000 | 01981cam a2200313 a 4500 | ||
---|---|---|---|
003 | EG-GiCUC | ||
008 | 150803s2015 ua e f m 000 0 eng d | ||
040 |
_aEG-GiCUC _beng _cEG-GiCUC |
||
041 | 0 | _aeng | |
049 | _aDeposite | ||
097 | _aM.Sc | ||
099 | _aCai01.13.04.M.Sc.2015.Ta.E | ||
100 | 0 | _aTarek Mohamed Zein Eldeen | |
245 | 1 | 0 |
_aEnergy analysis and design improvements of an existing crude vacuum distillation unit / _cTarek Mohamed Zein Eldeen ; Supervised Fatma Ashour , Mamdouh Gadalla |
246 | 1 | 5 | _aدراسة لتحليل عناصر الطاقة و تحسين التصميم لأبراج التقطير التفريغى |
260 |
_aCairo : _bTarek Mohamed Zein Eldeen , _c2015 |
||
300 |
_a142 P. : _bplans ; _c30cm |
||
502 | _aThesis (M.Sc.) - Cairo University - Faculty of Engineering - Department of Chemical Engineering | ||
520 | _aRefineries are among the most energy consuming industries in the petroleum sector; therefore lots of research efforts are spent to decrease the consumption of the energy in such industries, especially for crude and vacuum distillation columns. Adjusting and optimising the process operation will have a great effect on the energy consumed in the refinery. In addition, energy integration in the pre-heat trains is a key driver in increasing the duty of the pre - heat train of the distillation that leads to less fuel consumption in the fired-heater (furnace). Also decreasing the energy consumption of the refinery process is equivalent to cutting down the total emissions from the refinery unit. Previous methods that cope with the above objectives include column modifications and pre - heat train modifications | ||
530 | _aIssued also as CD | ||
653 | 4 | _aDistillation | |
653 | 4 | _aPinch | |
653 | 4 | _aVacuum | |
700 | 0 |
_aFatma Elzahraa Ashour , _eSupervisor |
|
700 | 0 |
_aMamdouh Ayad Gadalla , _eSupervisor |
|
905 |
_aNazla _eRevisor |
||
905 |
_aSamia _eCataloger |
||
942 |
_2ddc _cTH |
||
999 |
_c51834 _d51834 |