A new facility to produce Monoethanolamine $($MEA$)$ is being considered due to anincrease in demand. Therefore, you have been requested to design a plant to produce$10,000$ metric tons per annum of MEA $($at $99\mathrm{.}5\%$ purity$).$ The plant is to be located inRichards Bay, South Africa.The following feed streams are available: Ammonia feed is available at $10$ atm and $50\backslash$deg C from an adjacent plant.Ammonia is available as an aqueous solution of $55$ wt$.\%$ of ammonia and $45$wt$.\%$ water. Ethylene Oxide $(99\mathrm{.}99\%$ pure$)$ is available at $5$ atm and $40\backslash$deg C$.$ A reaction temperature of $150$ oC is maintained in the reactor, and a pressureof $160$ atmospheres to avoid the evaporation of ammonia. Under specified conditions of reaction, only MEA is produced when the feedratio of Ammonia $/$Ethylene oxide is $10.$ The plant should operate for $330$ days a year to allow for shutdown andmaintenance.You need to consider alternative design decisions$\mathrm{.}1.$ Decide whether the process is batch or continuous$\mathrm{.}2.$ Conduct material balances to determine the target feed requirements$\mathrm{.}3.$ Consider whether a recycling system is required$\mathrm{.}4.$ Consider different conversion rates to determine how this will affect the feedrequirements and process flowsheet$\mathrm{.}5.$ Determine the amount of heat to be added or removed from the system byconducting an energy balance$\mathrm{.}6.$ Determine the thermodynamic favourability of the reaction at standardconditions and reaction conditions$\mathrm{.}7.$ Determine process conditions for the separation units$\mathrm{.}8.$ Determine the effect of the inerts on the system$\mathrm{.}9.$ Determine the effect of pressure on compression work. Show In depth calculations And energy balances