Question #230595

In a steam engine the steam at the beginning of the expansion process is

at 7 bar, dryness fraction 0.98 and expansion follows the law pv1.1 = constant, down to a pressure

of 0.34 bar. Calculate per kg of steam :

(i) The work done during expansion ;

(ii) The heat flow to or from the cylinder walls during the expansion.


1
Expert's answer
2021-08-29T16:55:48-0400

Initial pressure of steam,

p1=7  bar=7×105  N/m2p_{1} =7 \;bar = 7 × 10^{5} \; N/m^{2}

Dryness fraction,

x1=0.98x_{1} = 0.98

Law of expansion,

pv1.1=constantpv^{1.1} = constant

Final pressure of steam,

p2=0.34  bar=0.34×105  N/m2p_{2} =0.34 \; bar = 0.34 \times 10^{5} \; N/m^{2}

At 7 bar :

vg=0.273  m3/kgv1=x1vg=0.98×0.273=0.267  m3/kgp1v1n=p2v2nv2v1=(p1p2)1nu20.267=(70.34)11.1v_{g} = 0.273 \; m^{3}/kg \\ v_{1}=x_{1}v_{g}= 0.98 \times 0.273 = 0.267 \; m^{3}/kg \\ p_{1}v_{1}^{n}=p_{2}v_{2}^{n} \\ \frac{v_{2}}{v_{1}}=\left ( \frac{p_{1}}{p_{2}} \right )^{\frac{1}{n}} \\ \frac{u_{2}}{0.267}=\left ( \frac{7}{0.34} \right )^{\frac{1}{1.1}}

or

v2=0.267(70.34)11.1=4.174  m3/kgv_{2}= 0.267\left ( \frac{7}{0.34} \right )^{\frac{1}{1.1}}= 4.174 \; m^{3}/kg

(i) Work done by the steam during the process :

W=p1v1p2v2n1=7×105×0.2670.34×105×4.174(1.11)=1050.1(1.8691.419)=105×4.5  Nm/kgW=\frac{p_{1}v_{1}-p_{2}v_{2}}{n-1} \\ =\frac{7\times 10^{5}\times 0.267-0.34\times 10^{5}\times 4.174}{\left ( 1.1-1 \right )} \\ =\frac{10^{5}}{0.1}(1.869 - 1.419) =10^{5}\times 4.5 \; Nm/kg

Work done =105×4.5103=450  kJ/kg.= \frac{10^{5}\times 4.5}{10^{3}} =450\; kJ/kg.

At 0.34 bar : vg=4.65  m3/kgv_{g}= 4.65\; m^{3}/kg , therefore, steam is wet at state 2 (since  v2<vg)(since \;v_{2} < v_{g}) .

Now, v2=x2vgv_{2}=x_{2}v_{g} , where x2=x_{2} = dryness fraction at pressure p2  (0.34  bar)p_{2} \; (0.34 \;bar)

4.174=x2×4.654.174 = x_{2}\times 4.65

or

x2=4.1744.65=0.897x_{2} = \frac{4.174}{4.65}= 0.897

The expansion is shown on a p-v diagram in Fig., the area under 1-2 represents the work done per kg of steam.



(ii) Heat transferred :

Internal energy of steam at initial state 1 per kg,

u1=(1x1)uf+x1ug=(10.98)696+0.98×2573=2535.46  kJ/kgu_{1}= (1 - x_{1})u_{f} + x_{1}u_{g} \\ = (1 - 0.98) 696 + 0.98 \times 2573 = 2535.46 \; kJ/kg

Internal energy of steam at final state 2 per kg,

u2=(1x2)uf+x2ug=(10.897)302+0.897×2472=2248.49  kJ/kgu_{2}=\left ( 1-x_{2} \right )u_{f}+x_{2}u_{g} \\ = (1 - 0.897) 302 + 0.897 \times 2472 = 2248.49 \; kJ/kg

Using the non-flow energy equation,

Q=(u2u1)+W=(2248.492535.46)+450=163.03  kJ/kgQ=\left ( u_{2} -u_{1}\right )+W \\ = (2248.49 - 2535.46) + 450 = 163.03 \; kJ/kg

Heat supplied = 163.03 kJ/kg.


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