∮ Thermodynamics熱力學
Chapters章節  /  03 Laws03 定律

Entropy熵

Entropy turns the second law from a set of prohibitions into a working tool. It is an extensive property like mass and energy — but unlike them, it can be produced. Track it with an entropy balance and you can size irreversibility, rate real devices against the isentropic ideal, and read heat straight off a T–s diagram.

Isentropic-efficiency lab T–s diagrams
Overview總覽

What you'll be able to do本章學習成果

  • Understand entropy transfer, entropy production, and the increase-of-entropy principle.
  • Evaluate entropy and entropy change, and analyze isentropic processes with property data.
  • Represent heat transfer as an area on a T–s diagram.
  • Apply entropy balances to closed systems and control volumes, and evaluate isentropic efficiencies of turbines, nozzles, compressors, and pumps.

Key equations重要公式

Entropy change熵的變化
$\Delta S = \int (\delta Q/T)_{int\,rev}$
Closed-system balance封閉系統平衡
$\Delta S = \int(\delta Q/T)_b + \sigma$
Ideal-gas Δs理想氣體 Δs
$c_p\ln\tfrac{T_2}{T_1} - R\ln\tfrac{p_2}{p_1}$
Turbine efficiency渦輪機效率
$\eta_t = (h_1-h_2)/(h_1-h_{2s})$
Foundations基礎

Defining entropy change

Starting from the Clausius inequality, consider two internally reversible processes linking the same two states. The integral $\int \delta Q/T$ comes out identical for both — it depends only on the end states. A quantity whose change is path-independent is a property. We call it entropy, $S$:

$$ S_2 - S_1 = \int_1^2 \left(\frac{\delta Q}{T}\right)_{int\,rev} $$
Eq. 6.2a

You compute it by imagining any internally reversible path between the states — but because entropy is a property, the result holds for the actual process too, reversible or not. Entropy is extensive; specific entropy $s$ has units kJ/kg·K. For two-phase mixtures, $s = s_f + x\,s_{fg}$, just like $v$, $u$, and $h$.

Interpretation解釋

Entropy & heat transfer熵與熱傳

From counting Ω to measuring Q and T從計數 Ω 到量測 Q 與 T

In the Second Law chapter we met Boltzmann's $S = k_B\ln\Omega$. But nobody can count $\Omega$ for a real tank of steam, so how does it turn into something we can measure? Follow what heat does to the molecules.在第二定律章節中我們見過波茲曼的 $S = k_B\ln\Omega$。但沒有人能實際數出一槽蒸汽的 $\Omega$,那麼它如何變成可量測的量?看看熱對分子做了什麼。

  1. Heat adds energy to molecular motion. More energy gives the molecules more ways to share it among themselves — more speeds, more vibration and rotation. So $\Omega$ grows, and $S$ goes up. Work done by a piston does not have to do this; heat always does.熱增加分子運動的能量。能量越多,分子之間分配能量的方式就越多——更多種速度、振動與轉動。因此 $\Omega$ 增加,$S$ 上升。活塞作功不一定如此;熱則必然如此。
  2. The same heat matters more when the system is cold. A cold system has little energy and few arrangements, so a small amount of heat multiplies $\Omega$ by a large factor. A hot system already has an enormous $\Omega$; the same heat changes it proportionally much less. Like giving 1000 dollars to someone with nothing versus someone with a million, the effect scales as $1/T$.同樣的熱量,對冷的系統影響更大。冷的系統能量少、排列方式少,少量的熱就能使 $\Omega$ 成倍增加。熱的系統 $\Omega$ 已極為龐大,同樣的熱量造成的相對變化小得多。就像把 1000 元給一無所有的人與給百萬富翁,效果與 $1/T$ 成正比。
  3. This is what temperature means. Statistical mechanics defines temperature by exactly this sensitivity — how fast entropy rises as energy is added, with volume held fixed so no work is done:這正是溫度的意義。統計力學正是以此敏感度定義溫度——在體積固定(無作功)下,加入能量時熵上升的速率:
$$ \frac{1}{T} = \left(\frac{\partial S}{\partial U}\right)_V \quad\Longrightarrow\quad dS = \frac{dU}{T} = \frac{\delta Q_{int\,rev}}{T} $$
micro → macro微觀 → 巨觀

With no work, the energy added is the heat, $dU = \delta Q$. The result is Clausius's definition from the previous section, now derived from molecules. Both describe the same property: $\Omega$ explains what entropy is, and $\delta Q/T$ is how we measure it with a thermometer and a calorimeter.無作功時,加入的能量就是熱,$dU = \delta Q$。所得結果即為前一節克勞修斯的定義,如今由分子層次推導出來。兩者描述同一性質:$\Omega$ 說明熵是什麼,$\delta Q/T$ 則是用溫度計與量熱計量測它的方法。

On a differential basis $dS = (\delta Q/T)_{int\,rev}$. So heat into a system raises its entropy and heat out lowers it — entropy transfer accompanies heat transfer, in the same direction. An internally reversible, adiabatic process has no heat transfer and therefore constant entropy — an isentropic process.

Heat = area on a T–s diagram熱量 = T–s 圖上的面積

Rearranging, $\delta Q_{int\,rev} = T\,dS$, or per unit mass $\delta q_{int\,rev} = T\,ds$. The heat transferred in an internally reversible process is the area under the process curve on a temperature–entropy diagram — the T–s counterpart to "work is area under the p–v curve."

Accounting計算

The entropy balance熵的平衡

Entropy is accounted for like mass and energy — but with a production term. For a closed system:

$$ S_2 - S_1 = \int_1^2 \left(\frac{\delta Q}{T}\right)_b + \sigma $$
Eq. 6.24

The first term is entropy transfer with heat (evaluated at the boundary); $\sigma$ is entropy production from internal irreversibilities. Its sign is decisive:

  • $\sigma = 0$ — no internal irreversibilities
  • $\sigma > 0$ — irreversibilities present
  • $\sigma < 0$ — impossible

For an adiabatic process the transfer term vanishes, so $\sigma = S_2 - S_1$: a negative entropy change would be impossible. This is the increase-of-entropy principle in action — the test the explorer below applies.

Open systems開放系統

Control-volume entropy balance控制體積的熵平衡

Streams of matter carry entropy across a control surface. At steady state, for one inlet and one exit:

$$ 0 = \sum_j \frac{\dot Q_j}{T_j} + \dot m\,(s_1 - s_2) + \dot\sigma_{cv} $$
Eq. 6.37

A throttling valve is a clean example: adiabatic with $h_2 = h_1$, so $\dot\sigma_{cv}/\dot m = s_2 - s_1 > 0$ — the entropy production traces directly to the unrestrained expansion to lower pressure.

Evaluation計算

Calculating entropy change熵變化的計算

The property tables are built from the T ds equations, $T\,ds = du + p\,dv = dh - v\,dp$. Two models give closed forms. For an incompressible substance with constant $c$: $\Delta s = c\,\ln(T_2/T_1)$. For an ideal gas with constant specific heats:

$$ s_2 - s_1 = c_p \ln\frac{T_2}{T_1} - R\,\ln\frac{p_2}{p_1} $$
Eq. 6.22

Setting $s_2 = s_1$ recovers the familiar isentropic relation $T_2/T_1 = (p_2/p_1)^{(k-1)/k}$.

When specific heats vary appreciably, the temperature integral is tabulated instead. The ideal-gas table lists the entropy function $s^\circ(T) = \int_{T_\text{ref}}^{T} c_p(T)\,dT/T$ alongside $h$ and $u$, and the pressure term is added separately:當比熱變化明顯時,改以查表處理溫度積分。理想氣體表在 $h$、$u$ 之外另列熵函數 $s^\circ(T) = \int_{T_\text{ref}}^{T} c_p(T)\,dT/T$,壓力項則另外加上:

$$ s_2 - s_1 = s^\circ(T_2) - s^\circ(T_1) - R\,\ln\frac{p_2}{p_1} $$
variable specific heats變比熱
T Ks° kJ/kg·K
3001.70203
4001.99194
5002.21952
10002.96770
15003.44516

Air, ideal-gas table (Table A-22), excerpt. $h$ and $u$ for the same rows are in Equations of State. The relative-pressure $p_r$ column in the full table handles isentropic processes the same way.空氣理想氣體表(表 A-22)節選。同列的 $h$ 與 $u$ 見狀態方程式。完整表格中的相對壓力 $p_r$ 欄亦以同樣方式處理等熵過程。

Applications應用

Isentropic efficiency等熵效率

Because adiabatic devices can only reach exit states with $s_2 \ge s_1$, the isentropic (constant-entropy) endpoint is the best case. For a turbine, the most work is the isentropic work; the efficiency is the actual fraction of it:

$$ \eta_t = \frac{h_1 - h_2}{h_1 - h_{2s}} $$
Eq. 6.46

For a compressor or pump the ideal is the minimum work, so the ratio inverts: $\eta_c = (h_{2s}-h_1)/(h_2-h_1)$. In every case the actual process lands to the right of the isentropic one on a T–s or Mollier diagram — that horizontal shift is the entropy generated.

Interactive互動

Isentropic-efficiency lab等熵效率實驗室

Expand or compress air between two pressures at a chosen isentropic efficiency. The ideal path (1→2s) is vertical — constant entropy; the actual path (1→2) leans right by exactly the entropy generated. Watch the work and $\sigma$ respond as you lower the efficiency.

Air as ideal gas, constant $c_p = 1.005$ kJ/kg·K, $k = 1.4$. Adiabatic device, so actual Δs equals the entropy generated.

Worked example範例

Entropy change of an ideal gas理想氣體的熵變化

Example範例 Air heated and compressed空氣加熱並壓縮 ›

Given: air goes from 300 K, 100 kPa to 600 K, 300 kPa. Use $c_p=1.005$, $R=0.287$ kJ/kg·K.

Find: the specific entropy change.

Solution. $$\Delta s=c_p\ln\frac{T_2}{T_1}-R\ln\frac{p_2}{p_1}=1.005\ln 2-0.287\ln 3=0.696-0.315=0.381\ \tfrac{\text{kJ}}{\text{kg·K}}.$$ Heating raises $s$; the pressure rise pulls it back down.