE4037866A1/en
Application granted granted Critical
Publication of DE4037866C2 publication Critical patent/DE4037866C2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/32Drying 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
    • F26B3/34Drying 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
    • F26B3/343Drying 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/02Drying 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
    • F26B3/06Drying 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
    • F26B3/08Drying 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)

1. Kontinuierliches Wirbelschichtverfahren zur schonenden Trocknung von temperaturempfindlichen feuchten Produkten, wobei die feuchten Pro­ dukte in das fluidisierte Wirbelgut in einem Wirbelbetttrockner (= feuchtes, zu trocknendes Produkt) eindosiert und bei Temperaturen unterhalb der Siedetemperatur des Lösungsmittels getrocknet werden, die Steuerung der Produkttemperatur in der Wirbelschicht durch den Massenstrom und die Temperatur des Wirbelgases sowie durch den Massen­ strom des Produktes erfolgt, die Abführung der Brüden des Lösungs­ mittels durch das Wirbelgas erfolgt und die getrockneten Endprodukte aus der Wirbelschicht ausgetragen werden, dadurch gekennzeichnet, daß die Trocknung durch dielektrische Erwärmung der feuchten Produkte mittels eines Hochfrequenzfeldes und die Temperaturführung über die Wirbelgaseintrittstemperatur erfolgt.1.Continuous fluidized bed process for the gentle drying of temperature-sensitive moist products, the moist products being metered into the fluidized fluidized bed in a fluidized bed dryer (= moist product to be dried) and dried at temperatures below the boiling point of the solvent, the control of the product temperature in the Fluidized bed occurs through the mass flow and the temperature of the fluidizing gas and through the mass flow of the product, the evaporation of the vapors of the solution is carried out by means of the fluidizing gas and the dried end products are discharged from the fluidized bed, characterized in that the drying is carried out by dielectric heating of the moist Products by means of a high-frequency field and the temperature control via the fluidizing gas inlet temperature. 2. Diskontinuierliches Wirbelschichtverfahren zur schonenden Trocknung von temperaturempfindlichen feuchten Produkten, wobei die feuchten Produkte in einem Wirbelbetttrockner (= feuchtes, zu trocknendes Produkt) vorgelegt und bei Temperaturen unterhalb der Siedetemperatur des Lösungsmittels getrocknet werden, die Steuerung der Produkttem­ peratur in der Wirbelschicht durch den Massenstrom und die Temperatur 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, dadurch gekennzeichnet, daß die Trocknung durch dielektrische Erwärmung der feuchten Produkte mittels eines Hochfrequenzfeldes und die Temperaturführung über die Wirbelgaseintrittstemperatur erfolgt.2. Discontinuous fluidized bed process for gentle drying of temperature-sensitive moist products, whereby the moist Products in a fluid bed dryer (= moist, to be dried Product) submitted and at temperatures below the boiling point the solvent can be dried, the control of the product temperature temperature in the fluidized bed due to the mass flow and the temperature of the fluidizing gas and through the mass flow of the product, which The vapors of the solvent are removed by the fluidizing gas and the dried end products are discharged from the fluidized bed are characterized in that the drying by dielectric Heating the moist products using a high frequency field and the temperature is controlled via the fluidizing gas inlet temperature.
DE19904037866 1990-11-28 1990-11-28 Continuous fluidized bed process for gentle drying of temperature-sensitive, moist products Expired - Fee Related DE4037866C2 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
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

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