Irreversible Process to Move Gas from State 1 to State 2

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SUMMARY

The discussion centers on the theoretical exploration of an irreversible process to transition an ideal gas from state 1 to state 2, characterized by higher pressure, temperature, and volume. Participants examine the feasibility of achieving this in a single step, contrasting it with a two-step process involving isentropic compression followed by isothermal expansion. The concept of a polytropic process, defined by the relationship \(PV^n = \text{const}\), is highlighted as a potential method, with discussions on the necessary conditions for achieving the desired state changes. Ultimately, a practical example involving a hot liquid injected into a gas-filled cylinder is proposed, demonstrating that such a one-step process can be theoretically achieved under specific conditions.

PREREQUISITES
  • Understanding of ideal gas laws and state equations
  • Knowledge of thermodynamic processes, including isentropic and isothermal processes
  • Familiarity with polytropic processes and the polytropic index
  • Basic principles of heat transfer and work in thermodynamic systems
NEXT STEPS
  • Research the mathematical modeling of polytropic processes in thermodynamics
  • Explore the implications of the second law of thermodynamics on irreversible processes
  • Study the effects of heat transfer on gas behavior during expansion and compression
  • Examine real-world applications of polytropic processes in engineering systems
USEFUL FOR

This discussion is beneficial for thermodynamics students, mechanical engineers, and researchers interested in advanced gas behavior and thermodynamic process optimization.

  • #31
Here is my entropy change analysis for the irreversible path suggested by @mfig. If we apply the first law of thermodynamics to his path, we obtain $$mC_v(T_2-T_1)=Q-P_2(V_2-V_1)$$where ##P_2=(M_P+M_L)g/A## is the final pressure. Applying the ideal gas law to the work term in the above equation then gives: $$mC_v(T_2-T_1)=Q-mRT_2(1-\frac{V_1}{V_2})\tag{1}$$
Even though the present irreversible path bears little resemblance to the reversible polytropic path analyzed previously, as pointed out in post #29, we can still use the polytropic parameterization in terms of the polytropic parameter n to establish the final state of the gas, such that the range of values for the single parameter n from 0 to ##-\infty## span all possible final states of the gas for which the final pressure and final volume are greater than their values in the initial state. With this in mind, combining Eqn. 2 of post #29 with Eqn. 1 of the present develop gives:$$mC_v(T_2-T_1)=Q-mRT_2\left[1-\left(\frac{T_1}{T_2}\right)^{\frac{1}{1-n}}\right]\tag{2}$$From this, it follows that the total heat flow over the irreversible path is given by:$$Q=mC_v(T_2-T_1)+mRT_2\left[1-\left(\frac{T_1}{T_2}\right)^{\frac{1}{1-n}}\right]\tag{3}$$Since, for this irreversible path, all the heat transfer at the boundary takes place at the final temperature ##T_2##, the integral of dQ divided by the boundary temperature (i.e., the boundary where the heat flow occurs) is just equal to ##Q/T_2##: $$\int{\frac{dQ}{T_{boundary}}}=\frac{Q}{T_2}$$$$=mC_v\left(1-\frac{T_1}{T_2}\right)+mR\left[1-\left(\frac{T_1}{T_2}\right)^{\frac{1}{1-n}}\right]\tag{4}$$Calculations show that, for all values of (1) the "final state parameter" n in the range 0 to ##-\infty##, (2) the heat capacity ratio parameter ##1<\gamma<1.67##, and (3) the overall temperature ratio ##\frac{T_2}{T_1}>1## the integral of ##dQ/T_{boundary}## calculated from Eqn. 4 for this irreversible process path is less than the entropy change between the initial and final states calculated from Eqn. 3 of post #29 for the 2-step reversible path (or the reversible polytropic path). For example, for n = -1, ##\gamma=1.4##, and ##\frac{T_2}{T_1}=2##, we find that ##dQ/T_{boundary}=0.617mC_v## while ##\Delta S =0.832mC_v##. This is consistent with the Clausius inequality, which represents a mathematical statement of the 2nd law of thermodynamics.
 
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