(64a) An Ethylene Plant Start-up with Total Recycles: Dynamic Simulation of De-Ethanizer Transient Behaviors | AIChE

(64a) An Ethylene Plant Start-up with Total Recycles: Dynamic Simulation of De-Ethanizer Transient Behaviors

Authors 

Zhang, S., Dan F. Smith Department of Chemical Engineering, Lamar University



Flaring emissions during plant turnarounds have always been a major environmental and economical concern in the chemical process industry. A significant case is during plant start-ups. Traditionally, off-spec products are directed to flare system as wastes until operating units are in specifications. One of the recent flare minimization practices is the start-up with total recycles, in which off-spec streams from downstream are directed to system input until the process operates normally. Dynamic simulation is employed as a virtual tool to generate a new strategy and provide guiding procedure to operators.

In this study, an operation procedure of an ethylene plant start-up is investigated via dynamic simulations. Three case studies are presented to demonstrate the efficacy of dynamic simulations.  The base case is the conventional method of flaring off-spec products during the first three and a half hours to fire and stabilize three cracking furnaces before starting charged-gas compressor (CGC) system. Off-spec C2-hydrocarbons are withdrawn from DeC2 overhead and recycled back to feed CGC as an alternate to either one (Case One) or two furnaces (Case Two). This recycled stream is also mixed with another off-spec one from C3 splitter and additional natural gas to make up to achieve an equivalent molecular weight as CGC normal feed. Dynamic simulation contributes a great deal in evaluating new strategies as well as predicting process dynamic behaviors. It also helps achieving more precise timing to control the recycle loop; hence, flaring is potentially minimized while the start-up time is shortened. One observation is the difference of the recycle stream temperature and the expected value entering the first-stage compressor, a solution of which is confirmed by dynamic simulations. Following this representative, utilizing dynamic simulation as a driving force for operation during start-ups, shutdowns and malfunctions (SSM) conditions effectively provides an in-depth understanding and provides more detailed planning and expectations for all related personnel before the real action is proceeded.