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please find below the solution
to the problem. As working medium is not given so here we have to
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3. Complete the table considering the fact that Cp, and C, are not constant. as Gabon...
Part A Constants | Periodic Table The molar heat capacity Cp,m of SO2 (g) is described by the fol...
Please help me solve for delta H, I can't get it.
Thank you!
Part A Constants | Periodic Table The molar heat capacity Cp,m of SO2 (g) is described by the following equation over the range 300 K
Using the data reported in the table and 5°(298 K) considering Cp(T) = a + bt,...
Using the data reported in the table and 5°(298 K) considering Cp(T) = a + bt, calculate the molar standard entropy for: нь (a) Water vapor at 100°C. (20 points) (b) Water vapor at 200°C. (20 points) (C) Write a short comment on your results. (5 points) 188.8 J-K-1.mor 30.5 J.K-1.mol-1 10.3x10-3 J-K-2.mol-1
The molar heat capacity Cp m of SO2 (g) is described by the following equation over...
The molar heat capacity Cp m of SO2 (g) is described by the following equation over the range 300 K< T < 1700 K 45.81 x 10-7 T2 ка Cp +1.035 x 10-9 Ț3. кз 3.093 6.967 x 10-3 In this equation, T is the absolute temperature in kelvin. The ratios T"/K" ensure that Cp.m has the correct dimension. 1.65 moles of SO2 (g) is heated from 29.0 C to 1130 ° C at a constant pressure of 1 bar
Not sure how to do last one, can anyone help? Problem 3 Complete this table for...
Not
sure how to do last one, can anyone help?
Problem 3 Complete this table for water Phase Description P (psia) 67.2% 40 120 400 T (°F) u (Btu/lbm) 782 Sat axture 300 8ら6.og | saturated Liqu 267,22 74. SHV 500 400
Complete the following table for Refrigerant-134a. Use data from the steam tables. T,°C P, kPa u...
Complete the following table for Refrigerant-134a. Use data from the steam tables. T,°C P, kPa u kJ/kg 20 95 -12 Phase description (Click to select) Saturated liquid (Click to select) (Click to select) 300 400 600 8
I. (30 pts.) One mole of an ideal gas with constant heat capacities and ? 5/3...
I. (30 pts.) One mole of an ideal gas with constant heat capacities and ? 5/3 is compressed adiabatically in a piston-cylinder device from T1-300 K, pi = 1 bar to p2 = 10 bar at a constant external pressure Pext"- P2 -10 bar. Calculate the final temperature, T2, and W, Q. AU, AH for this process. 2. (20 pts.) Repeat problem 1 for an adiabatic and reversible compression. 3. (20 pts.) A rigid, insulated tank is divided into two...
Assuming constant pressure, calculate ΔU for the heating of 3 moles of Cu(s) from 300 K...
Assuming constant pressure, calculate ΔU for the heating of 3 moles of Cu(s) from 300 K to 600 K. Cp,m = 16,1324.44 J/mol•K
Question 5 (2.0 pts) Assume that Cp for an ideal gas is given by co(T) =...
Question 5 (2.0 pts) Assume that Cp for an ideal gas is given by co(T) = 0.9 + 2.5 x 10-* T, in kJ/kg-K, where is the temperature in Kelvin. (Use the gas constant R = 0.3 kJ/kg-K) (a) (+0.4) Derive an expression for Cy as a function of temperature. The gas undergoes an isochoric process from a temperature T, = 400 K to T2 = 500 K. Calculate the change in (b) (+0.6) enthalpy, in kJ/kg, (c) (+0.6) entropy,...
Total costs in the table are: Select one: a. decreasing at a decreasing rate. b. decreasing...
Total costs in the table are: Select one: a. decreasing at a decreasing rate. b. decreasing at a constant rate. c. increasing at a constant rate. d. increasing at an increasing rate. | M Control variable e 0 Total Benefits B(Q) arginal Benefit MB(Q) Marginal Cost MC(Q) Marginal Net Benefit MNB(Q) 0 900 1,700 100 200 Total Costs C(Q) 0 100 300 600 1,000 1,500 2,100 2,800 B 4,500 5,500 Net Benefits N(Q) 0 800 C 1,800 2,000 2,000 1,800...
Fill in the table with the appropriate response Topic is Accelerator principle of investment Drawing Assume...
Fill in the table with the appropriate response
Topic is Accelerator principle of investment
Drawing Assume a capital ratio of 2:1 Desired output level Demand (K Output level) Level of Net Investment 200 220 250 300 400 400- 440 500 600 800 1200 1400 600 700 P
Please help me solve for delta H, I can't get it.
Thank you!
Part A Constants | Periodic Table The molar heat capacity Cp,m of SO2 (g) is described by the following equation over the range 300 K
Using the data reported in the table and 5°(298 K) considering Cp(T) = a + bt, calculate the molar standard entropy for: нь (a) Water vapor at 100°C. (20 points) (b) Water vapor at 200°C. (20 points) (C) Write a short comment on your results. (5 points) 188.8 J-K-1.mor 30.5 J.K-1.mol-1 10.3x10-3 J-K-2.mol-1
The molar heat capacity Cp m of SO2 (g) is described by the following equation over the range 300 K< T < 1700 K 45.81 x 10-7 T2 ка Cp +1.035 x 10-9 Ț3. кз 3.093 6.967 x 10-3 In this equation, T is the absolute temperature in kelvin. The ratios T"/K" ensure that Cp.m has the correct dimension. 1.65 moles of SO2 (g) is heated from 29.0 C to 1130 ° C at a constant pressure of 1 bar
Not
sure how to do last one, can anyone help?
Problem 3 Complete this table for water Phase Description P (psia) 67.2% 40 120 400 T (°F) u (Btu/lbm) 782 Sat axture 300 8ら6.og | saturated Liqu 267,22 74. SHV 500 400
Complete the following table for Refrigerant-134a. Use data from the steam tables. T,°C P, kPa u kJ/kg 20 95 -12 Phase description (Click to select) Saturated liquid (Click to select) (Click to select) 300 400 600 8
I. (30 pts.) One mole of an ideal gas with constant heat capacities and ? 5/3 is compressed adiabatically in a piston-cylinder device from T1-300 K, pi = 1 bar to p2 = 10 bar at a constant external pressure Pext"- P2 -10 bar. Calculate the final temperature, T2, and W, Q. AU, AH for this process. 2. (20 pts.) Repeat problem 1 for an adiabatic and reversible compression. 3. (20 pts.) A rigid, insulated tank is divided into two...
Question 5 (2.0 pts) Assume that Cp for an ideal gas is given by co(T) = 0.9 + 2.5 x 10-* T, in kJ/kg-K, where is the temperature in Kelvin. (Use the gas constant R = 0.3 kJ/kg-K) (a) (+0.4) Derive an expression for Cy as a function of temperature. The gas undergoes an isochoric process from a temperature T, = 400 K to T2 = 500 K. Calculate the change in (b) (+0.6) enthalpy, in kJ/kg, (c) (+0.6) entropy,...
Fill in the table with the appropriate response
Topic is Accelerator principle of investment
Drawing Assume a capital ratio of 2:1 Desired output level Demand (K Output level) Level of Net Investment 200 220 250 300 400 400- 440 500 600 800 1200 1400 600 700 P
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