skip to main content

Catalytic pyrolysis of bamboo in a bubbling fluidized-bed reactor with two different catalysts: HZSM-5 and red mud for upgrading bio-oil

Ly, Hoang Vu ; Park, Jeong Woo ; Kim, Seung-Soo ; Hwang, Hyun Tae ; Kim, Jinsoo ; Woo, Hee Chul

Renewable Energy, April 2020, Vol.149, pp.1434-1445 [Periódico revisado por pares]

Texto completo disponível

Citações Citado por
  • Título:
    Catalytic pyrolysis of bamboo in a bubbling fluidized-bed reactor with two different catalysts: HZSM-5 and red mud for upgrading bio-oil
  • Autor: Ly, Hoang Vu ; Park, Jeong Woo ; Kim, Seung-Soo ; Hwang, Hyun Tae ; Kim, Jinsoo ; Woo, Hee Chul
  • Assuntos: Bubbling Fluidized-Bed Reactor ; Fractional Catalytic Pyrolysis ; Hzsm-5 ; Red Mud ; Bamboo ; Bubbling Fluidized-Bed Reactor ; Fractional Catalytic Pyrolysis ; Hzsm-5 ; Red Mud ; Bamboo ; Engineering
  • É parte de: Renewable Energy, April 2020, Vol.149, pp.1434-1445
  • Descrição: Bamboo has been considered a potential feedstock of energy for the future. It can be subjected to the pyrolysis for biofuels production. The thermogravimetric analysis (TGA) combined with differential thermogravimetric analysis (DTG) for bamboo was carried out prior to pyrolysis. The thermal degradation of bamboo was mainly between 230 and 420 °C. The conventional pyrolysis of bamboo was investigated in a bubbling fluidized-bed reactor using silica sand. The product distribution and composition of pyrolysis bio-oil were dependent on biomass component and operating conditions such as pyrolysis temperature, fluidization velocity, and particle size of biomass. The fractional catalytic pyrolysis of bamboo was also studied to upgrade the pyrolysis vapor, using HZSM-5 and red mud. The highest yield of bio-oil was 54.03 wt% compared to 49.14 wt% and 50.34 wt% of HZSM-5 and red mud catalyst, respectively. In the red mud catalytic pyrolysis, the oxygen content was rejected from pyrolysis...
  • Idioma: Inglês

Buscando em bases de dados remotas. Favor aguardar.