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003			KUKTEM
005			20251117113235.0
008			150115t2014 my a f m 000 0 eng d
020			_aTHE0003763(Local)
039		9	_a201905131427 _bshah _c201712041011 _dhuda _y201501151510 _zfawwaz
040			_aUMP
090			_aTN884 .T36 2014 r Bc.
100	3		_aTan, Fong Ling
245	1	0	_aEvaluation of effectiveness parameters on gas dehydration plant (simulation) / _cTan Fong Ling
260			_aKuantan, Pahang : _bUMP, _c2014
300			_axv, 36 p. : _bill. ; _c30 cm. + _e1 CD-ROM
500			_aFaculty of Chemical & Natural Resources Engineering
502			_aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2014
504			_aBibliography : p. 33-34
520	3		_aThe transportation of natural gas through pipeline is an important aspect in the world. However the combination of hydrocarbon and water under suitable condition form hydrates in pipeline. These hydrates will cause blockage of pipeline. Gas dehydration is the method used to remove water from the hydrocarbon for the smooth transfer of natural gas in pipeline around the world. This research describes the effectiveness parameters on gas dehydration plant. The parameters studies are gas flow rate, absorber pressure and number of equilibrium stages of an absorber in liquid triethylene glycol (TEG) dehydration units. ASPEN HYSYS is used for steady state simulation, design, performance monitoring and optimization of oil and gas production, gas processing and petroleum refining industries. Peng-Robinson equation of state and MESH equation are chosen in the system. In conclusion, the results showed that increasing gas flow rate decreases the dehydration efficiency. While, dehydration efficiency decreases with increasing of operating pressure. Increasing of equilibrium stages increases the dehydration efficiency
650		0	_aNatural gas _xDrying
856	4	0	_uhttp://ecollib.ump.edu.my/18311/ _zAccess in library only
999			_aVIRTUA40 _c5260 _d5266
999			_aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5000*5020*5040*5200*6500*8560*9992