dc.description.abstract |
Most petrochemical processes require ethylene oxide as an initiator. It serves as a
necessary ingredient in manufacturing several petroleum products like Ethylene glycol
(primary element in antifreeze's), Poly oxirane, Monoethyl ether ethylene glycol, Amino
derivatives, Surface active agents, Lubricants and Plasticizers. Our objective is Modeling
and Simulation of the Ethylene oxide production process in Aspen plus software and
energy optimization of the whole process using the Pinch technology. Ethylene oxide is
commercially generated mainly in two ways. One is the ethylene oxidized with air and
the second one is with oxygen. The difference between atmospheric and O2 industries
with equal volume is also similar to catalysts because the O2 base method produces
higher selectivity and requires less extraction. Air-based processes have high initial
construction costs, but many small and medium-sized plants have a low operating cost.
Oxygen-based processes require the stairs of releasing carbon dioxide, further stainless
steel also other more costly metals. The study focused on ethylene oxide production by
the air-based system and modeled and simulated the whole process in Aspen plus®
using
the SRK and PSRK thermodynamic models. By virtual experiments, we predict the
behavior of the actual process. After process simulation, it has finally been concluded
that control the oxygen concentration by controlling the airflow and controlling the
reactor's temperatures. When the oxygen concentration increases, ethylene is oxidized
completely and generates useless products such as carbon dioxide and water to enhance
production. Ethylene must partially be oxidized that is generating our desired product,
ethylene oxide. Energy optimization of ethylene oxide production process is completed
through Pinch analysis and recover most of the valuable energy that's cause the use of
external utilities low and save 18.27million $ per year which we consume in heating or
cooling of streams. |
en_US |