Modeling and Simulation for industrial ethylene oxide reactors
Publish place: 5th International Congress on Chemical Engineering
Publish Year: 1386
نوع سند: مقاله کنفرانسی
زبان: English
View: 2,125
This Paper With 12 Page And PDF Format Ready To Download
- Certificate
- من نویسنده این مقاله هستم
استخراج به نرم افزارهای پژوهشی:
شناسه ملی سند علمی:
ICHEC05_445
تاریخ نمایه سازی: 7 بهمن 1386
Abstract:
Dynamic simulation of a fixed bed industrial ethylene oxide reactor has been studied in the presence of long term catalyst deactivation. The performance of the reactor was investigated using of heterogeneous dynamic model. The model was validated against measured daily process data of a ethylene oxide plant recorded for a period of four years. Good agreements was achieved and model was found to predict almost identical results under industrial operating conditions. The high velocity of the reactant stream was found to be the most important reason for this phenomena. The simple model represents useful tool for dynamic simulation, optimization and control of ethylene oxide production.
Keywords: