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Introduction

  • Doctor Ojo discussing thermodynamics, focusing on the first law and related principles.
  • Problem presented involving an ICE engine with pressures and specific volume.

Problem Statement

  • Initial conditions:
    • Pressure: P1=420extkN/m2P_1 = 420 ext{ kN/m}^2
    • Specific Volume: V1=0.14extm3/extkgV_1 = 0.14 ext{ m}^3/ ext{kg}
  • Final conditions:
    • Pressure: P2=35extkN/m2P_2 = 35 ext{ kN/m}^2
  • Relationship: PV2=CPV^2 = C

Calculation of Work Done

  • Finding the work done by the fluid on the piston:

    • The equation PV2=CPV^2 = C relates initial and final states.
    • Initial state: C=P1V12C = P_1 V_1^2
    • Substitute values:
      • C=420imes103imes(0.14)2C = 420 imes 10^3 imes (0.14)^2
    • Simplification gives:
      • C
        ightarrow 8.59 ext{ N m/kg}
  • Calculating final specific volume, V2V_2:

    • Formula for V2V_2:

    V2=extsqrtCPV_2 = ext{sqrt}\frac{C}{P}

    • Substitute CC and P2P_2:

    V2=extsqrt8.58835V_2 = ext{sqrt}\frac{8.588}{35}

    • Result:
    • V_2
      ightarrow 0.495 ext{ m}^3/ ext{kg}
  • Work done (W):

    • Formula for work done:

    W=extintegralfromV1exttoV2extofPextdVW = ext{integral from } V_1 ext{ to } V_2 ext{ of } P ext{ dV}

  • Substitute PP:

    P=CV2P = \frac{C}{V^2}

  • Work calculation:

    • W=Cimesextintegral1V2dVW = C imes ext{integral}\frac{1}{V^2}dV
  • Evaluate integral:

    • W=Cimes[−1V]V1V2W = C imes \bigg[-\frac{1}{V}\bigg]_{V_1}^{V_2}
  • Applying limits:

    • W=8.588imes1000imes(−10.143+10.495)W = 8.588 imes 1000 imes \bigg(-\frac{1}{0.143} + \frac{1}{0.495}\bigg)
  • Final answer for work done:

    • W
      ightarrow 42.71 ext{ kJ/kg}

First Law of Thermodynamics

  • Definition: Related to the law of conservation of energy, stating:
    • Energy cannot be created or destroyed.
    • Energy can change forms.
  • Equation: Change in internal energy () in a closed system can be expressed as:
    • extΔU=Q−Wext{ΔU} = Q - W
    • Where:
    • QQ: energy added to the system
    • WW: work done by the system
  • Analogy with Pressure Pot:
    • Energy in water due to intermolecular interactions.
    • Heating leads to increased pressure, allowing the release of pressure (e.g., whistle).

Work Done and Heat Flow

  • Heat and Work Flow Behavior:
    • Work on the system from surroundings is negative.
    • Work done by the system on surroundings is positive.
    • Heat flow into the system is positive; heat flow out of the system is negative.
  • Equilibrium State Concept:
    • An equilibrium state has an internal energy state variable.
    • Energy transition between equilibrium states involves heat transfer and work.

Process Terminologies

  • Types of Processes:
    • Adiabatic Process: No heat transfer.
    • Q=0Q = 0, hence extΔU=−Wext{ΔU} = -W (positive change in internal energy).
    • Isothermal Process: Constant temperature.
    • extΔU=0ext{ΔU} = 0, therefore Q=WQ = W.
    • Isobaric Process: Constant pressure.
    • W=PimesextΔVW = P imes ext{ΔV}.
    • Isochoric Process: Constant volume.
    • No work done W=0W = 0, hence extΔU=Qext{ΔU} = Q.

Polytropic Process

  • Definition: Involves various states characterized by heat capacities and indices.
  • Example of Work Calculation:
    • Given: 500 J heat added to two moles of monatomic gas at 500 K.
    • Work done: 750 J
    • Use internal energy relationships for calculating final temperature.

Flow Processes

  • Types of Flow:
    • Steady Flow: Parameters (velocity, pressure, density) are constant over time.
    • Unsteady Flow: Fluctuating parameters over time.
  • Steady Flow Energy Equation (SFEE):
    • Total energy per unit mass:
      PV=U+KE+PEPV = U + KE + PE
    • Where KE: kinetic energy, PE: potential energy due to height.

Energy Change Equation

  • Formulation for energy change:
    • extΔE=P2V2+(U2+C222+gz2)−P1V1−(U1+C122+gz1)ext{ΔE} = P_2 V_2 + \bigg(U_2 + \frac{C_2^2}{2} + g z_2\bigg) - P_1 V_1 - \bigg(U_1 + \frac{C_1^2}{2} + g z_1\bigg)
  • Net Heat and Work Relation:
    • Energy change relates to heat supplied minus work done:
    • Q−W=H2−H1+ext(KEandPEcontributions)Q - W = H_2 - H_1 + ext{(KE and PE contributions)}

Mass Flow Rate

  • Steady Flow Condition:
  • Mass flow rate at inlet equals mass flow rate at outlet:
    • ext{ṁ} =
      ho_1 V_1 A_1 =
      ho_2 V_2 A_2 where:

    • ho: Density,
    • VV: Velocity,
    • AA: Cross-sectional area

Pure Substances

  • Definition: Substances with homogenous and invariable chemical composition.
  • Characteristics:
    • Example substances: Nitrogen, Oxygen, Water (H2O), etc.
    • Phases of substances: solid (ice), liquid (water), gaseous (steam).
    • Properties change with phase transitions influenced by pressure and temperature.

Phase Change Terminologies

  • Transitions:
    • Melting: solid to liquid
    • Evaporation: liquid to gas
    • Deposition: gas to solid
    • Sublimation: solid to gas
    • Triple Point: simultaneous presence of all phases.
  • Steam Tables:
    • Capture intrinsic properties (pressure, volume, temperature).
  • Boiling Point:
    • Water boils at 100°C at 1 atmosphere.

STEAM Table Properties

  • Key Variables:
    • Saturated Pressure, Saturated Temperature, Specific Volume, Internal Energy, Enthalpy, Entropy, etc.
  • Conversion of units (bar to Pascal):
    • 1extbar=105extN/m21 ext{ bar} = 10^5 ext{ N/m}^2

Interpolation in Steam Tables

  • Interpolation Concept:
  • Used to derive unknown values between two known values:
    • Textunknown−TextlowTexthigh−Textlow=Hextunknown−HextlowHexthigh−Hextlow\frac{T_{ ext{unknown}} - T_{ ext{low}}}{T_{ ext{high}} - T_{ ext{low}}} = \frac{H_{ ext{unknown}} - H_{ ext{low}}}{H_{ ext{high}} - H_{ ext{low}}}
  • Example: Finding enthalpy at 31°C using known values at 30°C and 32°C.

Example Problem on Saturated System

  • Case: Rigid tank with 10 kg of water at 90°C.
    • 8 kg in liquid state, 2 kg in vapor state.
  • Steps to find:
    1. Determine tank pressure using steam table for 90°C; pressure ≈ 0.011 bar.
    2. Convert to SI units: 0.011imes105extN/m20.011 imes 10^5 ext{ N/m}^2.
    3. Calculate total volume using mass and specific volumes of liquid and vapor.
    • Use dryness fraction for calculations:
    • X=extmassvaporexttotalmassX = \frac{ ext{mass vapor}}{ ext{total mass}}.

Conclusion

  • These principles form the foundation of thermodynamics and its applications in systems analysis, understanding energy transfer, and process dynamics in engineering.
  • The material serves to enhance comprehension of how various thermodynamic laws apply to real-world scenarios in fluid mechanics and thermodynamics.