| 000 | 01920nam a2200253 a 4500 | ||
|---|---|---|---|
| 001 | vtls000075748 | ||
| 003 | KUKTEM | ||
| 005 | 20251114204543.0 | ||
| 008 | 131028t2013 my da f abm 000 0 eng d | ||
| 020 | _aTHE0004490(Local) | ||
| 039 | 9 |
_a201905170848 _brohana _y201310281000 _znabilah |
|
| 040 | _aUMP | ||
| 090 | _aTP248.27.P55 T38 2013 rs Bc. | ||
| 100 | 0 | _aMohd Taufiq Rasdi | |
| 245 | 1 | 0 |
_aScale up study on production of biodiesel from Jatropha crude oil / _cMohd Taufiq Rasdi |
| 260 |
_aKuantan, Pahang : _bUMP, _c2013 |
||
| 300 |
_axvi, 69 p. : _bill. ; _c30 cm. + _e1 CD-ROM |
||
| 502 | _aProject paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2013 | ||
| 504 | _aBibliography : p. 64-67 | ||
| 520 | 3 | _aScale up is a very important activity in designing new industrial plants especially in specialty or fine chemicals production. The purposes of this study is to study on different between laboratory scale production and pilot plant production of biodiesel from Jatropha crude oil and to establish correlations between laboratory scale and pilot plant scale for construction of commercial plant. Transesterification process used KOH as a catalyst. The optimum quantity of methanol, catalyst KOH, reaction temperature and reaction time required for the transesterification of Jatropha oil were conducted by varying them. Then, the optimized conditions from laboratory scale were used in pilot plant scale. From this study, it was found that for laboratory scale and pilot plant scale, there are some differences in the value of the final yield. The difference of value of yield between the laboratory scale and pilot plant run was caused by several factors such as handling, operating conditions and others. | |
| 650 | 0 |
_aJatropha _xBiotechnology |
|
| 650 | 0 | _aBiodiesel fuels | |
| 999 |
_aVIRTUA40 _c4032 _d4038 |
||
| 999 | _aVTLSSORT0080*0200*0400*0900*1000*2450*2600*3000*5020*5040*5200*6500*6501*9992 | ||