000			02128nam a2200241 a 4500
001			vtls000056508
003			KUKTEM
005			20251114204507.0
008			111201t2010 my a f m 000 0 eng d
020			_aTHE0003952(Local)
039		9	_a201905141426 _bfauzi _c201112011624 _dFida _c201112011615 _dFida _y201112011452 _zFida
040			_aUMP
090			_aTP156.E65 A93 2010 rs Bc.
100	0		_aMohamad Azamudin Ishak
245	1	0	_aEffects of temperature on vapor liquid equilibrium of MTBE-methanol mixtures / _cMohamad Azamudin Ishak
260			_aKuantan, Pahang : _bUMP, _c2010
300			_axiii, 50 p. : _bill. ; _c30 cm. + _e1 computer disc
502			_aProject paper (Bachelor of Chemical Engineering --- Universiti Malaysia Pahang - 2010
504			_aBibliography : p. 49-50
520	3		_aIn separation process of binary mixture the vapor liquid equilibrium diagram is integral to design the separation apparatus. This research objective is to construct the vapor liquid equilibrium diagram for MTBE-Methanol binary mixture system at various temperatures and at constant pressure. Other objective is also to find the Azeotropic point which the MTBE-Methanol binary mixture formed at certain point that posed problems in separation processes. The separation process encountered problems during the Azeotropic point which vapor and liquid fraction is equal. The equipment used is Vapor Liquid Equilibrium Unit Equipment in the Unit Operation Laboratory. Initially the steps taken are to find the calibration curve for MTBEMethanol mixture. The experiment started with MTBE volume set at constant and gradually increase the Methanol volume. The mixture in the equipment will be heated at four different temperatures which will give enough data to construct the diagram. Record the RI index and the temperature. The experiment was conducted at four different temperatures. The result, MTBE fraction of x vapor fraction and y liquid fraction formed Azeotropic point at 0.6~0.7 x =y.
650		0	_aVapor-liquid equilibrium
999			_aVIRTUA40 _c2989 _d2995
999			_aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*9992