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    •   صفحهٔ اصلی
    • نشریات انگلیسی
    • Journal of Petroleum Science and Technology
    • Volume 13, Issue 3
    • مشاهده مورد
    •   صفحهٔ اصلی
    • نشریات انگلیسی
    • Journal of Petroleum Science and Technology
    • Volume 13, Issue 3
    • مشاهده مورد
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    Deactivation of Activated Alumina Adsorbents Used for H2S Removal from Olefin-containing Streams

    (ندگان)پدیدآور
    Sadighi, SepehrAnisi, HosseinGhorbani, YousefaliKarimi, Ali
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    نوع مدرک
    Text
    Research Paper
    زبان مدرک
    English
    نمایش کامل رکورد
    چکیده
    An oligomer produced from unsaturated and reactive components (green oil) is formed when hydrogen sulfide (H2S) is removed from the exhaust stream of the methyl tert-butyl ether (MTBE) plant. A remedy to minimize this contaminant formation is using adsorbents with low reactivity toward the olefinic precursors. Here, the green oil formation on the surface of different types of commercial alumina is studied. Results confirm that the regular commercially activated alumina has low H2S adsorption capacity. Still, the alumina alkalized with 3.98 wt.% of Na2O has a breakthrough time of more than 29 h and stable performance in a cyclic operation. Moreover, the promoted alumina with a wide pore diameter (about 9 nm) and low surface area (about 215 m2/g) is less susceptible to deactivation by forming green oil. It is supposed that the capillary condensation of C3/C4 unsaturated compounds and acidic sites of the alumina intensify the oligomerization inside the pores of an adsorbent.
    کلید واژگان
    Green oil
    Activated alumina
    Adsorption
    Methyl tert-butyl ether
    Hydrogen Sulfide

    شماره نشریه
    3
    تاریخ نشر
    2023-07-01
    1402-04-10
    ناشر
    Research Institute of Petroleum Industry (RIPI)
    سازمان پدید آورنده
    Catalysis Development Technologies Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran
    Iran University of Science and Technology, School of Chemical, Petroleum and Gas Engineering, Tehran, Iran
    Catalysis Development Technologies Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran
    Catalysis Development Technologies Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran

    شاپا
    2251-659X
    2645-3312
    URI
    https://dx.doi.org/10.22078/jpst.2024.5218.1900
    https://jpst.ripi.ir/article_1399.html
    https://iranjournals.nlai.ir/handle/123456789/1089937

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