(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
