sara lopez
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because i have for a =1,358 bar (m^3/kmol)^2 and b= 0,0364 m^3/kmolsara lopez said:bar*m^3 and then pass them to BTU
The discussion revolves around the calculation of work done by air during expansion in a cylinder, specifically under the assumption of a reversible process described by the equation P.V1.4 = constant. Participants explore the implications of using the Van der Waals equation versus ideal gas assumptions in this context.
Participants do not reach a consensus on the best approach to calculate the work done during the expansion, with ongoing debate about the applicability of the Van der Waals equation versus ideal gas assumptions. Uncertainty remains regarding the assumptions made about the number of moles and the initial temperature.
Participants note limitations in their assumptions, particularly regarding the number of moles and the initial temperature, which affect the calculations. There is also a lack of clarity about the conditions under which the Van der Waals equation can be applied compared to ideal gas behavior.
because i have for a =1,358 bar (m^3/kmol)^2 and b= 0,0364 m^3/kmolsara lopez said:bar*m^3 and then pass them to BTU
Why would that give a negative temperature?sara lopez said:because i have for a =1,358 bar (m^3/kmol)^2 and b= 0,0364 m^3/kmol
P2 is -48,354 BarChestermiller said:Why would that give a negative temperature?
0.0364 m^3/kmol = 0.0000364 m^3/molsara lopez said:because the volume molar is less than b
sorry, now the temperature 2 = 15304,4 K, isn't high?Chestermiller said:0.0364 m^3/kmol = 0.0000364 m^3/mol
1 mole is obviously too few. Try 100 moles.sara lopez said:sorry, now the temperature 2 = 15304,4 K, isn't high?
n= 100, T2= 15771,3Chestermiller said:1 mole is obviously too few. Try 100 moles.
How is that possible?sara lopez said:n= 100, T2= 15771,3
yes, you are right, thanks for the correctionChestermiller said:1 ft^3 = 28.3 liters
1500 psi = 102.0 atm.
n = 100 moles
IDEAL GAS LAW
$$T_1=\frac{PV}{nR}=\frac{(28.3)(102.0)}{(100)(0.0821)}=352 K$$
VAN DER WAAL EQUATION
a=1.344 atm (liters/mole)^2
b=0.0364 (liters/mole)
$$T_1=\frac{(28.3-3.64)(102+(13440)/(28.3^2))}{(100)(0.0821)}=358 K$$