RECIPROCATING COMPRESSOR CALCULATION SHEET ISOTHERMAL COMPRESSION Gas properties, flowrate and conditions. Compressor Calculation Sheet

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RECIPRCATING CMPRESSR CALCULATIN SHEET ISTHERMAL CMPRESSIN Gas properties, flowrate and conditions 1 Gas name Air Item or symbol Quantity Unit Item or symbol Quantity Unit Formula 2 Suction pressure, ps 1.013 bar A Discharge pressure, pd 38.2 bar A 3 Suction temperature, ts 35 C Head (m) : 4 Ts 308 K p CR 37.70 bar A H IS =234.86 R.T1{ Log (r')+ 0.05} 5 MW 28.4 kg/kgmol T CR 132.80 K Gas horse power (kw) : 6 k S 1.400 p R = p / p CR 0.027 GHP IS =0.064 Q1.p1.{ Log (r')+ Δ C }/Z1 7 R S 0.293 kj/kg. K T R = T / T CR 2.32 ΔC is approx.< 0.05 for Δp < 50 bar 8 DSs 1.123 kg/m3 Z S 1.00,p<200 bar A and temperature at 9 MCp 29.14 kj/kgmol. K Cp S 1.025 kj/kg near 50 C for each stage 10 G 12000 kg/hr G mol 423 kgmol/hr 11 Q S 10681 m 3 /hr Q N 9467 Nm 3 /hr Q1 capacity (m3/hr) at refference 12 pressure p1 and t1 Compressor Calculation Sheet Item Symbol Unit Quantity Note 13 Preliminary Calculation (General method) 14 Adiabatic compression 15 First Stage Volume flow Qs m3/hr 10681 Isothermal efficiency : When cooling system for cylinder and interstage 16 Cylinder intake pressure ps' bara 0.98261 cooler is applied and crankshaft speed is low, L/D is high, isothermal 17 Cylinder exhaust pressure pd' bara 39.346 efficiency will increase. 18 Pressure ratio (p D / p S ) r - 40.042 19 (k-1)/k - 0.2857 20 k/(k-1) - 3.500 21 Total Hydrodynamic head H IS-TTAL m 34994 22 Expected isothermal compr. eff. 0.750 Average isothermal efficiency is approximatelly 0.63 up to 0.70 from medium to large compr. 23 24 Frame BHP selection at first stage Casing I 25 No. of compression acting 2 Fig. A.2/A.3 Approx. no. of stage 7 26 Stroke length, L mm 430 Fig. A.2/A.3 Approx. pressure ratio, r' 1.6941 27 No. of throw at first stage, z 3 Fig. A.2/A.3 for each stage 28 Crankshaft speed, N RPM 200 Fig. A.1 29 Max. diameter, Dmax (= L / 0.6 ) mm 717 30 No. of frame 1 31 Calculated frame BHP/throw, 0.11 Qp1 kw 229 App. (A.4) 32 Max. H per throw m 5261 Eq.A.11

1 Detail calculation Note 2 Stage 1 Stage 2 Stage 3 Stage 4 Stage 5 Stage 6 Stage 7 Stage 8 3 Mass flow, G 12000 12000 12000 12000 12000 12000 12000 12000 4 Max. H per stage for parallel throws 5261.1 5261.1 5261.1 5261.1 5261.1 5261.1 5261.1 5261.1 5 Last cylinder exhaust press. (bara) 39.346 39.346 39.346 39.346 39.346 39.346 39.346 39.346 6 p1 1.013 1.013 1.013 1.013 1.013 1.013 1.013 1 Refference condition in 7 t1 35 35 35 35 35 35 35 35 this sheet is equal with 8 Q1 10681.1 10681.1 10681.1 10681.1 10681.1 10681.1 10681.1 10681 intake condition 9 Cyl. intake pressure, ps ' (bara) 0.98 1.665 2.820 4.777 8.093 13.710 23.226-10 Suction temperat ure, ts ( C) 35.0 35.0 35.0 35.0 35.0 35.0 35.0 35.0 11 Ts ( K) 308.0 308.0 308.0 308.0 308.0 308.0 308.0 308.0 12 MW 28.40 28.40 28 28 28 28 28 28 13 Rs = 8.314/MW 0.29 0.29 0.29 0.29 0.29 0.29 0.29 0.29 14 p CR 37.7 37.7 37.7 37.7 37.7 37.7 37.7 37.7 15 T CR 132.8 132.8 132.8 132.8 132.8 132.8 132.8 132.8 16 p R = p RED = p / pcr 0.03 0.044 0.07 0.13 0.21 0.36 0.62 #VALUE! 17 T R = T RED = T / T CR 2.32 2.319 2.32 2.32 2.32 2.32 2.32 2.32 18 Z S 1 1 1 1 1 1 1 1 19 MCp S (kj/kgmo l.k) 29.14 29.1 29.1 29.1 29.1 29.1 29.1 29.1 20 k = MCp 8. 1.40 1.399 1.399 1.399 1.399 1.399 1.399 1.400 21 Cp S = R.k /(k-1), (k J /kg.k) 1.02 1.026 1.026 1.026 1.026 1.026 1.026 1.025 22 DSs = 100.ps.R.Ts), (kg/m3) 1.1 1.8 3.1 5.3 9.0 15.2 25.8 #VALUE! 23 Q S = G / DSs, ( m3/hr) 10681.1 6500.0 3836.9 2264.9 1337.0 789.2 465.9 #VALUE! 24 r' 1.694 1.694 1.694 1.694 1.694 1.694 1.694 1.694 25 Discharge pressure, pd (bara) 1.665 2.820 4.777 8.093 13.710 23.226 39.346 #VALUE! 26 Cylinder exh p 1.715 2.905 4.921 8.336 14.121 23.922 40.526 #VALUE! Eq. A8 27 Clearance space vol ume, c (%) 5.0 5.0 5.0 5.0 5.0 5.0 5.0 5.0 28 Volumetric efficiency, η V 0.928 0.928 0.928 0.928 0.928 0.928 0.928 0.928 Eq. A4 29 Supply efficiency, λ/η V 0.980 0.980 0.980 0.980 0.980 0.980 0.980 0.980 Eq. A5 30 Required pist on capacity, Qp ( m3) 11740.1 7144.6 4217.4 2489.5 1469.5 867.5 512.1 #VALUE! Eq. A7 31 Preliminary Piston speed (m/s) 2.5 2.5 2.5 2.5 2.5 2.5 2.5 2.5 32 Stroke leng, ( ) 430 430 430 430 430 430 430 430 33 No. of compression acting 2 2 2 2 2 2 2 2 34 No. of throw st z 3 2 2 1 1 1 1 0 Fill for D < Dmax 35 Crankshaft d, 200 200 200 200 200 200 200 200 36 Piston speed, (m/s) 2.9 2.9 2.9 2.9 2.9 2.9 2.9 2.9 Eq. 12, max. 6 m/s 3 37 Piston displacement vol./strok e, m 0.163 0.149 0.088 0.104 0.061 0.036 0.021 #VALUE! 38 Piston di t ( ) 694.3 663.3 509.6 553.7 425.4 326.9 251.1 #VALUE! Max.(mm)= 717 39 Compression continue? Continue Continue Continue Continue Continue Continue Finish - 40 GHP IS 193 193 193 193 193 193 193 0 Eq. 9 41 Average Isothermal efficiency 0.750 42 Total GHP (kw) 1802.76 43 Mechanical efficiency 0.94 Fig. A4 44 Total BHP (kw) 2557

RECIPRCATING CMPRESSR CALCULATIN SHEET ISTHERMAL CMPRESSIN Gas properties, flowrate and conditions 1 Gas name Air Item or symbol Quantity Unit Item or symbol Quantity Unit Formula 2 Suction pressure, ps 1.013 bar A Discharge pressure, pd 38.2 bar A 3 Suction temperature, ts 35 C Head (m) : 4 Ts 308 K p CR 37.70 bar A H IS =234.86 R.T1{ Log (r')+ 0.05} 5 MW 28.4 kg/kgmol T CR 132.80 K Gas horse power (kw) : 6 k S 1.400 p R = p / p CR 0.027 GHP IS =0.064 Q1.p1.{ Log (r')+ Δ C }/Z1 7 R S 0.293 kj/kg. K T R = T / T CR 2.32 ΔC is approx.< 0.05 for Δp < 50 bar 8 DSs 1.123 kg/m3 Z S 1.00,p<200 bar A and temperature at 9 MCp 29.14 kj/kgmol. K Cp S 1.025 kj/kg near 50 C for each stage 10 G 6000 kg/hr G mol 211 kgmol/hr 11 Q S 5341 m 3 /hr Q N 4734 Nm 3 /hr Q1 capacity (m3/hr) at refference 12 pressure p1 and t1 Compressor Calculation Sheet Item Symbol Unit Quantity Note 13 Preliminary Calculation (General method) 14 Adiabatic compression 15 First Stage Volume flow Qs m3/hr 5341 16 Cylinder intake pressure ps' bara 0.98261 17 Cylinder exhaust pressure pd' bara 39.346 18 Pressure ratio (p D / p S ) r total - 40.042 19 (k-1)/k - 0.2857 20 k/(k-1) - 3.500 21 Total Hydrodynamic head H IS-TTAL m 34994 22 Expected isothermal eff. 0.750 Average isothermal efficiency is approximatelly 0.63 (medium size) up to 0.70 (large) 23 24 Frame BHP selection at first stage Casing I 25 No. of compression acting 1 Fig. A.2/A.3 Approx. no. of stage, i 4 26 Stroke length, L mm 400 Fig. A.2/A.3 Approx. pressure ratio, r' 2.5155 = r TTAL (1 / I ) 27 No. of throw at first stage, z 4 Fig. A.2/A.3 for each stage 28 Crankshaft speed, N RPM 200 Fig. A.1 29 Max. diameter, Dmax (= L / 0.6 ) mm 667 30 No. of frame 1 31 Calculated frame BHP/throw, 0.11 Qp1 kw 185 App. (A.4) 32 Max. H per throw m 8470 Eq.A.11

1 Detail calculation Note 2 Stage 1 Stage 2 Stage 3 Stage 4 Stage 5 Stage 6 Stage 7 Stage 8 3 Mass flow, G 6000 6000 6000 6000 6000 6000 6000 6000 4 Max. H per stage for parallel throws 8469.9 8469.9 8469.9 8469.9 8469.9 8469.9 8469.9 8469.9 5 Last cylinder exhaust press. (bara) 39.346 39.346 39.346 39.346 39.346 39.346 39.346 39.346 6 p1 1.013 1.013 1.013 1.013 1.013 1.013 1.013 1 Refference condition in 7 t1 35 35 35 35 35 35 35 35 this sheet is equal with 8 Q1 5340.5 5340.5 5340.5 5340.5 5340.5 5340.5 5340.5 5341 intake condition 9 Cyl. intake pressure, ps ' (bara) 0.98 2.472 6.218 15.641 - - - - 10 Suction temperat ure, ts ( C) 35.0 35.0 35.0 35.0 35.0 35.0 35.0 35.0 11 Ts ( K) 308.0 308.0 308.0 308.0 308.0 308.0 308.0 308.0 12 MW 28.40 28.40 28 28 28 28 28 28 13 Rs = 8.314/MW 0.29 0.29 0.29 0.29 0.29 0.29 0.29 0.29 14 p CR 37.7 37.7 37.7 37.7 37.7 37.7 37.7 37.7 15 T CR 132.8 132.8 132.8 132.8 132.8 132.8 132.8 132.8 16 p R = p RED = p / pcr 0.03 0.066 0.16 0.41 #VALUE! #VALUE! #VALUE! #VALUE! 17 T R = T RED = T / T CR 2.32 2.319 2.32 2.32 2.32 2.32 2.32 2.32 18 Z S 1 1 1 1 1 1 1 1 19 MCp S (kj/kgmo l.k) 29.14 29.1 29.1 29.1 29.1 29.1 29.1 29.1 20 k = MCp 8. 1.40 1.399 1.399 1.399 1.399 1.399 1.399 1.400 21 Cp S = R.k /(k-1), (k J /kg.k) 1.02 1.026 1.026 1.026 1.026 1.026 1.026 1.025 22 DSs = 100.ps.R.Ts), (kg/m3) 1.1 2.7 6.9 17.3 #VALUE! #VALUE! #VALUE! #VALUE! 23 Q S = G / DSs, ( m3/hr) 5340.5 2188.7 870.1 345.9 #VALUE! #VALUE! #VALUE! #VALUE! 24 r' 2.516 2.516 2.516 2.516 2.516 2.516 2.516 2.516 25 Discharge pressure, pd (bara) 2.472 6.218 15.641 39.346 #VALUE! #VALUE! #VALUE! #VALUE! 26 Cylinder exh p 2.546 6.404 16.110 40.526 #VALUE! #VALUE! #VALUE! #VALUE! Eq. A8 27 Clearance space vol ume, c (%) 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 28 Volumetric efficiency, η V 0.941 0.941 0.941 0.941 0.941 0.941 0.941 0.941 Eq. A4 29 Supply efficiency, λ/η V 0.958 0.958 0.958 0.958 0.958 0.958 0.958 0.958 Eq. A5 30 Required pist on capacity, Qp ( m3) 5923.7 2427.7 965.1 383.6 #VALUE! #VALUE! #VALUE! #VALUE! Eq. A7 31 Preliminary Piston speed (m/s) 3 3 3 3 3 3 3 3 32 Stroke leng, ( ) 400 400 400 400 400 400 400 400 33 No. of compression acting 1 1 1 1 1 1 1 1 34 No. of throw st z 4 2 1 1 0 0 0 0 Fill for D < Dmax 35 Crankshaft d, 200 200 200 200 200 200 200 200 36 Piston speed, (m/s) 2.7 2.7 2.7 2.7 2.7 2.7 2.7 2.7 Eq. 12, max. 6 m/s 3 37 Piston displacement vol./strok e, m 0.123 0.101 0.080 0.032 #VALUE! #VALUE! #VALUE! #VALUE! 38 Piston di t ( ) 626.2 566.9 505.5 318.7 #VALUE! #VALUE! #VALUE! #VALUE! Max.(mm)= 667 39 Compression continue? Continue Continue Continue Finish - - - - 40 GHP IS 156 156 156 156 0 0 0 0 Eq. 9 41 Average Isothermal efficiency 0.750 42 Total GHP (kw) 832.13 43 Mechanical efficiency 0.94 Fig. A4 44 Total BHP (kw) 1180

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