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Pressure Chp 3-A) Complete the property table based on a 1 kg sample mass of each...
Chp 3-A) Complete the property table based on a 1 kq sample mass of each substance....
Chp 3-A) Complete the property table based on a 1 kq sample mass of each substance. Substance Phase Pressure Temperature Sp. Volume Sp. Internal Energy (mkg) C) or quality (bar) (kJkg) 1) water (H2O) 300 0.085 Ccl 2) water (H2O) 1.00 -20 noint 3) water (H2O) 020 5.000 X x 0.200 4) R-134a 6.00 Liauid 5) R-134a 6.00 150 X vapor T>T Vapoi 6) R-134a 280 10 Irgle e Soldapor Specie voe
Chp 3-A) Complete the property table based on...
Question 1 Complete the following table for R-134a T. °C P, kPa 34 v, m2 /kg...
Question 1 Complete the following table for R-134a T. °C P, kPa 34 v, m2 /kg 0.019 x % Phase description Saturated mixture 280 110 700 1 Saturated vapor Superheated
Complete the following chart using the units specified, showing your work. For each chart, if a...
Complete the following chart using the units specified, showing your work. For each chart, if a property is not relevant, write ‘n/a’ for the property. Like for vapor and liquid state, x should be mentioned as ‘n/a’. If not enough information is given to complete a row, fill in what you can and draw an 'x' through the boxes that cannot be determined. V Substance State P (bar) (m²/kg) T(°C) u (kJ/kg) h (kJ/kg) R-134a 40 280 Propane 8 350...
(3) Use the vapor pressures for tetrachloromethane given in the following table to estimate the temperature...
(3) Use the vapor pressures for tetrachloromethane given in the following table to estimate the temperature and pressure of the triple point and also the enthalpies of fusion, vaporization and sublimation. Solid 230 225.7 280 340 6440 62501 Liquid 4) Calculate the change in the freezing point of water at 100. and 500. bar compared to that at 1 bar assuming that the density of the liquid and solid phases remain constant at 997 and 917 kg m, respectively. Explain...
Question 1 Using the tables for water determine the specified property data at the indicated state....
Question 1 Using the tables for water determine the specified property data at the indicated state. For H2O at p = 0.7 MPa and v = 0.51 m3/kg, find u in kJ/kg. Note: Round up the answer to 2 decimal places. Question 2 Using the tables for water determine the specified property data at the indicated state. For H2O at p = 10 MPa and u = 990 kJ/kg, find h in kJ/kg. Note: Round up the answer to 2...
Problem 3: Complete the following data based on the provided tables for water State 1: Pi...
Problem 3: Complete the following data based on the provided tables for water State 1: Pi = 200 kPa Tl-500°C State 2: P2 300 kPa T-1 160°C phase2- State 3: State 4: P 175 kPa P4 250 kPa ei phases Sat. vapor phase4 v0.630 /kg a7 Saturated water- Pressure table Specific volume m-/k Internal energy kJ/k Sat. Sat. Sat liquid, Evap, vapor, Press, temp, liquid, vapor LI 116,04 0.001057 1.0037 486.82 2037.7 2524.5 120.21 0.001061 0.88578 504.50 2024.6 2529.1 123.97...
4. Comparison of process paths: Calculate the AH for 1 kg of water going from liquid...
4. Comparison of process paths: Calculate the AH for 1 kg of water going from liquid at the triple point of water (0.01 °C and 0.0061 bar) to saturated steam (100 °C, 1 atm) by two different process paths. The two paths are defined as a. liquid water at triple point to saturated vapor at the triple point, followed by heating the saturated vapor to 0.0061 bar to saturated vapor at 1 atm. b. liquid water at triple point heated...
3. 1 kg of moist air at mixture pressure 100 kPa has a dry bulb temperature...
3. 1 kg of moist air at mixture pressure 100 kPa has a dry bulb temperature of 30°C and relative humidity of 60%. It is then cooled to a dry bulb temperature of 5°C where it reaches saturation. Without using the psychrometric chart, determine: (35 pts) i) Initial humidity ratio ii) Mass of dry air (kg) iii) Mass of condensate (kg) 720 Tables in SI Units Sal U; X 10 Temp. "C 01 00 ON A 10 11 12 13...
Chp 3-A) Complete the property table based on a 1 kq sample mass of each substance. Substance Phase Pressure Temperature Sp. Volume Sp. Internal Energy (mkg) C) or quality (bar) (kJkg) 1) water (H2O) 300 0.085 Ccl 2) water (H2O) 1.00 -20 noint 3) water (H2O) 020 5.000 X x 0.200 4) R-134a 6.00 Liauid 5) R-134a 6.00 150 X vapor T>T Vapoi 6) R-134a 280 10 Irgle e Soldapor Specie voe
Chp 3-A) Complete the property table based on...
Question 1 Complete the following table for R-134a T. °C P, kPa 34 v, m2 /kg 0.019 x % Phase description Saturated mixture 280 110 700 1 Saturated vapor Superheated
Complete the following chart using the units specified, showing your work. For each chart, if a property is not relevant, write ‘n/a’ for the property. Like for vapor and liquid state, x should be mentioned as ‘n/a’. If not enough information is given to complete a row, fill in what you can and draw an 'x' through the boxes that cannot be determined. V Substance State P (bar) (m²/kg) T(°C) u (kJ/kg) h (kJ/kg) R-134a 40 280 Propane 8 350...
(3) Use the vapor pressures for tetrachloromethane given in the following table to estimate the temperature and pressure of the triple point and also the enthalpies of fusion, vaporization and sublimation. Solid 230 225.7 280 340 6440 62501 Liquid 4) Calculate the change in the freezing point of water at 100. and 500. bar compared to that at 1 bar assuming that the density of the liquid and solid phases remain constant at 997 and 917 kg m, respectively. Explain...
Problem 3: Complete the following data based on the provided tables for water State 1: Pi = 200 kPa Tl-500°C State 2: P2 300 kPa T-1 160°C phase2- State 3: State 4: P 175 kPa P4 250 kPa ei phases Sat. vapor phase4 v0.630 /kg a7 Saturated water- Pressure table Specific volume m-/k Internal energy kJ/k Sat. Sat. Sat liquid, Evap, vapor, Press, temp, liquid, vapor LI 116,04 0.001057 1.0037 486.82 2037.7 2524.5 120.21 0.001061 0.88578 504.50 2024.6 2529.1 123.97...
4. Comparison of process paths: Calculate the AH for 1 kg of water going from liquid at the triple point of water (0.01 °C and 0.0061 bar) to saturated steam (100 °C, 1 atm) by two different process paths. The two paths are defined as a. liquid water at triple point to saturated vapor at the triple point, followed by heating the saturated vapor to 0.0061 bar to saturated vapor at 1 atm. b. liquid water at triple point heated...
3. 1 kg of moist air at mixture pressure 100 kPa has a dry bulb temperature of 30°C and relative humidity of 60%. It is then cooled to a dry bulb temperature of 5°C where it reaches saturation. Without using the psychrometric chart, determine: (35 pts) i) Initial humidity ratio ii) Mass of dry air (kg) iii) Mass of condensate (kg) 720 Tables in SI Units Sal U; X 10 Temp. "C 01 00 ON A 10 11 12 13...
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