Industrial operation analysis of Pt-Re reforming catalyst at the industrial unit by predictive modelling method; Petroleum and Coal; Vol. 60, iss. 3
| Parent link: | Petroleum and Coal Vol. 60, iss. 3.— 2018.— [P. 416-421] |
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| Institution som forfatter: | |
| Andre forfattere: | , , , , |
| Summary: | Title screen Analysis of the PR-51 catalyst operation effectiveness of the reforming process was conducted with mathematical modelling method using. The main characteristics of PR-51 reforming catalyst were calculated. It was found that the catalyst has proven to be appropriate in operation and ensure high selectivity. It is shown that the product yield increases by 3-5%mass with octane number 96-97. |
| Sprog: | engelsk |
| Udgivet: |
2018
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| Fag: | |
| Online adgang: | https://www.vurup.sk/wp-content/uploads/2018/05/PC_3_2018_Belinskaya_13.pdf |
| Format: | Electronisk Book Chapter |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=659871 |
| Summary: | Title screen Analysis of the PR-51 catalyst operation effectiveness of the reforming process was conducted with mathematical modelling method using. The main characteristics of PR-51 reforming catalyst were calculated. It was found that the catalyst has proven to be appropriate in operation and ensure high selectivity. It is shown that the product yield increases by 3-5%mass with octane number 96-97. |
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