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Title | Efficiency Investigation of Coffee Production Waste Drying by Filtration Method |
Authors |
Ivashchuk, O.S.
Atamanyuk, V.M. Chyzhovych, R.A. |
ORCID | |
Keywords |
biomass energy efficiency technologically feasible parameters fuel briquettes |
Type | Article |
Date of Issue | 2024 |
URI | https://essuir.sumdu.edu.ua/handle/123456789/96966 |
Publisher | Sumy State University |
License | Creative Commons Attribution - NonCommercial 4.0 International |
Citation | Ivashchuk O. S., Atamanyuk V. M., Chyzhovych R. A. (2024). Efficiency investigation of coffee production waste drying by filtration method. Journal of Engineering Sciences (Ukraine), Vol. 11(2), pp. F9–F16. https://doi.org/10.21272/jes.2024.11(2).f2 |
Abstract |
This article presents the results of determining the technologically feasible parameters of filtration drying
of coffee production waste based on experimental data on the kinetics of material drying and the hydrodynamics of
thermal agent filtration. The lowest total energy costs were observed with the following process parameters: the material
layer height of 120 mm, the thermal agent temperature of 90 °C, the velocity through the stationary layer of 1.76 m/s,
and the specific energy consumption of 5857 kJ per 1 kg of water. Based on the determined technologically feasible
process parameters, an evaluation of the filtration drying method for coffee production waste was performed at an
industrial installation. According to the calculation, using the filtration method, 1164 kW h of energy was required to
dry about 1000 kg of coffee production waste. A total energy of about 1.65 kW h/kg was required to remove 1 kg of
moisture from the material in an industrial filtration drying installation. The results were compared with a drying
material with similar initial parameters. It was calculated that to dry 1000 kg of coffee production waste in a rotary
dryer, it is necessary to spend about 1625 kW h, and the total energy consumption for removing 1 kg moisture from the
studied material is approximately 2.37 kW h/kg. Thus, for a similar output of about 1000 kg/h, filtration drying can
reduce energy consumption by about 465 kW·h and reduce the required drying time by more than 20 times. The overall
economic effect of using the filtration drying method in industry is expected to be higher, given the significant heat
losses to the environment for a rotary dryer due to its large size, long drying time, design features, and the need for
energy-intensive auxiliary equipment. After calculating the energy consumption per 1 kg of dry material, it is necessary
to spend 12 950 kJ/kg of dry matter, about 41.5 % less than the higher calorific value for experimental samples of
briquetted solid fuel made from this material. This result makes it economically feasible to further dry coffee production
waste to produce alternative solid fuels. |
Appears in Collections: |
Journal of Engineering Sciences / Журнал інженерних наук |
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