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008 130925t2013 my da f m 000 0 eng d
020 _aTHE0003813(Local)
039 9 _a201905151517
_bshah
_c201310011522
_dhuda
_c201309261255
_dtraining
_y201309251714
_ztraining
040 _aUMP
090 _aTP156.A35 A97 2013 rs Bc.
100 1 _aMuhammad Noor Azreen Mohd Khairu
245 1 0 _aStudy on continuous adsorption process for monoethanolamine (MEA) wastewater treatment using granular activated carbon and sugarcane bagasse /
_cMuhammad Noor Azreen Mohd Khairu
260 _aKuantan, Pahang :
_bUMP,
_c2013
300 _axiii, 69 p. :
_bill. (some col.) ;
_c30 cm. +
_e1 CD-ROM
502 _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2013
504 _aBibliography : p. 55-60
520 3 _aMonoethanolamine (MEA) is one of the most widely used alkanolamines for removing sour gases such as H2S and CO2 from natural gas for refining processes. MEA has gained attention for the abatement of greenhouse gases and the disposal of the MEA wastewater causing a problem as MEA cannot be treated easily due to its toxic effect and slow biodegradability. Foaming phenomena is formed in the absorber when heavy hydrocarbon component carried to the absorber with the feed gas that will leads to several problems such as increased amine losses, reduced gas adsorption efficiency and MEA feed back into the stripper as properties deterioration. This study was conducted to determine potential of continuous technique for treating MEA wastewater and to evaluate the potential of recycling on the treated MEA wastewater. Adsorption method was used for the treatment adsorbent of granular activated carbon with sugarcane bagasse as the comparison of these two adsorbents was investigated. Three parameters have being analysed which is the removal of oil content, amine concentration and COD level. The results showed that activated carbon was the best adsorbent for MEA wastewater treatment system. At the optimum condition, amine concentration is maintained and the residue oil reached its highest removal percentage of 91.72% and COD level reduction of 61.04% approximately via activated carbon adsorption treatment.
650 0 _aAdsorption
999 _aVIRTUA40
_c2604
_d2610
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*9992