Question 9.3: The Ideal Otto Cycle An ideal Otto cycle has a compression r...

The Ideal Otto Cycle

An ideal Otto cycle has a compression ratio of 8. At the beginning of the compression process, air is at 100 kPa and 17°C, and 800 kJ/kg of heat is transferred to air during the constant-volume heat-addition process. Accounting for the variation of specific heats of air with temperature, determine (a) the maximum temperature and pressure that occur during the cycle, (b) the net work output, (c) the thermal efficiency, and (d) the mean effective pressure for the cycle. (e) Also, determine the power output from the cycle, in kW, for an engine speed of 4000 rpm (rev/min). Assume that this cycle is operated on an engine that has four cylinders with a total displacement volume of 1.6 L.

Question Data is a breakdown of the data given in the question above.
  • Compression ratio: 8
  • Initial conditions:
    • Pressure: 100 kPa
    • Temperature: 17°C
  • Heat transferred during constant-volume heat-addition process: 800 kJ/kg
  • Specific heat variation of air with temperature
  • Required calculations:
    • Maximum temperature and pressure during the cycle
    • Net work output
    • Thermal efficiency
    • Mean effective pressure for the cycle
    • Power output from the cycle at an engine speed of 4000 rpm
    • Engine specifications:
      • Four cylinders
      • Total displacement volume: 1.6 L
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Step 1:
Assumptions We make several assumptions for this analysis: The air-standard assumptions are applicable. Kinetic and potential energy changes are negligible. The variation of specific heats with temperature is accounted for.
Step 2:
Analysis We start by examining the P-v diagram of the ideal Otto cycle. It is important to note that the air contained in the cylinder forms a closed system.
Step 3:
(a) Maximum temperature and pressure: The maximum temperature and pressure occur at the end of the constant-volume heat-addition process (state 3). However, we first need to determine the temperature and pressure at the end of the isentropic compression process (state 2). Using data from Table A-17, we find the values for state 1 as T1 = 290 K, u1 = 206.91 kJ/kg, and vr1 = 676.1.
Step 4:
Next, we calculate the values for state 2 using the isentropic compression process. We use the equation vr2 = vr1/r, where r is the compression ratio. For this problem, r = 8. Substituting the values, we find vr2 = 84.51 and T2 = 652.4 K. Similarly, we find u2 = 475.11 kJ/kg.
Step 5:
Using the equation P2v2/T2 = P1v1/T1, we can determine the pressure at state 2. Substituting the values, we find P2 = 1799.7 kPa.
Step 6:
Next, we analyze the constant-volume heat addition process (2-3). We know that qin = u3 - u2 = 800 kJ/kg. Using this information, we find u3 = 1275.11 kJ/kg and T3 = 1575.1 K. Additionally, vr3 = 6.108.
Step 7:
Using the equation P3v3/T3 = P2v2/T2, we can determine the pressure at state 3. Substituting the values, we find P3 = 4.345 MPa.
Step 8:
(b) Net work output: To calculate the net work output, we can either find the boundary (PdV) work involved in each process and add them or find the net heat transfer equivalent to the net work done during the cycle. We choose the latter approach.
Step 9:
Next, we analyze the isentropic expansion process (3-4). Using the equation vr4 = rvr3, where r is the compression ratio, we find vr4 = 48.864. Similarly, we find T4 = 795.6 K and u4 = 588.74 kJ/kg.
Step 10:
Analyzing the constant-volume heat rejection process (4-1), we find qout = u4 - u1 = 381.83 kJ/kg.
Step 11:
The net work output is given by the equation wnet = qin - qout = 800 - 381.83 = 418.17 kJ/kg.
Step 12:
(c) Thermal efficiency: The thermal efficiency of the cycle is determined by the equation eth = wnet / qin. Substituting the values, we find eth = 0.523 or 52.3%.
Step 13:
Under the cold-air-standard assumptions, the thermal efficiency would be given by the equation eth,Otto = 1 - 1/r^(k-1). Substituting the values, we find eth,Otto = 0.565 or 56.5%. This value is considerably different from the one obtained above, indicating the importance of being cautious while using cold-air-standard assumptions.
Step 14:
(d) Mean effective pressure: The mean effective pressure (MEP) is determined by the equation MEP = wnet / (vmax - vmin). Using the equation MEP = wnet / (v1 - v2), we find MEP = 574 kPa.
Step 15:
(e) Power output: To calculate the power output, we need to determine the total air mass taken by all four cylinders when they are charged. Using the equation m = Vd / v1, we find m = 0.001922 kg.
Step 16:
The net work produced by the cycle is given by Wnet = mw_net = (0.001922 kg)(418.17 kJ/kg) = 0.8037 kJ.
Step 17:
Since there are two revolutions per thermodynamic cycle in a four-stroke engine (or in the ideal Otto cycle including intake and exhaust strokes), the power produced by the engine is determined by the equation Wdot_net = (Wnet * n) / n_rev. Substituting the values, we find Wdot_net = 26.8 kW.
Discussion: If we were analyzing a two-stroke engine operating on an ideal Otto cycle with the same values, the power output would be calculated differently. Since there is one revolution in one thermodynamic cycle in two-stroke engines, the power output would be Wdot_net = (Wnet * n) / n_rev = (0.8037 kJ/cycle)(4000 rev/min) / (1 rev/cycle)(60 s/min) = 53.6 kW. This demonstrates the difference in power output between four-stroke and two-stroke engines.

Final Answer

An ideal Otto cycle is considered. The maximum temperature and pressure, the net work output, the thermal efficiency, the mean effective pressure, and the power output for a given engine speed are to be determined.

Assumptions     1 The air-standard assumptions are applicable. 2 Kinetic and potential energy changes are negligible. 3 The variation of specific heats with temperature is to be accounted for.

Analysis     The P-v diagram of the ideal Otto cycle described is shown in Fig. 9-20. We note that the air contained in the cylinder forms a closed system.

(a) The maximum temperature and pressure in an Otto cycle occur at the end of the constant-volume heat-addition process (state 3). But first we need to determine the temperature and pressure of air at the end of the isentropic compression process (state 2), using data from Table A-17:

\begin{aligned}T_{1}=290  \mathrm{~K} \rightarrow u_{1} &=206.91  \mathrm{~kJ} / \mathrm{kg} \\v_{r 1} &=676.1\end{aligned}

Process 1-2 (isentropic compression of an ideal gas):

\begin{aligned}\frac{v_{r 2}}{v_{r 1}}=\frac{v_{2}}{v_{1}}=\frac{1}{r} \rightarrow v_{r 2}=\frac{v_{r 1}}{r}=\frac{676.1}{8}=84.51  \rightarrow \quad T_{2}&=652.4  \mathrm{~K} \\u_{2}&=475.11  \mathrm{~kJ} / \mathrm{kg}\end{aligned}

\begin{aligned}\frac{P_{2} \mathrm{v}_{2}}{T_{2}}=\frac{P_{1} \mathrm{v}_{1}}{T_{1}} \rightarrow P_{2} &=P_{1}\left(\frac{T_{2}}{T_{1}}\right)\left(\frac{\mathrm{v}_{1}}{\mathrm{v}_{2}}\right) \\&=(100  \mathrm{kPa})\left(\frac{652.4  \mathrm{~K}}{290  \mathrm{~K}}\right)(8)=1799.7  \mathrm{kPa}\end{aligned}

Process 2-3 (constant-volume heat addition):

\begin{aligned}q_{\mathrm{in}}&= u_{3}-u_{2} \\800  \mathrm{~kJ} / \mathrm{kg} &=u_{3}-475.11  \mathrm{~kJ} / \mathrm{kg} \end{aligned}

\begin{aligned}\quad\quad\quad\quad\quad\quad\quad\quad\quad\quad\quad\quad u_{3}=1275.11  \mathrm{~kJ} / \mathrm{kg}\quad \rightarrow \quad T_{3}&=1575.1  \mathrm{~K} \\ v_{r 3}&=6.108 \end{aligned}

\begin{aligned}\frac{P_{3} v_{3}}{T_{3}}=\frac{P_{2} v_{2}}{T_{2}} \rightarrow P_{3}=& P_{2}\left(\frac{T_{3}}{T_{2}}\right)\left(\frac{v_{2}}{v_{3}}\right) \\=&(1.7997  \mathrm{MPa})\left(\frac{1575.1  \mathrm{~K}}{652.4  \mathrm{~K}}\right)(1)=4.345  \mathrm{MPa}\end{aligned}

(b) The net work output for the cycle is determined either by finding the boundary (P d V) work involved in each process by integration and adding them or by finding the net heat transfer that is equivalent to the net work done during the cycle. We take the latter approach. However, first we need to find the internal energy of the air at state 4:

Process 3-4 (isentropic expansion of an ideal gas):

\begin{aligned}\frac{v_{r 4}}{v_{r 3}}=\frac{v_{4}}{v_{3}}=r \rightarrow v_{r 4}=r v_{r 3}=(8)(6.108)=48.864 \rightarrow \quad T_{4} &=795.6  \mathrm{~K} \\u_{4} &=588.74  \mathrm{~kJ} / \mathrm{kg}\end{aligned}

Process 4-1 (constant-volume heat rejection):

\begin{aligned}-q_{\mathrm{out}} &=u_{1}-u_{4} \rightarrow q_{\mathrm{out}}=u_{4}-u_{1} \\q_{\mathrm{out}} &=588.74-206.91=381.83  \mathrm{~kJ} / \mathrm{kg}\end{aligned}

Thus,

w_{\text {net }}=q_{\text {net }}=q_{\text {in }}-q_{\text {out }}=800-381.83=418.17  \mathrm{k} J / \mathrm{kg}

(c) The thermal efficiency of the cycle is determined from its definition:

\eta_{\text {th }}=\frac{w_{\text {net }}}{q_{\text {in }}}=\frac{418.17  \mathrm{~kJ} / \mathrm{kg}}{800  \mathrm{~kJ} / \mathrm{kg}}=0.523 \text { or } 52.3 \%

Under the cold-air-standard assumptions (constant specific heat values at room temperature), the thermal efficiency would be (Eq. 9-8)

\eta_{\text {th,Otto }}=1-\frac{1}{r^{k-1}}        (9-8)

\eta_{\text {th, } O \text { tto }}=1-\frac{1}{r^{k-1}}=1-r^{1-k}=1-(8)^{1-1.4}=0.565 \text { or } 56.5 \%

which is considerably different from the value obtained above. Therefore, care should be exercised in utilizing the cold-air-standard assumptions.

(d) The mean effective pressure is determined from its definition, Eq. 9-4:

\mathrm{MEP}=\frac{W_{\mathrm{net}}}{V_{\max }-V_{\min }}=\frac{w_{\mathrm{net}}}{v_{\max }-v_{\min }}     ( kPa )                (9-4)

\mathrm{MEP}=\frac{w_{\text {net }}}{v_{1}-v_{2}}=\frac{w_{\text {net }}}{v_{1}-v_{1} / r}=\frac{w_{\text {net }}}{v_{1}(1-1 / r)}

where

v_{1}=\frac{R T_{1}}{P_{1}}=\frac{\left(0.287  \mathrm{kPa} \cdot \mathrm{m}^{3} / \mathrm{kg} \cdot \mathrm{K}\right)(290  \mathrm{~K})}{100  \mathrm{kPa}}=0.8323  \mathrm{~m}^{3} / \mathrm{kg}

Thus,

\mathrm{MEP}=\frac{418.17  \mathrm{~kJ} / \mathrm{kg}}{\left(0.8323  \mathrm{~m}^{3} / \mathrm{kg}\right)\left(1-\frac{1}{8}\right)}\left(\frac{1  \mathrm{kPa} \cdot \mathrm{m}^{3}}{1  \mathrm{~kJ}}\right)=574  \mathrm{kPa}

(e) The total air mass taken by all four cylinders when they are charged is

m=\frac{V_{d}}{v_{1}}=\frac{0.0016  \mathrm{~m}^{3}}{0.8323  \mathrm{~m}^{3} / \mathrm{kg}}=0.001922  \mathrm{~kg}

The net work produced by the cycle is

W_{\text {net }}=m w_{\text {net }}=(0.001922  \mathrm{~kg})(418.17  \mathrm{~kJ} / \mathrm{kg})=0.8037  \mathrm{~kJ}

That is, the net work produced per thermodynamic cycle is 0.8037  \mathrm{~kJ} / \mathrm{cycle}. Noting that there are two revolutions per thermodynamic cycle \left(n_{\mathrm{rev}}=2\right. rev/cycle) in a fourstroke engine (or in the ideal Otto cycle including intake and exhaust strokes), the power produced by the engine is determined from

\dot{W}_{\text {net }}=\frac{W_{\text {net }} \dot{n}}{n_{\text {rev }}}=\frac{(0.8037  \mathrm{~kJ} / \text { cycle })(4000  \mathrm{rev} / \mathrm{min})}{2 \text { rev/cycle }}\left(\frac{1  \mathrm{~min}}{60  \mathrm{~s}}\right)=26.8  \mathrm{~kW}

Discussion     If we analyzed a two-stroke engine operating on an ideal Otto cycle with the same values, the power output would be calculated as

\dot{W}_{\text {net }}=\frac{W_{\text {net }} \dot{n}}{n_{\text {rev }}}=\frac{(0.8037  \mathrm{~kJ} / \text { cycle })(4000  \mathrm{rev} / \mathrm{min})}{1  \text { rev/cycle }}\left(\frac{1 \mathrm{~min}}{60  \mathrm{~s}}\right)=53.6  \mathrm{~kW}

Note that there is one revolution in one thermodynamic cycle in two-stroke engines.

9.20

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