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configuration which the author has investigated, such as two single ORC systems, reheat ORC system, etc. (Aneke et al., 2012b). Therefore, based on the above facts, the standalone ORC system proposed in this work for the conversion of the waste heat from the fryer section of the KP Billingham crisp manufacturing plant is the dual heat source ORC system. The schematic diagram of the proposed system is shown in Figure 6-1. 6.1 Process Description of the Proposed ORC System In the process, the liquid working fluid from the condenser (state 1) is pumped to the preheater (state 2) where the lower-temperature (120oC) waste heat from the fryer is initially used to preheat the working fluid to a high-temperature sub-cooled liquid (state 3). The high-temperature liquid working fluid is passed from the first preheater to the preheater/evaporator Figure 6–1: Proposed Dual Heat Source ORC System 120PDF Image | OPTIMISING THERMAL ENERGY RECOVERY
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