Question 13.3: An existing heat exchanger has a cross section as shown in F......

An existing heat exchanger has a cross section as shown in Figure 13.3 with nine 1-in-OD tubes inside a 5-in-ID pipe. For a 5-ft length of heat exchanger, what flow rate of water at 60 F can be achieved in the shell side of this unit for a pressure drop of 3 psi?

Figure 13.3
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An energy-equation analysis using equation (6-10) will follow the same steps as in Example 2 in this chapter, yielding, as the governing equation,

{\frac{\delta Q}{d t}}-{\frac{\delta W_{\mathrm{s}}}{d t}}=\iint_{\mathrm{c.s.}}\left(e+{\frac{P}{\rho}}\right)\rho(\mathbf{v}\cdot\mathbf{n})\,d A+{\frac{\partial}{\partial t}}\iiint_{\mathrm{c.v.}}e\rho\,d V+{\frac{\delta W_{\mu}}{d t}}    (6-10)

0=\frac{P_{2}-P_{1}}{\rho}+g h_{L}

The equivalent diameter for the shell is evaluated as follows:

{\mathrm{Flow~area}}={\frac{\pi}{4}}(25-9)=4\pi\operatorname{in}_{\cdot}^{2}

{\mathrm{Wetted\ perimeter}}=\pi(5+9)=14\pi\,\mathrm{in}.

thus

D_{\mathrm{eq}}=4\frac{4\pi}{14\pi}=1.142\,\mathrm{in}.

Substituting the proper numerical values into the energy equation for this problem reduces it to

0=-\frac{3\,\mathrm{lb}_{f}/\mathrm{in}^{2}(\,144\,\mathrm{in.}^{2}/\mathrm{ft}^{2})}{1.94\,\mathrm{slugs/ft}^{3}}+2f_{f}v_{\mathrm{avg}}^{2}\,\mathrm{ft}^{2}/\mathrm{s}^{2}\frac{5\,\mathrm{ft}}{(1.142/12)\,\mathrm{ft}}\frac{g}{g}

or

0=-223+105f_{f}v_{\mathrm{avg}}^{2}

As f_{f} cannot be determined without a value of Re, which is a function of υ_{avg}, a simple trial-and-error procedure such as the following might be employed:

1. Assume a value for f_{f}.

2. Calculate υ_{avg} from the above expression.

3. Evaluate Re from this value of υ_{avg}.

4. Check the assumed value of f_{f} using equation (13-15a).

{\frac{1}{\sqrt{f_{f}}}}=-3.6\log_{10}\left[{\frac{6.9}{\mathrm{Re}}}+\left({\frac{e}{3.7D}}\right)^{10/9}\right]    (13-15a)

5. If the assumed and calculated values for f_{f} do not agree, repeat this procedure until they do.

Employing this method, we find the velocity to be 23.6 fps, giving a flow rate for this problem of 2.06\;\mathrm{ft}^{3}/\mathrm{min}(0.058\;{\mathrm{m}}^{3}/{\mathrm{s}}).

Notice that in each of the last two examples in which a trial-and-error approach was used, the assumption of f_{f} was made initially. This was not, of course, the only way to approach these problems; however, in both cases a value for f_{f} could be assumed within a much closer range than either D or υ_{avg}.

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