Author/Authors :
Kim، نويسنده , , Kwangsu and Kim، نويسنده , , Youngdoo and Yang، نويسنده , , Changwon and Moon، نويسنده , , Jihong and Kim، نويسنده , , Beomjong and Lee، نويسنده , , Jeongwoo and Lee، نويسنده , , Uendo and Lee، نويسنده , , Seehoon and Kim، نويسنده , , Jaeho and Eom، نويسنده , , Wonhyun and Lee، نويسنده , , Sangbong and Kang، نويسنده , , Myungjin and Lee، نويسنده , , Yunje، نويسنده ,
Abstract :
Long-term operation of the biomass-to-liquid (BTL) process was conducted with a focus on the production of bio-syngas that satisfies the purity standards for the Fischer–Tropsch (FT) process. The integrated BTL system consisted of a bubbling fluidized bed (BFB) gasifier (20 kWth), gas cleaning unit, syngas compression unit, acid gas removing unit, and an FT reactor. Since the raw syngas from the gasifier contains different types of contaminants, such as particulates, condensable tars, and acid gases, which can cause various mechanical problems or deactivate the FT catalyst, the syngas was purified by passing through cyclones, a gravitational dust collector, a two-stage wet scrubber (packing-type), and a methanol absorption tower. The integrated system was operated for 500 h over several runs, and stable operating conditions for each component were achieved. The cleaned syngas contained no sulfur compounds (under 1 ppmV) and satisfied the requirements for the FT process.
Keywords :
Syngas cleaning , Biomass gasification , Fischer–Tropsch (FT) synthesis , Biomass to liquid (BTL) , Methanol absorption