A steam boiler drum produces steam at a mass flow rate of \(64 \mathrm{~kg}
\cdot \mathrm{s}^{-1}\) at 60 bar. This stream still contains \(2 \mathrm{wt}
\%\) moisture. The feedwater from the economizer (a heat exchanger) is fed to
the drum at a mass flow rate of \(62 \mathrm{~kg} \cdot \mathrm{s}^{-1}\). It
contains \(3 \mathrm{ppm}_{\mathrm{w}}\) solids. Makeup water, containing \(50
\mathrm{ppm}_{\mathrm{w}}\) solids, is also fed into the drum at a mass flow
rate of \(2 \mathrm{~kg} \cdot \mathrm{s}^{-1}\). Steam production is such that
the solid content of the moisture leaving with the steam is \(5
\mathrm{ppm}_{\mathrm{w}}\). Blowdown, which is the release of hot liquid from
the bottom of the drum, must keep the concentration of solids in the drum to
\(1000 \mathrm{ppm}_{\mathrm{w}}\) -
a. Calculate the blowdown requirement in \(\mathrm{kg} \cdot \mathrm{s}^{-1}\).
b. Calculate the heat loss associated with blowdown in \(\mathrm{kW}\).