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    • Journal of Petroleum Science and Technology
    • Volume 13, Issue 1
    • مشاهده مورد
    •   صفحهٔ اصلی
    • نشریات انگلیسی
    • Journal of Petroleum Science and Technology
    • Volume 13, Issue 1
    • مشاهده مورد
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    N2-bubbling Method for O2 Removal from the Loaded MEA Solution in the CO2 Capture Process

    (ندگان)پدیدآور
    Shokouhi, MohammadZoghi, AliMehrabi, Mehrnooshabbasghorbani, maryamZamaniyan, AkbarZhaleh Rajabi, Ehsan
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    نوع مدرک
    Text
    Research Paper
    زبان مدرک
    English
    نمایش کامل رکورد
    چکیده
    Flue gas stream contains full-oxidized (carbon dioxide), partially oxidized hydrocarbons, and some extent of oxygen. Carbon dioxide can be separated by CO2 capture and separation (CCS) process using monoethanolamine (MEA). In this process, CO2 accompanied with O2 can be absorbed by the solution (MEA+H2O). Dissolved molecular oxygen may explicitly participate in the cathodic reaction and generate sever corrosion problems, or it may induce amine degradation via irreversible oxidative reaction, reducing amine efficiency. In this research, the method of N2-bubbling was investigated for deoxygenation of loaded aqueous MEA solution on a laboratory scale. N2-bubbling set-up was simulated with a known volume glass vessel in which bubbling of N2 with an available flow rate was applied through the loaded amine solution. A mathematical formula was developed to correlate the N2-bubbling flow rate, F, the volume of amine solution in the bubbling column, V, and time taking the oxygen concentration decreases from saturated O2-solution to less than 0.5 mg/L.
    کلید واژگان
    CO2 capture
    De-oxygenation
    Dissolved oxygen
    monoethanolamine solution
    N2-Bubbling

    شماره نشریه
    1
    تاریخ نشر
    2023-02-01
    1401-11-12
    ناشر
    Research Institute of Petroleum Industry (RIPI)
    سازمان پدید آورنده
    Gas Refining Technology Group, Gas Research Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran.
    Gas Refining Technology Group, Gas Research Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran.\Natural Gas Sweetening Group, Gas Processing Institute (GPI), Tehran, Iran.
    Gas Refining Technology Group, Gas Research Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran.
    Gas Refining Technology Group, Gas Research Division, Research Institute of Petroleum Industry (RIPI), Tehran, Iran.
    Downstream Research Center, Research Institute of Petroleum Industry (RIPI),Tehran, Iran
    Department of Chemical Engineering, Universiti of Teknologi Petronas, malysia

    شاپا
    2251-659X
    2645-3312
    URI
    https://dx.doi.org/10.22078/jpst.2023.5123.1880
    https://jpst.ripi.ir/article_1355.html
    https://iranjournals.nlai.ir/handle/123456789/1064393

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