Citation: ZHAO Peng, LI Jun-fang, WU Yan, MAO Xue-feng, ZHANG Xiao-jing, CHANG Qiu-lian. Reaction and hydrogen transfer in complex multi-phase system during coal hydro-liquefaction[J]. Journal of Fuel Chemistry and Technology, ;2018, 46(12): 1423-1429. shu

Reaction and hydrogen transfer in complex multi-phase system during coal hydro-liquefaction

  • Corresponding author: ZHAO Peng, 411296849@qq.com
  • Received Date: 12 June 2018
    Revised Date: 10 August 2018

    Fund Project: NSFC-Joint Funds for Coal Base Low Carbon of Shanxi Province of China U1610221the National Key R & D Program of China 2016YFB0600303The project was supported by the National Key R & D Program of China (2016YFB0600303) and NSFC-Joint Funds for Coal Base Low Carbon of Shanxi Province of China(U1610221)

Figures(7)

  • Reaction behavior of Naomaohu (NMH) coal in tetralin was carried out under atmosphere of H2. Hydrogen transfer in complex multi-phase system of direct coal liquefaction were discussed. The influence of phase transition process of iron-based catalyst on liquefaction performance was investigated using X-ray diffraction, saturate magnetization and scanning electron microscope. The results show that NMH coal presents good liquefaction performance at 420℃ and 17 MPa. Active phase Fe7S8 plays catalytic role during initial reaction and changes into nonactive phase-Fe9S10 and FeS later. High hydrogenation activity of catalyst and long residence time are beneficial to hydrogenation of preasphaltene and asphaltene into light oil. Catalyst promotes the activation of H2 transferring to coal pyrolysis products and solvent. Catalyst promotes the hydrogen in solvent to transfer to coal pyrolysis products as well. The contribution to activated hydrogen from solvent is twice as that from H2 in the condition of the experiment. Hydrogen transferring from H2 to solvent changes little with temperature, pressure and time. Activated hydrogen from H2 and solvent is proportional to the conversion of coal and asphaltene to oil and gas.
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