Predictive modeling and optimization of industrial penex isomerization unit / Mohanad Magdy Menoufi Mohamed Said ; Supervised Tarek Mohamed Mostafa , Tamer Samir Mohamed
Material type:
- النمذجة التنبؤية و الإستفادة المثلى من وحدة صناعية للأزمرة بطريقة بنكس [Added title page title]
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قاعة الرسائل الجامعية - الدور الاول | المكتبة المركزبة الجديدة - جامعة القاهرة | Cai01.13.04.M.Sc.2015.Mo.P (Browse shelf(Opens below)) | Not for loan | 01010110066963000 | ||
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مخـــزن الرســائل الجـــامعية - البدروم | المكتبة المركزبة الجديدة - جامعة القاهرة | Cai01.13.04.M.Sc.2015.Mo.P (Browse shelf(Opens below)) | 66963.CD | Not for loan | 01020110066963000 |
Thesis (M.Sc.) - Cairo University - Faculty of Engineering - Department of Chemical Engineering
This work presents a model for UOP hydrogen once through (HOT) penex process using aspen HYSYS petroleum refining V7.3. The model relies on routinely taken samples of process streams and normal operating conditions of Penex unit located in Cairo oil refinery. Due to absence of detailed analysis of C7 + fraction in feed, a de - lumping procedure of this fraction has been conducted using available bulk properties. Acquired data sets have been tested and screened to ensure data validity for building the model and avoiding erroneous results. A reaction network with 20 reactions and 19 components has been used for the reactors model. The reactors model has been validated using 4 months of plant data. In addition, rigorous tray by tray simulation of isomerate stabilizer has been utilized to match the performance of plant stabilizer close enough. The model has then been used for studying the effects of each process variable on plant performance
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