000			02053nam a2200253 a 4500
001			vtls000031311
003			KUKTEM
005			20251114204352.0
008			080828t2008 my a f m 000 0 eng|d
020			_aTHE0003924(Local)
039		9	_a201905140956 _bfauzi _c201107132042 _dVLOAD _c200908141514 _dVLOAD _c200908141444 _dVLOAD _y200808281654 _zida84
040			_aUMP
090			_aTP156.D5 N87 2008 rs Thesis
100	0		_aNurul Shamsinar Shahirin
245	1	0	_aPurification of clove oil via middle vessel batch distillation / _cNurul Shamsinar Shahirin
246	3		_aPurification of clove oil via middle vessel batch distillation _h[electronic resource]
260			_aKuantan, Pahang : _bUMP, _c2008
300			_a44 p. : _bill. (some col.) ; _c30 cm. + _e1 computer disc
502			_aProject paper (Bachelor of Chemical Engineering) --- Universiti Malaysia Pahang - 2008
520	3		_aBatch distillation process is becoming increasingly important because of its flexibility. However, regular batch distillation required high energy consumption and high residence time in the column. Middle Vessel Batch Distillation is one of the alternative configurations to overcome these problems. In this study, Middle Vessel Batch Distillation is used to purify crude clove oil. The scopes of this study are based on the effects of vessel holdup and operating time of distillation process. The objectives are to obtain the separation performance of clove oil by using middle vessel batch distillation column and to find out the effects of time and the middle vessel holdups to the composition of Eugenol in clove oil. The samples of clove oil after the process are analyzed by Gas Chromatography. The performance separation of the Middle Vessel Batch Distillation column is fully understood. It is proven that by varying vessel holdup and operating time, the separation performances are improved. -Author
650		0	_aDistillation
650		0	_aPurification
999			_aVIRTUA40 _c824 _d830
999			_aVTLSSORT0080*0200*0400*0900*1000*2450*2460*2600*3000*5020*5200*6500*6501*9992