The First Law of Thermodynamics

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Vocabulary flashcards covering key definitions, principles, formulas, and process relations from the lecture notes on the First Law of Thermodynamics.

19 Terms

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First law of thermodynamics

The law of energy conservation stating that energy can neither be created nor destroyed and is conserved in a system; it relates the total energy stored in a system to energy transferred via heat and work.

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Constant-volume specific heat (CvC_v)

The energy required to raise the temperature of 1 kg1\,\text{kg} of a substance by 1 ∘C1\,^{\circ}\text{C} in an isochoric process, defined mathematically as Cv=(∂u∂T)vC_v = \left(\frac{\partial u}{\partial T}\right)_v.

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Specific heat transfer (qq)

The amount of heat transfer per unit mass of a substance, given by q=Qmq = \frac{Q}{m} with units of kJ/kg\text{kJ/kg}.

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Boundary work

The mechanical work associated with the expansion or compression of a gas performed at the boundary between a system and its surroundings.

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Specific boundary work (ww)

The boundary work done by or on a unit mass of a substance, expressed in units of kJ/kg\text{kJ/kg} or J/kg\text{J/kg}.

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Polytropic process

An expansion or compression process that includes heat transfer, described by the relation PVn=constantP\mathbb{V}^n = \text{constant} or Pvn=constantPv^n = \text{constant}, where nn is the dimensionless polytropic exponent.

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Isobaric process

A thermodynamic process occurring at constant pressure (P=constantP = \text{constant}), corresponding to a polytropic exponent of n=0n = 0.

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Isothermal process

A thermodynamic process occurring at constant temperature (T=constantT = \text{constant}), corresponding to a polytropic exponent of n=1n = 1 for an ideal gas.

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Isochoric process

A thermodynamic process occurring at constant volume (v=constantv = \text{constant}), corresponding to a polytropic exponent of n=∞n = \infty.

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Polytropic boundary work (n≠1n \neq 1)

The boundary work expression valid for both real and ideal gases undergoing a polytropic process where the exponent is not equal to one: 1W2=P2V2−P1V11−n{_1W_2} = \frac{P_2\mathbb{V}_2 - P_1\mathbb{V}_1}{1 - n}.

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Isothermal boundary work for ideal gases (n=1n = 1)

The boundary work expression valid specifically for ideal gases in a constant-temperature process: 1W2=mRTln⁡(V2V1)=mRTln⁡(P1P2){_1W_2} = mRT\ln\left(\frac{\mathbb{V}_2}{\mathbb{V}_1}\right) = mRT\ln\left(\frac{P_1}{P_2}\right).

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First law of thermodynamics for closed systems

The statement that the change in internal energy equals net heat added to the system minus net work done by the system: ΔU=U2−U1=1Q2−1W2\Delta U = U_2 - U_1 = {_1Q_2} - {_1W_2}.

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Control volume (Open system)

A thermodynamic system that always exchanges mass with its surroundings, and may exchange energy with its surroundings in the form of heat and work across its open boundary.

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Enthalpy (HH)

A property essential for energy analysis in open systems, related to mass and specific enthalpy by the equation H=mhH = mh, with units in kJ\text{kJ} or J\text{J}.

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Constant-pressure specific heat (CpC_p)

The energy required to raise the temperature of 1 kg1\,\text{kg} of a substance by 1 ∘C1\,^{\circ}\text{C} in an isobaric process, defined mathematically as Cp=(∂h∂T)pC_p = \left(\frac{\partial h}{\partial T}\right)_p.

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Specific heat approximation for solids and liquids

The thermodynamic relation for incompressible substances where Cp≈CvC_p \approx C_v, leading to the approximation Δh≈Δu≈Cp(T2−T1)\Delta h \approx \Delta u \approx C_p(T_2 - T_1).

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Mass flow rate (m˙\dot{m})

The amount of mass flowing through a cross-sectional area per unit of time, defined as m˙=dmdt=ρV˙=ρVavg,nA\dot{m} = \frac{dm}{dt} = \rho\dot{\mathbb{V}} = \rho V_{\text{avg}, n}A, in units of kg/s\text{kg/s}.

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Volume flow rate (V˙\dot{\mathbb{V}})

The volume of fluid passing through a cross-sectional area per unit of time, defined as V˙=dVdt=m˙v=Vavg,nA\dot{\mathbb{V}} = \frac{d\mathbb{V}}{dt} = \dot{m}v = V_{\text{avg}, n}A, in units of m3/s\text{m}^3\text{/s}.

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Steady-flow energy equation

The energy conservation expression for an open system operating under steady flow conditions: Q˙cv+∑m˙i(hi+12Vi2+gzi)=W˙cv+∑m˙e(he+12Ve2+gze)\dot{Q}_{cv} + \sum \dot{m}_i \left(h_i + \frac{1}{2}V_i^2 + gz_i\right) = \dot{W}_{cv} + \sum \dot{m}_e \left(h_e + \frac{1}{2}V_e^2 + gz_e\right).