Development of the Mathematical Model of Diesel Fuel Catalytic Dewaxing Process Taking into Account Factors of Nonstationarity; MATEC Web of Conferences; Vol. 85 : Chemistry and Chemical Technology in XXI Century (CCT 2016)
| Parent link: | MATEC Web of Conferences Vol. 85 : Chemistry and Chemical Technology in XXI Century (CCT 2016).— 2016.— [01023, 5 p.] |
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| 其他作者: | , |
| 總結: | Title screen The paper describes the results of mathematical modelling of diesel fuel catalytic dewaxing process, performed taking into account the factors of process nonstationarity driven by changes in process technological parameters, feedstock composition and catalyst deactivation. The error of hydrocarbon contents calculation via the use of the developed model does not exceed 1.6 wt.%. This makes it possible to apply the model for solution to optimization and forecasting problems occurred in catalytic systems under industrial conditions. It was shown through the model calculation that temperature in the dewaxing reactor without catalyst deactivation is lower by 19 °С than actual and catalyst deactivation degree accounts for 32 %. |
| 語言: | 英语 |
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2016
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| 在線閱讀: | http://dx.doi.org/10.1051/matecconf/20168501023 http://earchive.tpu.ru/handle/11683/36577 |
| 格式: | 電子 Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=652855 |
| 總結: | Title screen The paper describes the results of mathematical modelling of diesel fuel catalytic dewaxing process, performed taking into account the factors of process nonstationarity driven by changes in process technological parameters, feedstock composition and catalyst deactivation. The error of hydrocarbon contents calculation via the use of the developed model does not exceed 1.6 wt.%. This makes it possible to apply the model for solution to optimization and forecasting problems occurred in catalytic systems under industrial conditions. It was shown through the model calculation that temperature in the dewaxing reactor without catalyst deactivation is lower by 19 °С than actual and catalyst deactivation degree accounts for 32 %. |
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| DOI: | 10.1051/matecconf/20168501023 |