MARC View

000			02117nam a2200265 a 4500
001			vtls000058601
003			KUKTEM
005			20251114204512.0
008			120307t2010 my a f m 001 0 eng d
020			_aTHE0003766(Local)
039		9	_a201905131431 _bshah _y201203071311 _zida
040			_aUMP
090			_aTP155.7 .A35 2010 rs Bc.
100	0		_aNoor Adila Zulkepa
245	1	0	_aEnergy conservation for production of 100,000 MT/A isobutylene plant and effect to the plant economic / _cNoor Adila Zulkepa
260			_aKuantan, Pahang : _bUMP, _c2010
300			_axvi, 52 p. : _bill. (some col.) ; _c30 cm. + _e1 CD-ROM
502			_aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2010
504			_aBibliography : p. 51-52
520	3		_aThis research shows how the application of Pinch technology can lead towards great energy saving. A few step need to undergo before start a heat exchanger network design which, analysis of process flow diagram data, pinch analysis and economic analysis. The heat exchanger network of the isobutylene process plant has been studied and it was shows how the application of pinch technology makes it possible to reduce the demand of hot and cold utility. After design the heat exchanger network, the overall heat exchanger required in these process is seven heat exchanger and all of them need to be redesign. The energy saving for total cooling is 65% and for total heating 38% which mean the good investment. Heat recovery is slightly reduced as the different minimum temperature increase. Even though the value of capital investment is higher than original process, but by implement pinch analysis in this plant, energy saving for utilities can recover the capital investment. Pay back period for the project is 0.8 year ( 9 month 3 days) that means, this project can be classify as quick win project
650		0	_aSustainable engineering
650		0	_aChemical processes
650		0	_aChemical industry _xEnergy conservation
999			_aVIRTUA40 _c3140 _d3146
999			_aVTLSSORT008002000400090010002450260030005020504052006500650165029992