A shell-and-tube (two shell passes) 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)$ by geothermal brine flowing through the
shell passes. The heated water is then fed into commercial warewashing
equipment. The National Sanitation Foundation (NSF) standard for commercial
warewashing equipment (ANSI/NSF 3) requires that the final rinse water
temperature be between 82 and \(90^{\circ} \mathrm{C}\). The geothermal brine
enters and exits the heat exchanger at 98 and \(90^{\circ} \mathrm{C}\),
respectively. The water flows through a thin-walled tube inside the shell
passes. The tube diameter is \(25 \mathrm{~mm}\), and the tube length per pass
is 4 \(\mathrm{m}\). The corresponding convection heat transfer coefficients on
the outer and inner tube surfaces are 450 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 \(0.0002\)
\(\mathrm{m}^{2} \cdot \mathrm{K} / \mathrm{W}\). If the water enters the heat
exchanger at \(20^{\circ} \mathrm{C}\), determine the number of tube passes
required inside each shell pass to heat the water to \(86^{\circ} \mathrm{C}\)
so that it complies with the ANSI/ NSF 3 standard.