Hostname: page-component-6766d58669-7cz98 Total loading time: 0 Render date: 2026-05-21T11:19:36.347Z Has data issue: false hasContentIssue false

Industrial scale microwave applicator for high temperature alkaline hydrolysis of PET

Published online by Cambridge University Press:  22 May 2018

Vasileios Ramopoulos*
Affiliation:
Institute for pulsed power and microwave technology, Karlsruhe Institute of Technology, Hermann – von Helmholtz – Platz 1, 76344 Eggenstein – Leopoldshafen, Germany
Guido Link
Affiliation:
Institute for pulsed power and microwave technology, Karlsruhe Institute of Technology, Hermann – von Helmholtz – Platz 1, 76344 Eggenstein – Leopoldshafen, Germany
Sergey Soldatov
Affiliation:
Institute for pulsed power and microwave technology, Karlsruhe Institute of Technology, Hermann – von Helmholtz – Platz 1, 76344 Eggenstein – Leopoldshafen, Germany
John Jelonnek
Affiliation:
Institute for pulsed power and microwave technology, Karlsruhe Institute of Technology, Hermann – von Helmholtz – Platz 1, 76344 Eggenstein – Leopoldshafen, Germany Institute for Radio Frequency Engineering and Electronics, Karlsruhe Institute of Technology, Engesserstraße 5, 76131 Karlsruhe, Germany
*
Author for correspondence: Vasileios Ramopoulos, E-mail: vasileios.ramopoulos@kit.edu
Rights & Permissions [Opens in a new window]

Abstract

A microwave design for an industrial scale applicator of a continuous microwave assisted depolymerization of polyethylene terephthalate (PET) has been developed. The cavity is designed for use in combination with an Archimedean screw pump to transport the reaction material, surrounded by a cylindrical pipe with a diameter of 250 mm and a length of 250 mm at the 2.45 GHz ISM band. The proposed design is modular and can be easily expanded for the heating of longer reactor tubes. Simulation results show that a homogeneous heating of the process material along the screw axis can be achieved by using a novel cavity design which is based on the TE1,0,x– rectangular waveguide cavity mode. The achieved design provides high energy efficiency with a reflected power of less than 10%. It is robust against changes in the permittivity of the reactants. The electromagnetic design is based on the dielectric properties of the solvolytic reaction mixture measured in the relevant temperature range. It is verified over the full range of the expected permittivities.

Information

Type
Research Papers
Creative Commons
Creative Common License - CCCreative Common License - BYCreative Common License - NCCreative Common License - SA
This is an Open Access article, distributed under the terms of the Creative Commons Attribution-NonCommercial-ShareAlike licence (http://creativecommons.org/licenses/by-nc-sa/4.0/), which permits non-commercial re-use, distribution, and reproduction in any medium, provided the same Creative Commons licence is included and the original work is properly cited. The written permission of Cambridge University Press must be obtained for commercial re-use.
Copyright
Copyright © Cambridge University Press and the European Microwave Association 2018
Figure 0

Table 1. Molar volumes of the reagents

Figure 1

Fig. 1. Designed dual-mode cavity for the dielectric measurements setup.

Figure 2

Fig. 2. (a): Temperature depending dielectric constant for the initial mixture and final mixture. (b): Temperature depending dielectric loss tangent for the initial mixture and final mixture.

Figure 3

Fig. 3. Part of the Archimedean screw (left) and simplified model (right).

Figure 4

Table 2. Simulated relative power absorption for different screw parameters, scaled to the wavelength

Figure 5

Fig. 4. Simulated relative power absorption as a function of tanδ (@ 2.46 GHz and εr = 30).

Figure 6

Fig. 5. Principal design of the microwave reactor (top), temperature profile (bottom).

Figure 7

Fig. 6. Simulated electric field in the cylindrical microwave cavity.

Figure 8

Fig. 7. Simulated geometry of center zone (left), side view (right).

Figure 9

Fig. 8. Electric field distribution of the power distribution network design in azimuthal direction of zone c (upper left); of levels b and d (lower left); of levels a and e (lower right) and in the axial direction (upper right).

Figure 10

Table 3. Power distribution in the cavity load [% of the absorbed power]

Figure 11

Fig. 9. Pabs(f) at the single microwave port.

Figure 12

Fig. 10. Experimental setup.

Figure 13

Fig. 11. Simulated power distribution (left), measured temperature distribution (right).