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Previous Chapter

Appendix

Appendix 1

Figure A1.1 Dry bulb temperature over five years for Ahwaz.

Figure A1.2 Relative humidity over five years for Ahwaz.

Figure A1.3 T_wb of Ahwaz based on five-year average of RH and T_db.

Figure A1.4 Dry bulb temperature over five years for Chabahar.

Figure A1.5 Relative humidity over five years for Chabahar.

Figure A1.6 T_wb of Chabahar based on five-year average of RH and T_db.

Figure A1.7 Dry bulb temperature over five years for Kamyaran.

Figure A1.8 Relative humidity over five years for Kamyaran.

Figure A1.9 T_wb of Kamyaran based on five-year average of RH and T_db.

Figure A1.10 Dry bulb temperature over five years for Bandar-Anzali.

Figure A1.11 Relative humidity over five years for Bandar-Anzali.

Figure A1.12 T_wb of Bandar-Anzali based on five-year average of RH and T_db.

Appendix 2

Technical input data to the code:

η_pp = 0.35, η_g = 0.85, η_b = 0.8, _FCU = 0.85, _wh = 0.85, η_CHP = 0.85, COP_abc = 0.7, T₀ = 15°C, T_hg = 1000°C, T_oil = 60°C, T_jacketing = 100°C, T_exhaust = 540°C, Q_oil = 0.15Q_rec, Q_jacketing = 0.35Q_rec, Q_exhaust = 0.5Q_rec, T_room,sum = 25°C, T_room,win = 22°C, T_{db,sum,Kerman} = 36.5°C, T_{db,win,Kerman} = −2.5°C, T_db,sum,Ahwaz = 46.74°C, T_db,win,Ahwaz = 8.73°C, T_{db,sum,Bandar Anzali} = 29.76°C, T_{db,win,Bandar Anzali} = 4.61°C, T_{db,sum,Chabahar} = 33.55°C, T_{db,win,Chabahar} = 16.87°C, T_{db,sum,Kmayaran} = 36.82°C, T_{db,win,Kmayaran} = −4.88°C, LAT_Kerman = 30.28°, LAT_Ahwaz = 31.33°, LAT_{Bandar Anzali} = 37.46°, LAT_Chabahar = 25.28°, LAT_Kamyaran = 34.80°, NOU = 8

Environmental input data:

$i_{C O, P}^{0} = 4$ $i_{C O, P}^{0} = 4$ , $i_{C O, C}^{0} = 0.1274 / C O P_{a b c}$ $i_{C O, C}^{0} = 0.1274 / C O P_{a b c}$ , $i_{C O, H}^{0} = 0.1274$ $i_{C O, H}^{0} = 0.1274$ , $i_{C O, D}^{0} = 0.1274$ $i_{C O, D}^{0} = 0.1274$ , $i_{C O_{2}, P}^{0} = 700$ $i_{C O_{2}, P}^{0} = 700$ , $i_{C O_{2}, C}^{0} = 182 .04 / C O P_{a b c}$ $i_{C O_{2}, C}^{0} = 182 .04 / C O P_{a b c}$ , $i_{C O_{2}, H}^{0} = 182 .04$ $i_{C O_{2}, H}^{0} = 182 .04$ , $i_{C O_{2}, D}^{0} = 182 .04$ $i_{C O_{2}, D}^{0} = 182 .04$ , $i_{N O_{X}, P}^{0} = 300$ $i_{N O_{X}, P}^{0} = 300$ , $i_{N O_{X}, C}^{0} = 0.1532 / C O P_{a b c}$ $i_{N O_{X}, C}^{0} = 0.1532 / C O P_{a b c}$ , $i_{N O_{X}, H}^{0} = 0.1532$ $i_{N O_{X}, H}^{0} = 0.1532$ , $i_{N O_{X}, D}^{0} = 0.1532$ $i_{N O_{X}, D}^{0} = 0.1532$ , $i_{C O, P}^{1} = 0.8$ $i_{C O, P}^{1} = 0.8$ , $i_{C O, C}^{1} = 0.1274 / C O P_{a b c}$ $i_{C O, C}^{1} = 0.1274 / C O P_{a b c}$ , $i_{C O, H}^{1} = 0.1274$ $i_{C O, H}^{1} = 0.1274$ , $i_{C O, D}^{1} = 0.1274$ $i_{C O, D}^{1} = 0.1274$ , $i_{C O_{2}, P}^{1} = 430$ $i_{C O_{2}, P}^{1} = 430$ , $i_{C O_{2}, C}^{1} = 182.04 / C O P_{a b c}$ $i_{C O_{2}, C}^{1} = 182.04 / C O P_{a b c}$ , $i_{C O_{2}, H}^{1} = 182.04$ $i_{C O_{2}, H}^{1} = 182.04$ , $i_{C O_{2}, D}^{1} = 182.04$ $i_{C O_{2}, D}^{1} = 182.04$ , $i_{N O_{X}, P}^{1} = 0.7$ $i_{N O_{X}, P}^{1} = 0.7$ , $i_{N O_{X}, C}^{1} = 0.1532 / C O P_{a b c}$ $i_{N O_{X}, C}^{1} = 0.1532 / C O P_{a b c}$ , $i_{N O_{X}, H}^{1} = 0.1532$ $i_{N O_{X}, H}^{1} = 0.1532$ , $i_{N O_{X}, D}^{1} = 0.1532$ $i_{N O_{X}, D}^{1} = 0.1532$

Economic input data (the currency of these data is USD):

$i_{E}^{0} = 10.83 U S D$ $i_{E}^{0} = 10.83 U S D$ is the price of each electricity consumption counter.

$i_{E}^{1} = \{\begin{array}{l} 1.1 (1.534 \times 10^{17} E_{n o m}^{- 10.33} + 866.4), & 25 \leq E_{n o m} \leq 500 \\ 1.1 \times 1420, 0 < E_{n o m} < 25 \end{array}$ $i_{E}^{1} = \{\begin{array}{l} 1.1 (1.534 \times 10^{17} E_{n o m}^{- 10.33} + 866.4), & 25 \leq E_{n o m} \leq 500 \\ 1.1 \times 1420, 0 < E_{n o m} < 25 \end{array}$ is the engine cost per kW of electricity; the coefficient 1.1 is consideration for the heat recovery heat exchangers.

$I_{O M}^{1} = 1.1 (E_{n o m} \times 3.3 \times 10^{- 5} + 26.5)$ $I_{O M}^{1} = 1.1 (E_{n o m} \times 3.3 \times 10^{- 5} + 26.5)$ is the operation and maintenance costs. $i_{C}^{0} = i_{C}^{1} = (- 35.4 \log (C_{n o m}) + 431)$ $i_{C}^{0} = i_{C}^{1} = (- 35.4 \log (C_{n o m}) + 431)$ is the chiller cost per kW of cooling. The boiler cost per kW of capacity is measured as follows:

$i_{H}^{0} = i_{H}^{1} = \{\begin{array}{l} (1.38 \times 10^{9} H_{n o m}^{- 3.212} + 9.39) & H_{n o m} \geq 464.8 \\ (23.54 \times H_{n o m}^{- 0.08598} - 6.48) & 75.53 \leq H_{n o m} < 464.8 \\ 9.74, 0 < H_{n o m} < 75.53 \end{array}$ $i_{H}^{0} = i_{H}^{1} = \{\begin{array}{l} (1.38 \times 10^{9} H_{n o m}^{- 3.212} + 9.39) & H_{n o m} \geq 464.8 \\ (23.54 \times H_{n o m}^{- 0.08598} - 6.48) & 75.53 \leq H_{n o m} < 464.8 \\ 9.74, 0 < H_{n o m} < 75.53 \end{array}$

$i_{s o l a r} = 267 (U S D / m^{2})$ $i_{s o l a r} = 267 (U S D / m^{2})$ is the plate solar collector cost.

$t_{s e} = t_{b e} = 0.1188 (U S D / k W h)$ $t_{s e} = t_{b e} = 0.1188 (U S D / k W h)$ and $t_{g a s} = 0.377 (U S D / m^{3})$ $t_{g a s} = 0.377 (U S D / m^{3})$ are the electricity and gas tariffs.

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Appendix

Appendix 1

Appendix 2

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