(Chapter – 4) 1st Law of Thermodynamics: Definition of stored energy and internal energy, 1st. law of Thermodynamics of cyclic process, Non Flow Energy Equation, Flow Energy & Definition of Enthalpy, Condition for Steady State, Steady Flow; Steady State Steady Flow Energy Equation.


First Law of Thermodynamics

  • First Law = Law of Conservation of Energy.
  • Energy can neither be created nor destroyed; it can only be transferred or transformed.
  • For a thermodynamic system: Heat supplied = Increase in stored energy + Work done.
  • For a closed system: \( Q = \Delta U + W \)
  • Sign convention: \( Q > 0 \) → heat supplied to system; \( W > 0 \) → work done by system.

Stored Energy

  • Stored energy = Energy possessed by a system due to its state or position.
  • Main forms:
    • Internal energy (\( U \)) – molecular/thermal energy stored inside the system.
    • Kinetic energy (KE) = \( \frac{mV^2}{2} \)
    • Potential energy (PE) = \( mgz \)
  • Total energy of a system:\( E = U + KE + PE \)

    \( E = U + \frac{mV^2}{2} + mgz \)

Internal Energy (\( U \))

  • Internal energy = Microscopic energy associated with molecular motion and molecular interactions.
  • It is a property/state function.
  • For a pure substance, internal energy depends on its thermodynamic state.
  • \( \Delta U = U_2 – U_1 \)
  • For an ideal gas, \( U = f(T) \); therefore internal energy depends only on temperature.
  • Specific internal energy: \( u = U/m \)

First Law for a Cyclic Process

  • In a cycle, the system returns to its initial state.
  • Therefore, change in any property over one complete cycle = 0.
  • Hence: \( \Delta U = 0 \)
  • First law:\( \oint \delta Q = \oint \delta W \)
  • Therefore, for a cyclic process:Net heat supplied = Net work done
  • This law establishes conservation of energy but does not specify the direction of heat flow.

Non-Flow Energy Equation (NFEE)

  • Used mainly for a closed system where there is no mass crossing the system boundary.
  • General energy equation:

\( Q – W = \Delta U + \Delta KE + \Delta PE \)

  • Expanded form:

\( Q – W = (U_2 – U_1) + \frac{m(V_2^2 – V_1^2)}{2} + mg(z_2 – z_1) \)

  • If changes in kinetic and potential energies are negligible:

\( Q – W = \Delta U \)

  • Therefore: \( Q = \Delta U + W \)

Flow Energy

  • In an open system/control volume, fluid continuously enters and leaves.
  • Energy required to push fluid into or out of a control volume is called Flow Energy.
  • Flow energy per unit mass = \( Pv \)
  • Since \( v = 1/\rho \):Flow energy = \( P/\rho \)
  • For mass \( m \): Flow energy = \( mPv \)

Enthalpy (\( H \))

  • Enthalpy is defined as:

\( H = U + PV \)

  • Specific enthalpy:

\( h = u + Pv \)

  • Enthalpy combines:Internal energy + Flow energy
  • It is a property/state function.
  • Unit of specific enthalpy: kJ/kg.
  • For an ideal gas: \( h = h(T) \); therefore enthalpy depends only on temperature.
  • Important relation:\( \Delta h = \Delta u + \Delta(Pv) \)

Steady State

  • A system is in steady state when its properties at a fixed point do not change with time.
  • At steady state:
    • Mass inside control volume remains constant.
    • Energy stored inside control volume remains constant.
    • No accumulation of mass or energy with time.
  • For mass:Rate of mass entering = Rate of mass leaving

Steady Flow

  • Steady flow means fluid properties at a particular location remain constant with time.
  • Examples: turbine, compressor, pump, nozzle, boiler, condenser, heat exchanger.
  • For steady flow:\( \dot{m}_1 = \dot{m}_2 \) for a single-inlet, single-outlet device.
  • Mass flow rate:

\( \dot{m} = \rho A V = \frac{AV}{v} \)

Conditions for Steady-State Steady-Flow (SSSF)

  • Flow properties at a fixed point remain constant with time.
  • No accumulation of mass inside the control volume.
  • No accumulation of energy inside the control volume.
  • For one inlet and one outlet:\( \dot{m}_1 = \dot{m}_2 \)
  • Heat transfer, work transfer and mass flow may occur, but their rates remain constant with time.

Steady Flow Energy Equation (SFEE)

  • SFEE is the First Law applied to a steady-flow control volume.

\( \dot{Q} – \dot{W} = \dot{m}\left[(h_2 – h_1) + \frac{V_2^2 – V_1^2}{2} + g(z_2 – z_1)\right] \)

  • Per unit mass:

\( q – w = (h_2 – h_1) + \frac{V_2^2 – V_1^2}{2} + g(z_2 – z_1) \)

  • Using specific kinetic and potential energy:

\( q – w = \Delta h + \Delta\left(\frac{V^2}{2}\right) + \Delta(gz) \)

SFEE – Important Special Cases

Device Important assumption Energy relation
Turbine Usually \( q \approx 0 \), \( \Delta KE \) & \( \Delta PE \) small \( w \approx h_1 – h_2 \)
Compressor Usually \( q \approx 0 \), \( \Delta KE \) & \( \Delta PE \) small \( w \approx h_2 – h_1 \) input
Pump Liquid, \( \Delta KE \) & \( \Delta PE \) often considered \( w \approx h_2 – h_1 \) input
Nozzle \( q \approx 0 \), \( w = 0 \), \( \Delta PE \) small \( h_1 + \frac{V_1^2}{2} = h_2 + \frac{V_2^2}{2} \)
Diffuser \( q \approx 0 \), \( w = 0 \) Velocity decreases, pressure/enthalpy generally increases
Boiler \( w \approx 0 \), KE/PE changes small \( q \approx h_2 – h_1 \)
Condenser \( w \approx 0 \), KE/PE changes small \( q \approx h_2 – h_1 \)
Heat Exchanger No external work, usually \( q \) to surroundings \( \approx 0 \) \( \sum \dot{m} h_{in} = \sum \dot{m} h_{out} \)

Closed System vs Open System

Point Closed System Open System
Mass transfer ❌ No ✅ Yes
Energy transfer Heat/work Heat/work + flow energy
Main equation \( Q – W = \Delta U + \Delta KE + \Delta PE \) SFEE
Examples Piston-cylinder Turbine, compressor, nozzle

Most Important Formulae

  • Total energy: \( E = U + \frac{mV^2}{2} + mgz \)
  • First law: \( Q = \Delta U + W \)
  • Cyclic process: \( \oint \delta Q = \oint \delta W \)
  • NFEE: \( Q – W = \Delta U + \Delta KE + \Delta PE \)
  • Flow energy: \( Pv \)
  • Enthalpy: \( H = U + PV \)
  • Specific enthalpy: \( h = u + Pv \)
  • Mass flow rate: \( \dot{m} = \rho A V \)
  • SFEE: \( q – w = \Delta h + \Delta(V^2/2) + \Delta(gz) \)
  • Pressure energy per unit mass: \( Pv \)

Exam Traps

  • \( U \) = internal energy; \( H \) = enthalpy.
  • Enthalpy = Internal energy + Flow energy.
  • Flow energy per unit mass = \( Pv \).
  • For a complete cycle: \( \Delta U = 0 \).
  • Therefore cyclic process: Net heat = Net work.
  • NFEE → mainly closed system.
  • SFEE → mainly open/steady-flow system.
  • Steady state → properties at a fixed location do not change with time.
  • Steady flow ≠ zero flow; fluid can continuously flow while properties remain constant with time.
  • For an ideal gas, both \( u \) and \( h \) depend only on temperature.

One-Minute Revision

  • 1st Law → Conservation of Energy
  • Closed system → \( Q – W = \Delta U + \Delta KE + \Delta PE \)
  • Cycle → \( \Delta U = 0 \) → \( \oint Q = \oint W \)
  • Flow energy → \( Pv \)
  • Enthalpy → \( H = U + PV \)
  • Specific enthalpy → \( h = u + Pv \)
  • Steady state → No time variation at a fixed point
  • Steady flow → Continuous flow with time-independent properties at fixed locations
  • SFEE → \( q – w = \Delta h + \Delta KE + \Delta PE \)
  • Turbine → produces work
  • Compressor/Pump → consumes work
  • Nozzle → enthalpy decreases, velocity increases
Chapter – 4 : JSSC JE Mechanical Notes