| 000 | 02061ntm a2200289 a 4500 | ||
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| 001 | vtls000093802 | ||
| 003 | KUKTEM | ||
| 005 | 20251117113322.0 | ||
| 008 | 160314t2015 my a f 000 0 eng d | ||
| 020 | _aTHE0000888(Local) | ||
| 039 | 9 |
_a201905271503 _bnazirah _c201711290956 _dfateeha _y201603141150 _zhuda |
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| 040 | _aUMP | ||
| 090 | _aFKKSA .F57 2015 r Bc. | ||
| 100 | 0 | _aMohammad Firdaus Sahda | |
| 245 | 1 |
_aDevelopment of equilibrium model of vacuum distillation for benzene/toluene separation using mosaic software / _cMohammad Firdaus Sahda |
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| 260 |
_aKuantan, Pahang : _bUMP, _c2015 |
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| 300 |
_axiv, 63 p. : _bill. ; _c30 cm. + _e1 CD-ROM |
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| 500 | _aFaculty of Chemical & Natural Resources Engineering | ||
| 502 | _aProject Paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang – 2015 | ||
| 504 | _aBibliography : p. 24-25 | ||
| 520 | 3 | _aThis paper presents development of equilibrium model of vacuum distillation for benzene/toluene separation using MOSAIC software. The vacuum distillation process was modeled using MOSAIC software by key in the relevant equations and functions that related to vacuum distillation. The generated code from MOSAIC then transferred to MATLAB®environment to get the data for plotting the graph of temperature and composition profiles of vacuum distillation. The range of temperature in the vacuum distillation column was from 299 K to 318 K. The separation of benzene and toluene using vacuum distillation produce high purity of benzene at distillate which was 85 % of vapour mole fraction at distillate stream. Meanwhile, 92% of vapour mole fraction at bottom stream was toluene. | |
| 610 | 2 | 0 |
_aFaculty of Chemical & Natural Resources Engineering _xDissertations |
| 650 | 0 |
_aUniversities and Colleges _xDissertations |
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| 650 | 0 | _aTheses | |
| 856 | 4 | 0 |
_uhttp://ecollib.ump.edu.my/id/eprint/25600 _zAccess in library only |
| 999 |
_aVIRTUA40 _c6653 _d6659 |
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