Citation: LÜ Yong-xing, XU Hai-yan, ZHOU Yi, CHEN Jian, WU Chuang-zhi. Direct synthesis of LPG from syngas in a single-tube reactor[J]. Journal of Fuel Chemistry and Technology, ;2015, 43(3): 331-337. shu

Direct synthesis of LPG from syngas in a single-tube reactor

  • Corresponding author: WU Chuang-zhi, 
  • Received Date: 15 August 2014

    Fund Project: 国家科技支撑计划(2012BAA09B03) (2012BAA09B03) 广东省战略新兴产业项目(2012A032300019)。 (2012A032300019)

  • A hybrid catalyst for the direct synthesis of liquefied petroleum gas (LPG) from syngas was prepared through mechanical mixing of methanol synthesis catalyst with dehydration catalyst; its catalytic performance was tested in a single-tube reactor with a simulated biogas at 220~330 ℃, 1.2~5.1 MPa and a space velocity of 500~3 000 h-1. The results indicated that the hybrid catalyst has a good activity; at 325 ℃, 2.1 MPa, and a space velocity of 1 500 h-1, CO conversion and LPG content in the hydrocarbons product are 72.36% and 71.21%, respectively. At 325 ℃ and 2.1 MPa, a stable operation can be realized at a space velocity below 2 500 h-1, whereas the temperature cannot be well controlled at a space velocity over 3 000 h-1, which may lead to the catalyst deactivation. The NH3-TPD, XRD, N2 sorption and TPO characterization results suggest that the deposition of coke and decrease of the mount of strong acid sites and surface area are responsible for the catalyst deactivation.
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