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003 KUKTEM
005 20251117113302.0
008 150910t2015 my da f m 000 0 eng d
020 _aTHE0004201(Local)
039 9 _a201905152023
_bfarhana
_c201711281435
_dsaini
_y201509101619
_zhuda
040 _aUMP
090 _aTP157 .F58 2015 r Bc.
100 0 _aSiti Fitriana Alang Ahmat
245 1 0 _aModelling simultaneous nitritation and p-nitrophenol removal using aerobic granular biomass in a continuous airlift reactor /
_cSiti Fitriana Alang Ahmat
260 _aKuantan, Pahang :
_bUMP,
_c2015
300 _axv, 40 p. :
_bill. (some col.) ;
_c30 cm. +
_e1 CD-ROM
500 _aFaculty of Chemical & Natural Resources Engineering
502 _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2015
504 _aBibliography : p. 31-33
520 3 _aA mathematical biofilm model was developed with a dual-biomass kinetic including Haldane formalism to describe simultaneous nitritation and p-nitrophenol (PNP) removal in aerobic granular biomass operating in continuous airlift reactor. The model was validated with a set of experimental result previously reported in the literature. Then, the model was explored further to study the influence of pH, initial concentration of PNP in the influent, temperature of the operating system, and the influent loading rate for total ammonia nitrogen (TAN) and p-nitrophenol. The result showed that the maximum capacity of the reactor to treat simultaneous nitritation and PNP were 46.15 gN L-1d-1 and 288.5 mg PNP L-1d-1, respectively. Studying the effect of pH value in simultaneous nitritation and PNP removal, it showed that the range for optimum operation is between 7.3 and 8.3. While, the maximum advisable operating temperature is at 55°C. Higher operating temperature would result to a poor removal performance. In conclusion, simultaneous nitritation and PNP removal could be achieved in a single rector by using granular biomass.
650 0 _aChemical reactors
856 4 0 _uhttp://ecollib.ump.edu.my/id/eprint/9473
_zAccess in library only
999 _aVIRTUA40
_c6095
_d6101
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5000*5020*5040*5200*6500*8560*9992