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Featured researches published by Heiko Herold.


International Journal of Mineral Processing | 1996

Performance of a fluidized bed jet mill as a function of operating parameters

Mathias Benz; Heiko Herold; Benno Ulfik

Abstract Fluidized bed jet mills are used for the dry comminution in the μm range. The application of the jet mill ranges from deagglomeration purposes to grinding of hard materials. This indicates the wide field for the usage of this grinding technique. The comminution effect is based on particle-particle impact in expanding gas streams. A dynamic classifier is integrated in the fluidized bed jet mill. There are two parameters which can be used to control the performance of the fluidized bed jet mill: the speed of the classifier rotor and the pressure of the gas used for grinding. As a characteristic value the “spin-number” was defined. The “spin-number” is given as the ratio of the circumferential speed of the classifier rotor and the flow-through velocity of the classifying gas in radial direction. Results of limestone grinding were presented. The comminution of limestone represents a grinding process, not just a deagglomeration step. The fineness achieved, expressed by the mean particle diameter, can be modelled as a function of the “spin-number” and the pressure of the gas used for grinding. A similar dependency was found for the parameters of the RRSB-distribution, describing the shape and the position of the distribution. The dependencies could be backed-up with experiments performed with an easily grindable rubber chemical. A few experiments performed at the base-points of the working range of the fluidized bed jet mill enable to establish a characteristic field of performance for a given product. The knowledge of this characteristic field simplifies the selection of the optimum operation conditions of the fluidized bed jet mill for a given grinding task. Moreover it enables to include milling processes in more advanced process control systems.


Archive | 1992

Multiple dosage powder inhaler - has acceleration channel and dwell chamber for uniformly high drug dispersion

Heiko Herold; Axel Dr Wollenschlaeger; H. Landen; Franz Schmitt


Archive | 1993

Powder inhaler having dispersing, discharge, and dwell-time chambers, along with an acceleration channel

Heiko Herold; Axel Wollenschlager; H. Landen; Franz Schmitt


Archive | 1994

Device for inhalation

Heiko Herold; Axel Wollenschlager; Ahmed Dr Hegazy; Matthias Dr Herboth; Reiner Diederich; Roland Kleissendorf; Alfred Von Schuckmann


Archive | 2003

Process for the preparation of diisocyanates by quenching the gas phase resulting from the phosgenation of the corresponding diamines

Heiko Herold; Herbert Dr. Stutz; Hans-Joachim Brockhaus; Volker Michele


Archive | 2002

Method for producing highly pure, granular silicon in a fluidised bed

Heiko Herold; H. Günter Holdenried; Leslaw Mleczko; Matthias Pfaffelhuber; Karl-Theodor König


Archive | 2003

Electrochemical half-cell

Fritz Gestermann; Hans-Dieter Pinter; Karl-Ludwig Dr. Metzger; Heiko Herold


Archive | 1991

Process and device for fluidized bed spray granulation

Hans Uhlemann; Reinhard Boeck; Hans Daun; Heiko Herold


Archive | 1989

Process and apparatus for fluidized-bed granulation

Hans Uhlemann; Reinhard Boeck; Hans Daun; Heiko Herold


Archive | 1998

Gas phase polymerisation in a bell-shaped reactor

Friedrich Haendeler; Heiko Herold; Leslaw Mleczko; Claus Riehle; Franz-Josef Mersmann; Jürgen Schneider; Michael Dauben

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