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42 Results and Discussion 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 40 35 30 7 6.5 7.5 Evaporator Pressure [bar] 15 25 20 6 5.5 10 5 Segment Number [−] 5 4.5 4 Figure 4-3: Latin Hypercube Sampling result and hence, the probability of missing out on the optimum set of input values reduces. Based on these initial points, the optimization is run and the following section presents these results. 4-3-2 Optimization Results The CoMT-CAMD, as described earlier, has two steps. Thus the optimization procedure can be visualized as a two step problem. In the first step, the optimization of the process and fluid parameters leads to a hypothetical working fluid with segment number of 4.62 with a net output power of 10.09 kW. Figure 4-4 illustrates the value of the best objective function during each iteration. 12 10 8 6 4 2 0 A B 50 100 150 200 250 Iterations [−] Figure 4-4: Best objective function during each iteration Akshay Hattiangadi Master of Science Thesis Best Objective [kW] Condenser Pressure [bar]PDF Image | Working Fluid Design for Organic Rankine Cycle
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