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008 141224t2014 my a f m 000 0 eng d
020 _aTHE0003858(Local)
039 9 _a201905161534
_bshah
_c201905161534
_dshah
_c201711301149
_dhuda
_y201412241008
_zfawwaz
040 _aUMP
090 _aTP156.A35 S53 2014 r Bc.
100 0 _aAhmad Shafiq Hashim
245 1 0 _aAdsorption of methylene blue from aqueous solution using tea waste in a continuous stirred tank reactor (cstr) /
_cAhmad Shafiq Hashim
260 _aKuantan, Pahang :
_bUMP,
_c2014
300 _axv, 79 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. 61-65
520 3 _aIn these past few decades, huge numbers of technologies have been developed for wastewater treatment. The scale of these technologies is also very diverse, from a basic aeration pond, to a more sophisticated nanotechnology based treatment system. In this research, dye removal from aqueous solution by adsorption was studied in batch and continuous mode. The main objective of this study was to develop a continuous stirred tank reactor (CSTR) type adsorption unit for continuous dye removal from aqueous solution. The investigated parameters are the effect of adsorbent dose, and residence time on the performance of CSTR in treating synthetic Methylene Blue (MB) wastewater by using tea waste (TW). The equilibrium batch and kinetic study has been performed to characterize the adsorbent-adsorbate system. For the CSTR adsorption test, the adsorbent was added at suitable time intervals while the residence time and adsorbent dosage is varied. The Langmuir isotherm data obtained with varying MB concentrations fits the isotherm with an R2 of 0.99. The Langmuir parameters from the experiment were a Q (mg/g) of 68.02 and K (L/mg) of 0.385 while the RL value was 0.017, assuring a favourable adsorption. Next, the kinetics data were fitted with Unified Approach Model and the adsorption and desorption rate constants were determined to be 1.00E-8 ± 3.00E-9 and 2.60E-8 respectively. It was also found that the kinetic rate constants were initial concentration independent. Lastly, the CSTR adsorption study data was very comparable to the theoretical line predicted with the CSTR model, with very minute offsets from theoretical predictions. The maximum achievable utilization coefficient, ηmax was found to be 78% for TW-MB system, where higher utilization coefficient attributes to the higher adsorption capacity and better performance
650 0 _aAdsorption
856 4 0 _uhttp://ecollib.ump.edu.my/9659/
_zAccess in library only
999 _aVIRTUA40
_c5589
_d5595
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