000 01994nam a2200241 a 4500
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008 131031t2012 my da f m 000 0 eng d
020 _aTHE0002281(Local)
039 9 _a201905241215
_bshamsul
_c201311281652
_dnabilah
_y201310311703
_znabilah
040 _aUMP
090 _aQR99.69.B55 N67 2012 rs Bc.
100 0 _aNor Fatihah Ab Ghani
245 1 0 _aControl of phycocyanin production from Spirulina platensis in fed-batch reactor using mid course correction policy /
_cNor Fatihah Ab Ghani
260 _aKuantan, Pahang :
_bUMP,
_c2012
300 _axiii, 43 p. :
_bill. ;
_c30 cm. +
_e1 CD-ROM
502 _aProject paper (Bachelor of Chemical Engineering (Biotechnology)) -- Universiti Malaysia Pahang – 2012
504 _aBibliography : p. [41]-43
520 3 _aPhycocyanin is a product of cultivation of Spirulina platensis, a blue-green microalga. Phycocyanin is widely used in medical treatment as a cancer inhibitor and as a natural dye for cosmetics and foods. Spirulina platensis has been cultivated recently in fed batch reactor to optimize the cell growth and product formation. Large scale production of Spirulina platensis gives more advantage especially in production cost but it is hard to control the final product to the desired value due to the disturbance occurred during the cultivation process. Therefore, Mid-Course Correction (MCC) policy is introduced to the process. Throughout the MCC, a model predictor is constructed to predict the final product concentration based on the previous experimental data. A control model is build for phycocyanin production based on the light intensity adjustment. The adjustment is made on day 5 of the cultivation process and simulation is done to recheck whether the final phycocyanin production is fall in the desired range.
650 0 _aCyanobacterial blooms
999 _aVIRTUA40
_c3891
_d3897
999 _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*9992