| 000 | 02511naa2a2200385 4500 | ||
|---|---|---|---|
| 001 | 573735 | ||
| 005 | 20231030032243.0 | ||
| 035 | _a(RuTPU)RU\TPU\prd\272247 | ||
| 035 | _aRU\TPU\prd\272245 | ||
| 090 | _a573735 | ||
| 100 | _a20170623a2017 k y0rusy50 ba | ||
| 101 | 0 | _aeng | |
| 102 | _aRU | ||
| 135 | _adrcn ---uucaa | ||
| 200 | 1 |
_aProduction and purification of biodiesel produced from used frying oilusing hydrodynamic cavitation _bElectronic resource _fN. S. Kolhe, A. R. Gupta, A. R. Gupta |
|
| 203 |
_aText _celectronic |
||
| 300 | _aTitle screen | ||
| 320 | _a[References: p. 203 (25 tit.)] | ||
| 330 | _aThis work describes the biodiesel production from used frying oil using a hydrodynamic cavitation reactor as well as separation and purification of fatty acid methyl esters (FAME). Under the optimized process conditions, i.e., methanol to oil molar ratio of 4.5:1 and catalyst (KOH) concentration of 0.55 wt%, the conversion achieved was 93.86 mol%. Higher conversion (93.6%) was obtained in only 20 min as compared to 88.5% in 1 h in stirred tank reactor. Due to the completion of transesterification reaction, the amount of intermediate diglycerides and monoglycerides present in the reaction mixture was less. It helps for the complete separation of methyl ester and glycerol layers without hindrance in 1 h. Small amount KOH catalyst used for completion of reaction reduces amount of KOH and soap in ester layer which further helps to form a less stable emulsion during water washing step. The complete separation was observed at 70 °C temperature in just 3 h. Thus, this study indicates that the increased production capacity can be achieved by shortening the time for the separation and purification. | ||
| 461 | 1 |
_0(RuTPU)RU\TPU\prd\247369 _x2405-6537 _tResource-Efficient Technologies _oelectronic scientific journal _fNational Research Tomsk Polytechnic University (TPU) _d2015- |
|
| 463 | 1 |
_0(RuTPU)RU\TPU\prd\272237 _tVol. 3, iss. 2 _v[P. 198–203] _d2017 |
|
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _abiodiesel | |
| 610 | 1 | _aseparation | |
| 610 | 1 | _aбиодизели | |
| 610 | 1 | _aпереэтерификация | |
| 610 | 1 | _aреакторы | |
| 700 | 1 |
_aKolhe _bN. S. _gNitin |
|
| 701 | 1 |
_aGupta _bA. R. _gAnilkumar |
|
| 701 | 1 |
_aGupta _bA. R. _gAnilkumar |
|
| 801 | 1 |
_aRU _b63413507 _c20090623 _gPSBO |
|
| 801 | 2 |
_aRU _b63413507 _c20180831 _gPSBO |
|
| 856 | 4 | _uhttp://earchive.tpu.ru/handle/11683/50291 | |
| 942 | _cBK | ||