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working fluid, the simplified heater in the OFC system results in a 23.9% total component costs savings. This cost savings are summarized in Table 5 for different working fluids. butylbenzene Components Evaporator Condenser % of Total Component Cost 32.06 10.36 Preheater 17.72 Regenerator Total 68.34 Table 4. 1MW ORC Heater and Condenser Cost Breakdown4 Toluene 68.34 44.43 23.91 ethylbenzene o-xylene p-xylene D5 ORC Total Heater & Condenser Cost % 68.34 68.34 68.34 68.34 68.34 OFC Total Heater & Condenser Cost % 50.63 53.85 51.25 66.08 68.99 OFC Heater & Condenser Cost Saving % 17.71 14.49 17.09 2.26 -0.65 68.34 68.34 68.34 68.34 50.54 51.07 8.2 17.80 m-xylene 70.46 64.18 17.27 MD4M -2.12 MD3M 4.16 D6 Turbine & Generator As introduced in the Technology Overview, the anticipated MVP uses a two-stage turbine to enhance the overall system efficiency. The two-stage turbine is a cascading system with two small turbines. When compared to an ORC system of equivalent power, the assumption is that each of these two smaller turbines in the hypothetical OFC system will produce half of the power output. Based on quotes from industry research13, the cost for the two-stage turbine is estimated to be 20% higher over the single-stage turbine. Flash Evaporator Flash evaporators are components commonly found in the chemical and food preparation industries. They are simple devices comprised of a throttling valve and a pressure Table 5. Percentage Savings for OFC Heater and Condenser for Different Working Fluids 9PDF Image | ElectraTherm Commissions 10 Green Machines
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