Exam 1 Prep Review

Problem Solving for Exam Preparation

Introduction

  • The session focuses on solving problems in preparation for an upcoming exam.
  • The speaker encourages students to interrupt for clarification if necessary.

Problem 1: Isothermal Compressibility and Work Done in Isobaric Process

  • Initial Given Information:
    • Isothermal compressibility and volume expansivity values are provided.
    • The goal is to find the work needed to isobarically raise the temperature of a real fluid.
  • Key Assumption:
    • Assume the process is reversible, simplifying calculations.
  • Work Calculation Steps:
    • Work, $W = - ext{e} dB$, where $ ext{e}$ is the isothermal compressibility. In this case, $W = -P dV$ because it is an isobaric process.
    • The isobaric compressibility relationship provides:
      β=1V(VT)V\beta = \frac{1}{V} \left( \frac{\partial V}{\partial T} \right)_V
    • For volume changes, perform integration of the equation using separation of variables:
    • dBV=βdT\frac{dB}{V} = \beta dT
    • Integrate from initial state to final state:
      ln(V<em>2V</em>1)=β(T<em>2T</em>1)\ln \left( \frac{V<em>2}{V</em>1} \right) = \beta (T<em>2 - T</em>1)
  • Volume Change Calculation:
    • Rearranging yields:
      V<em>2=V</em>1eβ(T<em>2T</em>1)V<em>2 = V</em>1 e^{\beta (T<em>2 - T</em>1)}
    • Calculate $V_2$ as 0.506 liters/kg, given specific numerical values from the problem.
  • Work Calculation Details:
    • Substitute into the work expression: W=PV<em>2+PV</em>1W = -PV<em>2 + PV</em>1
    • Be cautious of units:
    • Convert bar to Pascal and liters to cubic meters to maintain SI units.
    • Completed calculations yield $W = 140.56$ joules.
  • Critical Thinking on Work Sign:
    • Clarified potential confusion on sign error; the work should be negative due to increasing volume driven by temperature increase in isobaric conditions.

Problem 2: Turbine Work and Efficiency Calculation

  • Scenario Overview:
    • An elevator powered by a steam turbine with energy transfer efficiency of 80%.
  • Key Goals:
    • Determine work done by the turbine in two scenarios: adiabatic and non-adiabatic (losing heat).
  • System Definition:
    • The turbine is the defined system, crucial for analyzing energy transfer.
    • Establish mass flow rate based on problem parameters: m˙=5\dot{m} = 5 kg/s.
  • Power Requirements:
    • Total power requirement for the elevator is 2,500 kW leading to:
      W=25000.8=3125kJ/sW = -\frac{2500}{0.8} = -3125 kJ/s
  • Material and Energy Balance:
    • Apply the steady-state material balance:
    • Mass in = Mass out = 5 kg/s.
    • Energy balance (adiabatic):
    • Since $Q = 0$, the equation simplifies to:
      m˙(H<em>2H</em>1)=W\dot{m} (H<em>2 - H</em>1) = W
  • Enthalpy Determination:
    • Enthalpy at the inlet ($H_1$) is given from steam tables for superheated steam.
    • Substitute enthalpy values to solve for $H2$: H</em>2=W/m˙+H1H</em>2 = W/\dot{m} + H_1
    • Example values result in: $H_2 = 2823$ kJ/kg.
    • Determine temperature at outlet using interpolation between temperature and enthalpy tables. Results in: 172 °C from provided enthalpy values.
  • Scenario B (non-adiabatic):
    • Update energy balance with heat loss, now $Q = 500 kJ/s$.
    • Rearranging yields:
      H<em>2=W+Qm˙+H</em>1H<em>2 = \frac{W + Q}{\dot{m}} + H</em>1
    • Calculate new enthalpy as $H_2 = 2720$ kJ/kg, and interpolate for outlet temperature, resulting in 121.8 °C.

Problem 3: Ideal Gas Behavior during Heating, Compression, and Cooling

  • Process Overview:
    • A cycle involving isobaric heating, adiabatic compression, and isochoric cooling of an ideal gas.
    • Initial conditions specified: 1 bar, 300 K to be heated to 750 K.
  • Isobaric Heating:
    • Given that Q=ΔH=C<em>P(T</em>2T1)Q = \Delta H = C<em>P (T</em>2 - T_1),
    • Calculate values for ΔU\Delta U using $C_V$.
    • Net work is deduced from ΔU=Q+W\Delta U = Q + W. Resulting in $W = -3741.3$ J/mol for this process.
  • Adiabatic Process:
    • For adiabatic compression, establish conditions:
    • $Q = 0$, apply relevant enthalpy and internal energy equations. Results need validating through known relationships like $h$, $u$, or both.
  • Isochoric Cooling:
    • Confirm $W = 0$ due to constant volume conditions.
    • Final checks on the overall cycle must confirm the cyclical nature where net changes should reach 0 for ΔU\Delta U and ΔH\Delta H.
  • Graphical Representation:
    • Outline of process expected to capture state changes effectively on PV diagrams, with critical consideration for behaviours of adiabatic processes (concave up forms as temperature drops).
  • Summary Checks:
    • Validate overall energy and heat exchanges across the full cycle emphasizing the conservation first law. Conditions like $Q$ and $W$ should balance appropriately per the first law's implications.

Reflection on Problem Solving Strategy

  • Keywords Identification:
    • For Problem 1: "isobaric" was crucial for simplifying assumptions.
    • For Problem 2: "80% efficiency" and "loses heat" dramatically shaped equations.
    • For Problem 3: "isobaric", "adiabatic", and "isochoric" clearly outlined steps and expectations for energy transfers.
  • Preparation involves recognizing and isolating these key terms to facilitate clear logical pathways through problems.

Conclusion

  • The session concludes with reminders on exam focus and availability for questions.
  • Highlights thorough systematic approaches in handling thermodynamic problems and emphasizes critical thinking, careful reading of questions, and the significance of units throughout calculations.