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Energies 2020, 13, 2259 21 of 24 Appendix A The LCA results in each component of the proposed configurations using copper as the material are presented in Table A1. Table A1. Results of Life Cycle Assessment for each component selecting copper as the material. Organic Equipment Fluid w Quality [mPts/kg] [kg] 1400 1579 1400 333 1400 179 1400 3137 1400 279 1400 2398 1400 3399 1400 848 1400 2822 1400 2 1400 9 46,467 184 2639 149 1400 3137 1400 300 1400 153 1400 3137 1400 279 1400 2398 1400 3399 1400 810 1400 2822 1400 2 1400 3 46,467 184 2680 144 1400 1579 1400 312 1400 115 1400 3137 1400 279 1400 2398 1400 3399 1400 921 1400 2822 1400 2 1400 18 46,467 184 5426 170 Yco [mPts] 2,321,003 490,057 263,130 4,611,496 409,760 3525712 4,996,099 1,245,860 4,148,525 2894 12,842 8,568,515 Yom [mPts] 0 0 0 0 0 0 0 1 2 3 4 856,851 Yde [mPts] 110,524 23,336 12,530 219,595 19,512 167,891 237,909 59,327 197,549 138 612 231,350 10,585 219,595 21,002 10,694 219,595 19,512 167,891 237,909 56,683 197,549 138 209 231,350 10,430 110,524 21,821 8054 219,595 19,512 167,891 237,909 64,466 197,549 138 1249 231,350 Y [mPts] 2,431,527 513,393 275,660 4,831,091 429,272 3,693,603 5,234,008 1,305,187 434,6076 3035 13,457 9,656,716 441,819 4,831,091 462,038 235,264 4,831,094 429,276 3,693,608 5,234,014 1,247,024 4,346,082 3043 4618 9,656,716 407,461 2,431,527 480,064 177,187 4831094 429,276 3,693,608 5,234,014 1,418,266 4,346,082 3036 27,499 9,656,716 1,041,370 Cyclohexane ITC1 ITC2 ITC3 RHR HTR T1 T2 T3 C1 P1 P2 Thermal Oil Fluid ITC1 ITC2 ITC3 RHR HTR T1 Material Copper Copper Copper Copper Copper Copper Copper Copper Copper Copper Copper Therminol Cyclohexane Copper Copper Copper Copper Copper Copper Copper Copper Copper Copper Copper Therminol Toluene Copper Copper Copper Copper Copper Copper Copper Copper Copper Copper Copper Therminol Acetone Toluene T2 T3 C1 P1 P2 Thermal Oil Fluid ITC1 ITC2 ITC3 RHR HTR T1 Acetone T2 T3 C1 P1 P2 Thermal Oil Fluid References 1. Diaz, G.A.; Forero, J.D.; Garcia, J.; Rincon, A.; Fontalvo, A.; Bula, A.; Padilla, R.V. Maximum power from fluid flow by applying the first and second laws of thermodynamics. J. Energy Resour. Technol. 2017, 139, 032903. [CrossRef] 2. Ramírez, R.; Gutiérrez, A.S.; Eras, J.J.C.; Valencia, K.; Hernández, B.; Forero, J.D. Evaluation of the energy recovery potential of thermoelectric generators in diesel engines. J. Clean. Prod. 2019, 241, 118412. [CrossRef] 3. Angelino, G. Carbon Dioxide Condensation Cycles. J. Eneg. Power 1968, 287–295. [CrossRef] 4. Dostal, V.; Driscoll, M.J.; Hejzlar, P.A. Supercritical Carbon Dioxide Cycle for Next Generation Nuclear Reactors. Ph.D. Thesis, Massachusetts Institute of Technology, Cambridge, UK, March 2004. 5. Abrosimov, K.A.; Baccioli, A.; Bischi, A. Techno-economic analysis of combined inverted Brayton—Organic Rankine cycle for high-temperature waste heat recovery. Energy Convers. Manag. X 2019, 3, 100014. [CrossRef] 392,031.28 39,203.13 4,611,495.84 441,035.62 224,568.70 4,611,495.84 409,759.56 3,525,711.97 4,996,098.50 1,190,334.01 4,148,525.01 2895.92 4398.53 8,568,515 386,282.14 2,321,002.70 458,241.95 169,131.42 4,611,495.84 409,759.56 3,525,711.97 4,996,098.50 1,353,793.03 4,148,525.01 0 1 2 3 4 5 6 7 8 9 10 856,851 10,748.90 0 1 2 3 4 5 6 7 8 9 10 856,851 2889.66 26,239.27 8,568,515 924,019.85 92,401.98 24,949PDF Image | S-CO2 Brayton Cycle Coupled with ORC as Bottoming Cycle
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