The National Sanitation Foundation (NSF) standard for commercial warewashing
equipment (ANSL/NSF 3) requires that the final rinse water temperature be
between 82 and \(90^{\circ} \mathrm{C}\). A shell-and-tube heat exchanger is to
heat \(0.5 \mathrm{~kg} / \mathrm{s}\) of water $\left(c_{p}=4200 \mathrm{~J} /
\mathrm{kg} \cdot \mathrm{K}\right)\( from 48 to \)86^{\circ} \mathrm{C}$ by
geothermal brine flowing through a single shell pass. The heated water is then
fed into commercial warewashing equipment. The geothermal brine enters and
exits the heat exchanger at 98 and \(90^{\circ} \mathrm{C}\), respectively. The
water flows through four thin-walled tubes, each with a diameter of $25
\mathrm{~mm}$, with all four tubes making the same number of passes through
the shell. The tube length per pass for each tube is \(5 \mathrm{~m}\). The
corresponding convection heat transfer coefficients on the outer and inner
tube surfaces are 1050 and $2700 \mathrm{~W} / \mathrm{m}^{2} \cdot
\mathrm{K}$, respectively. The estimated fouling factor caused by the
accumulation of deposit from the geothermal brine is $0.0002 \mathrm{~m}^{2} .
\mathrm{K} / \mathrm{W}$. Determine the number of passes required for the
tubes inside the shell to heat the water to \(86^{\circ} \mathrm{C}\), within
the temperature range required by the ANIS/NSF 3 standard.