Please do the T$-$xy MEA$-$WATER solution table and the McCabe$-$Thiele diagram for the MEA distillation column

The preliminary equipments ate :

o The Ammonia$-$Ethylene oxide reactor,

o Flash drum $($ammonia removal$),$

o Compressor $($ammonia recycler$),$

o MEA$-$water distillation column

o Feed pumps.

A new facility to produce Monoethanolamine $($MEA$)$ is being considered due to an

increase 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 in

Richards Bay, South Africa. 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 $40$ oC$.$ A

reaction temperature of $150$ oC is maintained in the reactor, and a pressure of $160$

atmospheres is used to avoid the evaporation of ammonia. Under specified conditions

of reaction, only MEA is produced when the feed ratio of Ammonia $/$Ethylene oxide is

$10.$ The plant should operate for $330$ days in a year, in order to allow for shutdown and

maintenance.