The catalytic cracking of the off-spec polyisoprene rubber thermolysis products
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products over a mesoporous zeolite has been studied on a laboratory unit with a fixed-bed reactor. The effect of the reaction temperature and the feed space velocity on the feedstock conversion degree and the yield of gas and gas...
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EDP Sciences
2020-01-01
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Online Access: | https://www.e3s-conferences.org/articles/e3sconf/pdf/2020/17/e3sconf_ktti2020_02027.pdf |
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doaj-4e229b5e61464b60bb29e1fecf31a80b2021-04-02T12:55:16ZengEDP SciencesE3S Web of Conferences2267-12422020-01-011570202710.1051/e3sconf/202015702027e3sconf_ktti2020_02027The catalytic cracking of the off-spec polyisoprene rubber thermolysis productsValiev Airat0Zemskii Dmitrii1Kazan National Research Technological UniversityKazan National Research Technological UniversityThe catalytic cracking of the off-spec polyisoprene rubber thermolysis products over a mesoporous zeolite has been studied on a laboratory unit with a fixed-bed reactor. The effect of the reaction temperature and the feed space velocity on the feedstock conversion degree and the yield of gas and gasoline has been studied. The data obtained has shown that at rates below 2 h-1, a high gas generation and a low yield of liquid products are observed, while at rates above 3 h-1, the total yield of gas and gasoline decreases. In the course of the work, it has been noted that the reduction in conditional conversion occurs with an increase in the feed rate. The maximum yield of gasoline observed at a feed rate of 3 h- 1 and amounted to 35.6 %, gas yield was inversely proportional to the feed rate, and the coke yield changed slightly. With an increase in the feed rate, the content of C3-C4 in gas increases. To achieve high conversion or a high gasoline yield, the optimal feed rate should be 2 and 3 h-1, respectively. The products obtained in this process can be used as the motor fuel components.https://www.e3s-conferences.org/articles/e3sconf/pdf/2020/17/e3sconf_ktti2020_02027.pdf |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Valiev Airat Zemskii Dmitrii |
spellingShingle |
Valiev Airat Zemskii Dmitrii The catalytic cracking of the off-spec polyisoprene rubber thermolysis products E3S Web of Conferences |
author_facet |
Valiev Airat Zemskii Dmitrii |
author_sort |
Valiev Airat |
title |
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products |
title_short |
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products |
title_full |
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products |
title_fullStr |
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products |
title_full_unstemmed |
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products |
title_sort |
catalytic cracking of the off-spec polyisoprene rubber thermolysis products |
publisher |
EDP Sciences |
series |
E3S Web of Conferences |
issn |
2267-1242 |
publishDate |
2020-01-01 |
description |
The catalytic cracking of the off-spec polyisoprene rubber thermolysis products over a mesoporous zeolite has been studied on a laboratory unit with a fixed-bed reactor. The effect of the reaction temperature and the feed space velocity on the feedstock conversion degree and the yield of gas and gasoline has been studied. The data obtained has shown that at rates below 2 h-1, a high gas generation and a low yield of liquid products are observed, while at rates above 3 h-1, the total yield of gas and gasoline decreases. In the course of the work, it has been noted that the reduction in conditional conversion occurs with an increase in the feed rate. The maximum yield of gasoline observed at a feed rate of 3 h- 1 and amounted to 35.6 %, gas yield was inversely proportional to the feed rate, and the coke yield changed slightly. With an increase in the feed rate, the content of C3-C4 in gas increases. To achieve high conversion or a high gasoline yield, the optimal feed rate should be 2 and 3 h-1, respectively. The products obtained in this process can be used as the motor fuel components. |
url |
https://www.e3s-conferences.org/articles/e3sconf/pdf/2020/17/e3sconf_ktti2020_02027.pdf |
work_keys_str_mv |
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