Conversion of propane-butane fraction to arenes on zeolite catalystsmodified by gallium oxides
| Parent link: | Journal of Economics and Social Sciences: electronic scientific journal.— , 2012-.— 2312-2978 № 14.— 2019.— [5 p.] |
|---|---|
| Autore principale: | |
| Ente Autore: | |
| Riassunto: | Title screen The main industrial technologies used currently for the conversion of natural and associated petroleum gas (APG) aresteam reforming of methane and APG into synthesis gas on alum-nickel catalysts which is carried out at 860–950 ° Cand the Fisher-Tropsch process. The synthesis gas is further processed into hydrocarbons on iron and cobalt catalysts.The high temperature (860–950 ° C) in the processes, especially at the first stage of synthesis gas production and the lowselectivity of the target products in the Fischer-Tropsch process are major drawbacks of these technologies for theprocessing of natural gas (methane) and APG. The paper provides the comparative analysis of the activity and selectivityof microporous high-silica zeolites of the ZSM-5 type, synthesized using various additives, during the conversion ofnatural associated gas. |
| Pubblicazione: |
2019
|
| Serie: | Социологические науки |
| Soggetti: | |
| Accesso online: | http://earchive.tpu.ru/handle/11683/55739 |
| Natura: | Elettronico Capitolo di libro |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=584049 |
| Descrizione fisica: | 1 файл (444 Кб) |
|---|---|
| Riassunto: | Title screen The main industrial technologies used currently for the conversion of natural and associated petroleum gas (APG) aresteam reforming of methane and APG into synthesis gas on alum-nickel catalysts which is carried out at 860–950 ° Cand the Fisher-Tropsch process. The synthesis gas is further processed into hydrocarbons on iron and cobalt catalysts.The high temperature (860–950 ° C) in the processes, especially at the first stage of synthesis gas production and the lowselectivity of the target products in the Fischer-Tropsch process are major drawbacks of these technologies for theprocessing of natural gas (methane) and APG. The paper provides the comparative analysis of the activity and selectivityof microporous high-silica zeolites of the ZSM-5 type, synthesized using various additives, during the conversion ofnatural associated gas. |