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  1. Intan Soraya Shamsudin, Mohd Shamsul Anuar, Ahmad Husni Mohd. Hanif, Yus Aniza Yusof, Suraya Mohd Tahir
    MyJurnal
    This research was conducted to investigate the compaction performance and mechanical
    strength of compacted urea fertilizer in unlubricated and lubricated die systems. The
    ground urea 46% N fertilizer was compacted in a 13 mm flat-face cylindrical die set in
    both unlubricated and lubricated die systems with vegetable fatty acids and magnesium
    stearate as lubricants at various compaction stresses to produce urea fertilizer tablets. In
    conclusion, a lubricated die system reduces the frictional effects during the production of
    urea fertilizer tablets and also produces a mechanically stronger urea fertilizer tablet than
    those produced in an unlubricated die system. In addition, the vegetable fatty acids and
    magnesium stearate lubricants are found to improve the compaction performance of urea
    fertilizer tablet as well as its mechanical strength.
  2. Manzoor, Sama, Yus Aniza Yusof, Ling, Chin Nyuk, Intan Syafinaz Mohamed Amin Tawakkal, Mohammad Fikry, Chang Lee Sin
    MyJurnal
    In this study, papaya (Carica papaya) peel was dried using convection oven and microwave drying methods to investigate the drying kinetics and the drying behavior in the attempt to search for a feasible way to utilize waste peel. Three different drying temperatures (45, 55, and 65 oC) and microwave powers (250, 440, and 600 W) were applied to dry the papaya peel, wherein the drying data were fitted into the following seven drying kinetic models: Lewis, Page, Modified Page, Henderson and Pabis, Logarithmic, Two-Term, and Approximation of Diffusion models. The study outcomes indicated that the Page model emerged as the best fitted model for oven drying of papaya peels with the highest coefficient of determination (R2) value (0.994-0.996) for all the three temperatures. As for microwave drying, the Approximation of Diffusion model exhibited the best fit owing to the highest R2 value (0.996-0.999) for all the three powers. The effective moisture diffusivity values for convection oven and microwave drying methods ranged from 6.65 x 10-08 to 4.35 x 10-07 and from 2.43 x 10-07 to 6.67 x 10-07, respectively. Additionally, the activation energy values were recorded at 61.301 kJ/mol and 46.621 W/g for oven and microwave drying methods, respectively.
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