Holooly Plus Logo

Question 13.10: The compressor in a single-spool turbojet engine is composed......

The compressor in a single-spool turbojet engine is composed of a four-stage axial compressor and a single-stage centrifugal compressor. The rotational speed is 290 rev/s. The detailed data of both compressors are given as
Axial compressor (A):
Temperature rise per stage 25 K
Polytropic efficiency \eta_{\text{pc}} 0.9
Centrifugal compressor (B):
Impeller tip diameter 0.5 m
Power input factor ψ 1.04
Slip factor σ 0.9
Efficiency \eta_{\text{c}} 0.9
The inlet total conditions to the compressor section are

T_{01}=298 \text{ K}, \quad P_{01}=1.0 \text{ bar}

As shown in Figure 13.58a, two arrangements are investigated, namely, the axial compressor (A) is installed upstream of the centrifugal compressor (c) (arrangement 1) and the reverse (arrangement 2).
(a) Compare the overall stagnation pressure ratio and temperature rise in both cases.
(b) Plot these operating conditions on the maps of both compressors (m° = 20 kg/s).
(c) Calculate the overall efficiency for both arrangements.
(d) Same as in (a) and (c) but with a reduced value for the efficiency of the centrifugal compressor (\eta_{\text{c}} = 0.8).
(e) Compare between both layouts from aerodynamics, performance, and mechanical points of view.

13.56
13.57
التقاط1
Step-by-Step
The 'Blue Check Mark' means that this solution was answered by an expert.
Learn more on how do we answer questions.

(a) The temperature difference across these compressors is given by

(T_{0\text{e}}-T_{0\text{i}})_{\text{axial}}=N \Delta T_{0\text{s}} \\ (T_{0\text{e}}-T_{0\text{i}})_{\text{centrifugal}}=\frac{\Psi \sigma U^2_{\text{tip}}}{Cp}

Both are constants for the two arrangements.
Arrangement 1
The pressure and temperature at the inlets and outlets of compressor in arrangement (1) is shown in Figure 13.58b.

\Delta T_{0\text{axial}}=N \Delta T_{0\text{s}}=4 \times 25=100 \text{ K} \\ T_{01}=298 \text{ K}, \quad T_{02}=398 \text{ K} \\ \frac{n}{n-1} =\eta_{\text{PC}}\frac{\gamma}{\gamma-1} =0.9\frac{1.4}{0.4} =3.15 \\ \pi_{\text{axial}}=\left(1+\frac{\Delta T_0}{T_{01}} \right) ^{n/(n-1)} \\ \pi_{\text{axial}}=\left(1+\frac{100}{298}\right)^{n/(n-1)} =(1.3356)^{3.15}=2.488

For the centrifugal compressor

U_{\text{tip}}=\pi d_{\text{t}}N=\pi \times 0.5 \times 290=455.5 \text{ m/s} \\ (\Delta T_0)_{\text{centrifugal}}=\frac{\Psi \sigma U^2_{\text{tip}}}{Cp} \\ (\Delta T_0)_{\text{centrifugal}}=\frac{1.04 \times 0.9 \times (455.5)^2}{1005} =193 \text{ K} \\ T_{03}=T_{02}+(\Delta T_0)_{\text{centrifugal}}=591 \text{ K} \\ \pi_{\text{centrifugal}}=\left(1+\eta_{\text{c}}\frac{\Delta T_0}{T_{02}} \right) ^{\gamma/(\gamma-1)}=\left(1+0.9\frac{193}{398} \right) ^{3.5}=3.5522 \\ \pi_{\text{total}}=\pi_{\text{axial}} \times \pi_{\text{centrifugal}}=8.838

The overall temperature rise across the two compressors is constant in both arrangements and equal to 293 K.

Arrangement 2
(a) The pressure and temperature at the inlets and outlets of compressor in arrangement (2) is shown in Figure 13.58c.

\pi_{\text{centrifugal}}=\left(1+0.9\frac{193}{298} \right) ^{3.5}=(1.5828859)^{3.5}=4.98969 \\ \pi_{\text{axial}}=\left(1+\frac{100}{491} \right) ^{3.15}=1.793 \\ \pi_{\text{total}}=8.9465

(b) The results for both arrangements are summarized in Tables 13.11 and 13.12 for axial and centrifugal compressors, respectively. The compressor map for axial compressor is shown in Figure 13.58d, while Figure 13.58e illustrates the compressor map for centrifugal compressor.
(c) The overall efficiency (\eta_{\text{a}}=\eta_{\text{c}}=0.9)

\eta=\frac{T_{02^\prime}-T_{01}}{T_{02}-T_{01}} =\frac{T_{01}\left\{(p_{02}/p_{01})^{(\gamma-1)/\gamma}-1\right\} }{T_{02}  –  T_{01}} \\ \eta_{\text{arrangement(1)}}=\frac{298\left\{(8.839)^{0.4/1.4}-1\right\} }{293} =\frac{298(1.8638-1)}{293} =0.8785 \\ \eta_{\text{arrangement(2)}}=\frac{298\left\{(8.9465)^{0.4/1.4}-1\right\} }{293} =\frac{298(1.8702-1)}{293} =0.8851

(d) The efficiency of the axial compressor is unchanged while the efficiency of the centrifugal compressor drops, or \eta_{\text{a}}=0.9,\eta_{\text{c}}=0.8.
Arrangement 1

T_{01}=298 \text{ K}

The compression ratio for the axial compressor will not change.

\therefore \pi_{\text{axial}}=2.488, \quad T_{02}=398 \text{ K} \\ \pi_{\text{centrifugal }} =\left(1+0.8\frac{193}{398} \right) ^{3.5}=(1.3879396)^{3.5}=3.1496 \\ T_{03}=591 \text{ K} \\ \pi_{\text{total}}=7.836

Arrangement 2

T_{01}=298 \text{ K} \\ \pi_{\text{centrifugal}}=\left(1+0.8\frac{193}{298} \right) ^{3.5}=4.3099 \\ T_{02}=491 \text{ K} \\ \pi_{\text{axial}}=\left(1+\frac{100}{491} \right) ^{3.15}=1.793 \\ \pi_{\text{total}}=7.7276

The overall efficiency (Table 13.13)

\eta_{\text{arrangement(1)}}=\frac{298\left\{(7.836)^{0.4/1.4}-1\right\} }{293} =\frac{298(1.8007-1)}{293} =0.81436 \\ \eta_{\text{arrangement(2)}}=\frac{298\left[(7.7276)^{0.4/1.4}-1\right] }{293} =\frac{298(1.7936-1)}{293} =0.8071

(e) From the above calculations, which is summarized in Table 13.13, it can be deduced that
1. The overall pressure ratio is slightly higher for arrangement (2) if both compressors have the same efficiency, but if the efficiency of the centrifugal compressor is dropped then arrangement (1) gives a higher pressure ratio.
2. When the efficiency of centrifugal compressor is less than that of the axial one, then the overall efficiency of the compressor in arrangement (1) is larger than the overall efficiency in arrangement (2).
3. Arrangement (1) is appropriate for the installation of combustion chamber while arrangement (2) needs some piping system between both compressors, which adds some mechanical complications to the compressor section. This piping increases the skin friction and thus reduces the total pressure upstream of the axial compressor.
The external drag force in arrangement (2) is larger than that in arrangement (1) as shown in Figure 13.58f.

TABLE 13.11 Output Results for an Axial Compressor
Arrangement T_{\text{0inlet}} K T_{\text{0exit}} K P_{0_{\text{i}}} bar P_{0_{\text{e}}} bar π \dot{m}\sqrt{T_{0\text{i}}}/P_{0\text{i}} N/\sqrt{T_\text{0inlet}}
1 298 398 1.0 2.488 2.488 345.5 16.8
2 491 591 4.989 8.9465 1.793 88.83 13.09

 

TABLE 13.12 Output Results for a Centrifugal Compressor
Arrangement T_{\text{0inlet}} K T_{\text{0exit}} K P_{0_{\text{i}}} bar P_{0_{\text{e}}} bar π \dot{m}\sqrt{T_{0\text{i}}}/P_{0\text{i}} N/\sqrt{T_\text{0inlet}}
1 398 591 2.488 8.838 3.5522 160.4 14.91
2 298 491 1.0 4.9897 4.9897 345.2 13.09

 

TABLE 13.13 Summary for Both Arrangements
(1) (2)
Arrangement \eta_{\text{a}}=\eta_{\text{c}}=0.9 \eta_{\text{a}}=0.9,\eta_{\text{c}}=0.8 \eta_{\text{a}}=\eta_{\text{c}}=0.9 \eta_{\text{a}}=0.9,\eta_{\text{c}}=0.8
Overall pressure ratio 8.838 7.836 8.9465 7.7276
Overall efficiency 0.8785 0.81436 0.8851 0.8071

 

13.581
13.582
13.583
13.58

Related Answered Questions

Question: 13.4

Verified Answer:

The vortex energy equation is expressed by ...