| Issue |
BIO Web Conf.
Volume 71, 2023
II International Conference on Current Issues of Breeding, Technology and Processing of Agricultural Crops, and Environment (CIBTA-II-2023)
|
|
|---|---|---|
| Article Number | 02021 | |
| Number of page(s) | 7 | |
| Section | Ecology, Environmental Protection and Conservation of Biological Diversity | |
| DOI | https://doi.org/10.1051/bioconf/20237102021 | |
| Published online | 07 November 2023 | |
Modeling of heat exchange processes in a condenser of a pyrolysis bioenergy plant
1 Karshi engineering economic Institute, 225, Mustaqillik street, Karshi, 180100, Uzbekistan
2 University of Economics and Pedagogy Non-state educational, 13, I.A. Karimov street, Karshi, 180100, Uzbekistan
3 Karshi branch of Tashkent university of information technologies named after Muhammad al- Khwarizmi, Beshkent road 3 km, Karshi, 180100, Uzbekistan
The article presents the results of mathematical modeling of heat exchange processes in the condenser of a pyrolysis plant, in order to identify the optimal parameters for cooling the biomass pyrolysis steam. A mathematical model of the thermal balance of the condenser of a pyrolysis plant has been developed for the calculation, selection and thermal analysis of the working cycle of the condenser, which allows to obtain the values of the optimal parameters of the temperature regime. The technological scheme of a pyrolysis bioenergy plant with a recuperative heat exchanger, which simultaneously provides hot water, gaseous and liquid biofuels to the consumer, is presented. The analysis of the obtained results shows that the water temperature at the outlet of the condenser of the pyrolysis plant is on average in the range of 60-70°C and suitable for heat supply systems of an autonomous consumer.
© The Authors, published by EDP Sciences, 2023
This is an Open Access article distributed under the terms of the Creative Commons Attribution License 4.0, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
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