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Effluent 270c 280C 30C Deodorizer 80C 200C 50C 180C 280C! 80C c Figure 1. Existing palm oil mill block diagram. T5, C Stream H1 H2
Effluent 270c 280C 30C Deodorizer 80C 200C 50C 180C 280C! 80C c Figure 1. Existing palm oil mill block diagram. T5, C Stream H1 H2 C2 Table 2. Extracted heat data. Tt, C 180 50 280 80 30 280 200 FCp, MWC 5 4 4 3 80 Figure 1 shows a palm oil mill block diagram and Table 2 shows the extracted heat data. a) Apply Composite Curves or Problem Table Algorithm to obtain a minimum heating and cooling utility target of 130 MW and 220 MW respectively with a hot and cold pinch temperature of 180C and 170C respectively. Assume ATmin of 10C for the streams extracted in Table 2. (10 marks)
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