Drying modelling and experimentation of Assam black tea (Camellia sinensis) with producer gas as a fuel

Thin layer drying kinetics of fermented tea (Camellia sinensis) was investigated at air temperatures (80, 90,100, 110) °C and velocities (0.50, 0.65, 075) m s−1 respectively using a producer gas furnace tea dryer. The tea samples weight, dry and wet bulb temperatures and air velocities were recorded...

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Veröffentlicht in:Applied thermal engineering 2014-02, Vol.63 (2), p.495-502
Hauptverfasser: Dutta, Partha Pratim, Baruah, Debendra Chandra
Format: Artikel
Sprache:eng
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Zusammenfassung:Thin layer drying kinetics of fermented tea (Camellia sinensis) was investigated at air temperatures (80, 90,100, 110) °C and velocities (0.50, 0.65, 075) m s−1 respectively using a producer gas furnace tea dryer. The tea samples weight, dry and wet bulb temperatures and air velocities were recorded continuously during each experiment. The black tea drying data were fitted to different semi-theoretical models such as Lewis, Page, Modified Page, Henderson and Pabis and Two Term, etc. The modified Page model gave better prediction of thin layer drying kinetics of black tea followed by Lewis model. The diffusivity constant (Do = 0.746 × 10−3 m2 s−1) and activation energy (Ea = 52.104 kJ mol−1) were computed from linear regression analysis. The modified Page model gave drying rate constant (k = 25.91 × 10−4 s−1) and exponent (n = 1) at 100 °C air temperature. Both air temperatures and velocities have influence to enhance drying rate constant (k) and exponent (n) in Page and Modified Page models. The energy consumption was found as 19.01 MJ kg−1 of made tea (3% w.b.) based on calorific value of producer gas (HHV = 4.39 MJ Nm−3). Specific energy consumption of the dryer was approximately 6.274 MJ kg−1 of water removed. •An experimental and modelling study of black tea drying (Assam variety) was performed.•Producer gas fired tea dryer was used for thin drying kinetic study of fermented tea.•Modified Page model gave best fit of experimental data.•Both hot air temperatures and velocities are reported to influence the drying rate.•Specific energy consumption per kilogram of made tea was computed as (19.01 MJ kg−1).
ISSN:1359-4311
DOI:10.1016/j.applthermaleng.2013.11.035