$1.$ Provide conceptual $($so not detailed to the stritting etc.$)$ design to produce about

$..20C..?..$glucose using microbial cells. Argument each step.

$2.$ As process engineer, your task is to design a bioreactor to produce iso$-$Butanol $($i$-$BaOH$)$

from corn$-$stover...?... year production. Capacity of $2800$ tons year using proprietary

Clastirilium spp pilot scale data is$..?...$ as YSP$=0\mathrm{.}6g$ i$-$Butanol $\frac{?}{gGlc},$ YSX$=0\mathrm{.}1$gDW$/$g Glc$.$

Corn$-$stover composition $35\%$Glucose, $20\%$ Xylase, $30\%$ Lignin. Pilot data also shows that

co$-$consumption of Xylose with Glucose is possible at the EXPENSIVE OF$...?.....$

fermentation time. Typically, $96$h$,$ with $150g$ Corn$-$stover equivalent. You don't need to

take PREVENTATION.?... corn$-$stover into account. Provide all necessary details.

$3.$ Clean water needs to be transported from the feed tank capacity with dimensions

$344(HWD)$ to the turbine. The steam turbine and the feed tank are at the either end

of the diagram for the.. plant sitting on $600m1200m$ land. The water needs to be

delivered at the top of the steam $...$TURBINE.$\mathrm{.}2$wordsmore?..high $)$ at atmospheric

pressure. Calculate the pumping power required as well as pipping $...$SPECIFICATION$(..$

drop, friction, number of elbows, pipe diameters$)$ required to pump water across the

plant.