derive cp=(Rln(p2/p1))/(ln(t1/t2)) from gibbs and discuss assumptions you make
derive cp=(Rln(p2/p1))/(ln(t1/t2)) from gibbs and discuss assumptions you make
Given ln (P2/P1) = -Delta HVAP/R (1/T2-1/T1). Find the Delta H Vap for C6H6 if the boiling point is 80.5*C and P2=1.5 at 95*C
The Clausius-Clapeyron equation is: ln (P2/P1)=-(dHvap/R)(1/T2-1/T1). My question is: Why the equation I have seen in a lot of answers has 1/T1 - 1/T2????
If water boils at 96°C what is the ambient pressure? Show use of formula ln(P2/P1)= (?️Hvap/R)*(1/T1 - 1/T2) ?️Hvap= 40.7 kJ/mol R= 8.312 J/mol*K
T1=4C P1=369.01 kpa P2=200kpa find T2 if volumen is contant
Thermo Question I have a reversible turbine, I am given T1,T2, and P1. I need to find P2 using variable specific heat method. NOT THE CONSTANT SPECIFIC HEAT METHOD.What equation would I use? also, the turbine takes in air. I know I would use steam tables for this part. Please let me know, thank you. ***Note that the constant specific heat method is p2 = p1(T2/T1)^(k/k-1).. I am not talking about this method. Thanks.
One mole of an ideal gas is taken from the initial state (P1=1atm,T1=298K) to a final state (P2=10atm,T2=298K). Calculate Delta G.
Thermo Question I have a reversible turbine, I am given T1,T2, and P1. I need to find P2 using variable specific heat method. What equation would I use? also, the turbine takes in air. I know I would use steam tables for this part. Please let me know, thank you.
4. Starting from the first law of thermodynamics and the ideal gas law, derive the relation between T2/T1 and P2/P1, in a isentropic compression, where subscripts 1 and 2 indicate the start and end of the process.
Water vapor is cooled in a closed, rigid tank from T1=660 degree Celsius and p1= 100 bar to a final temperature of T2=320 degree Celsius. Determine the final specific volume, v2 in m^3/kg, "AND THE FINAL PRESSURE, P2, IN bar".
Air undergoes an isentropic process from p1=1atm, T1=540R to a final state where the temperature is T2=1160R. employing the ideal gas model, determine the final pressure p2, in atm. Assume a constant specific ratio k evaluated at the mean temperature.