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May 6, 2026Beverages0 citationsOpen Access

Evaluation of Infrared Drying Parameters for Spent Coffee Grounds: Effects on Drying Kinetics, Quality, and Energy Consumption

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SWShu-Chin WangMTMeng-Jen TsaiCTChih-Hong Tung

Key Points

  • The research aims to evaluate how different infrared drying parameters affect the drying kinetics and quality of spent coffee grounds.
  • Investigated infrared power levels of 800, 900, and 1000 W.
  • Conducted drying experiments with a sample thickness of 0.7 cm and loading of 500 g.
  • Fitted drying data to four mathematical models to assess kinetics.
  • Measured moisture content, drying rate, and energy consumption.
  • Final moisture content of treated spent coffee grounds was <10%.
  • Drying time decreased from 30 to 24 minutes with increased power.
  • Effective moisture diffusivity increased with power, indicating stronger internal moisture diffusion.
  • Color differences were significantly lower at higher power levels (900 W and 1000 W).
  • Specific energy consumption showed a marginal decrease from 5.80 to 5.68 kWh/kg at higher power.

Abstract

Spent coffee grounds (SCGs) are abundant byproducts generated during coffee processing that are unsuitable for storage and subsequent value-added utilization owing to their high moisture content and water activity (aw). This study investigated the effects of different infrared power levels (800, 900, and 1000 W) on drying kinetics, product quality, and energy efficiency to determine the preferred drying parameters for SCGs. The initial moisture content and aw of SCGs were 63.56% (wet basis) and 0.95, respectively. To enhance mechanistic understanding, the drying data were fitted to four mathematical models, with the Midilli and Page models providing the best fit (R2 > 0.99). Drying experiments were conducted under a sample thickness of 0.7 cm and a loading of 500 g, with a final moisture content of <10% as the drying endpoint. The results showed that as infrared power increased, drying time decreased from 30 to 24 min and the drying rate significantly increased from 10.32 to 12.77 g H2O/min (p < 0.05). The drying process was mainly characterized by a falling-rate period, with the effective moisture diffusivity ranging from 0.97 to 1.15 × 10−8 m2/s and (increasing with rising power, indicating that internal moisture diffusion was the dominant drying mechanism. The final aw of each treatment group was ≤0.60, indicating good storage stability. Color analysis showed that the color differences in treatments at higher power levels (900 W and 1000 W) were significantly lower than those at lower ones (p < 0.05). While the specific energy consumption (SEC) showed a marginal decrease from 5.80 to 5.68 kWh/kg at higher power, a comprehensive evaluation of drying efficiency, quality characteristics, and energy consumption indicated that 1000 W was the preferred infrared drying power under the conditions employed in this study. These results confirm that infrared drying is an efficient stabilization method with strong potential for rapid stabilization of food processing byproducts.

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Cite This Study

Wang et al. (2026) studied this question.

synapsesocial.com/papers/69fa8eac04f884e66b530fa3https://doi.org/10.3390/beverages12050053
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