Sungmin Kim, Boda Yang, Oliver Y. Gutiérrez, Wei Zhang, Carlos Lizandara-Pueyo, Piyush Ingale, Ivana Jevtovikj, Reni Grauke, Janos Szanyi, Huamin Wang, Stephan A. Schunk and Johannes A. Lercher*,
{"title":"准超临界条件下钌催化聚乙烯氢解","authors":"Sungmin Kim, Boda Yang, Oliver Y. Gutiérrez, Wei Zhang, Carlos Lizandara-Pueyo, Piyush Ingale, Ivana Jevtovikj, Reni Grauke, Janos Szanyi, Huamin Wang, Stephan A. Schunk and Johannes A. Lercher*, ","doi":"10.1021/jacsau.5c0000610.1021/jacsau.5c00006","DOIUrl":null,"url":null,"abstract":"<p >Ru/C-catalyzed polyethylene (PE) and hydrocarbon hydrogenolysis under quasi-supercritical fluid of isopentane was kinetically and mechanistically investigated. PE hydrogenolysis with C–C and C–H cleavage showed zeroth order, suggesting strong adsorption of hydrocarbons. PE yielded broad product distribution of heavy (C<sub>21–40</sub>) and diesel-range (C<sub>11–20</sub>) hydrocarbons in the primary step of hydrogenolysis due to stochastic C–C cleavage over Ru surface. Catalytic hydrogenolysis of <i>n</i>-hexadecane, squalane, and light hydrocarbons such as <i>n</i>-pentane, iso-pentane, and <i>n</i>-hexane further described C–C cleavage reactivity between primary and secondary carbons, i.e., <sup>1</sup>C–<sup>2</sup>C and <sup>2</sup>C–<sup>2</sup>C, which has an order of magnitude higher hydrogenolysis rate than that involving a tertiary carbon. The PE saturated Ru surface and lower C–C cleavage reactivity of tertiary carbon in iso-pentane, therefore, imited sovlent conversion during hydrogenolysis, whereas leading to selective PE conversion. Using hexadecane, we observed comparable hydrogenolysis rates between H<sub>2</sub> and D<sub>2</sub> (<i>k</i><sub>H</sub><i>/k</i><sub>D</sub> ∼ 1), indicating the kinetically relevant step of C–C cleavage with facilitating C–H cleavage and rehydrogenation. However, the normal kinetic isotope effect between hexadecane and deuterated hexadecane (<i>k</i><sub>C<sub>16</sub>H<sub>34</sub></sub><i>/k</i><sub>C<sub>16</sub>D<sub>34</sub></sub> ∼ 5) revealed that the dehydrogenation, i.e., C–H cleavage, can be kinetically involved in the hydrogenolysis kinetic. By considering the 8-fold lower H-D exchange rate with deuterated hexadecane compared to n-hexadecane, the lower rate for hydrogenolysis and H-D exchange with deuterated hexadecane can be attributed to the C–D bond dissociation energy being 3 kJ/mol higher than that of the C–H bond. Increasing H<sub>2</sub> pressure favors internal C–C bond cleavage over terminal one. This minimizes the formation of lower hydrocarbons, particularly methane. However, the increase in H<sub>2</sub> pressure increases the coverage of adsorbed hydrogen on the Ru particles due to competitive adsorption of H<sub>2</sub> and polyethylene, which, in turn, reduces the polyethylene conversion rates.</p>","PeriodicalId":94060,"journal":{"name":"JACS Au","volume":"5 4","pages":"1760–1770 1760–1770"},"PeriodicalIF":8.5000,"publicationDate":"2025-04-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://pubs.acs.org/doi/epdf/10.1021/jacsau.5c00006","citationCount":"0","resultStr":"{\"title\":\"Ru-Catalyzed Polyethylene Hydrogenolysis under Quasi-Supercritical Conditions\",\"authors\":\"Sungmin Kim, Boda Yang, Oliver Y. Gutiérrez, Wei Zhang, Carlos Lizandara-Pueyo, Piyush Ingale, Ivana Jevtovikj, Reni Grauke, Janos Szanyi, Huamin Wang, Stephan A. Schunk and Johannes A. Lercher*, \",\"doi\":\"10.1021/jacsau.5c0000610.1021/jacsau.5c00006\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >Ru/C-catalyzed polyethylene (PE) and hydrocarbon hydrogenolysis under quasi-supercritical fluid of isopentane was kinetically and mechanistically investigated. PE hydrogenolysis with C–C and C–H cleavage showed zeroth order, suggesting strong adsorption of hydrocarbons. PE yielded broad product distribution of heavy (C<sub>21–40</sub>) and diesel-range (C<sub>11–20</sub>) hydrocarbons in the primary step of hydrogenolysis due to stochastic C–C cleavage over Ru surface. Catalytic hydrogenolysis of <i>n</i>-hexadecane, squalane, and light hydrocarbons such as <i>n</i>-pentane, iso-pentane, and <i>n</i>-hexane further described C–C cleavage reactivity between primary and secondary carbons, i.e., <sup>1</sup>C–<sup>2</sup>C and <sup>2</sup>C–<sup>2</sup>C, which has an order of magnitude higher hydrogenolysis rate than that involving a tertiary carbon. The PE saturated Ru surface and lower C–C cleavage reactivity of tertiary carbon in iso-pentane, therefore, imited sovlent conversion during hydrogenolysis, whereas leading to selective PE conversion. Using hexadecane, we observed comparable hydrogenolysis rates between H<sub>2</sub> and D<sub>2</sub> (<i>k</i><sub>H</sub><i>/k</i><sub>D</sub> ∼ 1), indicating the kinetically relevant step of C–C cleavage with facilitating C–H cleavage and rehydrogenation. However, the normal kinetic isotope effect between hexadecane and deuterated hexadecane (<i>k</i><sub>C<sub>16</sub>H<sub>34</sub></sub><i>/k</i><sub>C<sub>16</sub>D<sub>34</sub></sub> ∼ 5) revealed that the dehydrogenation, i.e., C–H cleavage, can be kinetically involved in the hydrogenolysis kinetic. By considering the 8-fold lower H-D exchange rate with deuterated hexadecane compared to n-hexadecane, the lower rate for hydrogenolysis and H-D exchange with deuterated hexadecane can be attributed to the C–D bond dissociation energy being 3 kJ/mol higher than that of the C–H bond. Increasing H<sub>2</sub> pressure favors internal C–C bond cleavage over terminal one. This minimizes the formation of lower hydrocarbons, particularly methane. However, the increase in H<sub>2</sub> pressure increases the coverage of adsorbed hydrogen on the Ru particles due to competitive adsorption of H<sub>2</sub> and polyethylene, which, in turn, reduces the polyethylene conversion rates.</p>\",\"PeriodicalId\":94060,\"journal\":{\"name\":\"JACS Au\",\"volume\":\"5 4\",\"pages\":\"1760–1770 1760–1770\"},\"PeriodicalIF\":8.5000,\"publicationDate\":\"2025-04-16\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://pubs.acs.org/doi/epdf/10.1021/jacsau.5c00006\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"JACS Au\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://pubs.acs.org/doi/10.1021/jacsau.5c00006\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"CHEMISTRY, MULTIDISCIPLINARY\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"JACS Au","FirstCategoryId":"1085","ListUrlMain":"https://pubs.acs.org/doi/10.1021/jacsau.5c00006","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
Ru-Catalyzed Polyethylene Hydrogenolysis under Quasi-Supercritical Conditions
Ru/C-catalyzed polyethylene (PE) and hydrocarbon hydrogenolysis under quasi-supercritical fluid of isopentane was kinetically and mechanistically investigated. PE hydrogenolysis with C–C and C–H cleavage showed zeroth order, suggesting strong adsorption of hydrocarbons. PE yielded broad product distribution of heavy (C21–40) and diesel-range (C11–20) hydrocarbons in the primary step of hydrogenolysis due to stochastic C–C cleavage over Ru surface. Catalytic hydrogenolysis of n-hexadecane, squalane, and light hydrocarbons such as n-pentane, iso-pentane, and n-hexane further described C–C cleavage reactivity between primary and secondary carbons, i.e., 1C–2C and 2C–2C, which has an order of magnitude higher hydrogenolysis rate than that involving a tertiary carbon. The PE saturated Ru surface and lower C–C cleavage reactivity of tertiary carbon in iso-pentane, therefore, imited sovlent conversion during hydrogenolysis, whereas leading to selective PE conversion. Using hexadecane, we observed comparable hydrogenolysis rates between H2 and D2 (kH/kD ∼ 1), indicating the kinetically relevant step of C–C cleavage with facilitating C–H cleavage and rehydrogenation. However, the normal kinetic isotope effect between hexadecane and deuterated hexadecane (kC16H34/kC16D34 ∼ 5) revealed that the dehydrogenation, i.e., C–H cleavage, can be kinetically involved in the hydrogenolysis kinetic. By considering the 8-fold lower H-D exchange rate with deuterated hexadecane compared to n-hexadecane, the lower rate for hydrogenolysis and H-D exchange with deuterated hexadecane can be attributed to the C–D bond dissociation energy being 3 kJ/mol higher than that of the C–H bond. Increasing H2 pressure favors internal C–C bond cleavage over terminal one. This minimizes the formation of lower hydrocarbons, particularly methane. However, the increase in H2 pressure increases the coverage of adsorbed hydrogen on the Ru particles due to competitive adsorption of H2 and polyethylene, which, in turn, reduces the polyethylene conversion rates.