Q$1)$ Design an industrial Shell & Tube heat exchanger for a specific application in the oil and gas industry

following the TEMA $($Tubular Exchanger Manufacturers Association$)$ standards. The objective is to

transfer heat from a hot process stream to a cold process stream while considering the unique

requirements and challenges of the oil and gas industry. Your design should ensure efficient heat

transfer, reliability, and compliance with industry standards.

Fluid A:

Inlet temperature $($Tin$,$ A$)$: $A{1}_{}C$

Outlet temperature $($Tout$,$ A$)$: $A2C$

Specific heat capacity $($Cp$)$: $4\mathrm{.}2k\frac{J}{k}gC$

Flow rate $(M)$:$Mk\frac{g}{s}$

Density $()$: $1000k\frac{g}{m^3}$

Viscosity $()$:$0\mathrm{.}8cP$

Eluid B:

Inlet temperature $($Tin$,$ B$)$: $B1C$

Outlet temperature $($Tout$,$ B$)$: $B_{}C$

Specific heat capacity $(Cp)$:$3\mathrm{.}8k\frac{J}{k}gC$

Density $()$:$900k\frac{g}{m^2}$

Viscosity $()$:$1\mathrm{.}2cP$

Material: Stainless steel $($thermal conductivity $=15\frac{W}{m}C)$

Determine:

$($i$)$ Heat transfer rate and Corrected LMTD$.$

$($ii$)$ Tube bundle diameter $($Using TEMA standards and Codes$)$ and Tube cross sectional area.

$($iii$)$ Heat transfer coefficient.

$($iv$)$ Heat Transfer Area.

$($v$)$ Pressure Drop $($Shell side & Tube Side$).$

$($vi$)$ Select and justify the TEMA standard $($AEM$,$ BEM, or NEN$)$ to be used for the design.

Design Guidelines:

Assume counter$-$current flow for the heat exchanger.

Assume negligible fouling factors.

Consider a safety factor of $1\mathrm{.}2$ for the required heat transfer area $($A$)$ to ensure efficient

performance.

Use appropriate correlations and equations from heat transfer textbooks or other credible sources.

Present your design calculations, assumptions, and reasoning in a clear and organized manner.

Use the metric system for all calculations and measurements.