$1.$Consider different conversion rates to determine how this will affect the feed

requirements and process flowsheet.

Daily production of MEA is $30\mathrm{.}30$ metric tons$/$ day $,$ however pure MEA is required at $30\mathrm{.}151$ metric tons$/$day$.$ The rest is considered as additional water

Ethylene oxide required is $21\mathrm{.}748$ metric tons$/$day

Aqueous ammonia feed is $152\mathrm{.}776$ metric tons$/$day

Pure ammonia from the aqueous solution is : $84\mathrm{.}03$ tons$/$day

Note: $*$Ammonia feed was available at $10$ atm and $50\backslash$deg C before going into the reactor and Ethylene Oxide was available at $5$ atm and $40\backslash$deg C$.$

$*$A reaction temperature of $150$ C is maintained in the reactor, and a pressure of $160$ atmospheres to avoid the evaporation of ammonia.