Selective production of aromatic hydrocarbons from catalytic pyrolysis of biomass over Cu or Fe loaded mesoporous rod-like alumina

RSC Advances ◽  
2016 ◽  
Vol 6 (56) ◽  
pp. 50618-50629 ◽  
Author(s):  
Surachai Karnjanakom ◽  
Asep Bayu ◽  
Pairuzha Xiaoketi ◽  
Xiaogang Hao ◽  
Suwadee Kongparakul ◽  
...  

The selective production of aromatic hydrocarbons from bio-oil derived from the fast pyrolysis of sunflower stalks over Cu or Fe-modified mesoporous rod-like alumina catalysts was investigated.

2012 ◽  
Vol 26 (5) ◽  
pp. 2962-2967 ◽  
Author(s):  
Chih-Chiang Chang ◽  
Seng-Rung Wu ◽  
Chi-Cheng Lin ◽  
Hou-Peng Wan ◽  
Hom-Ti Lee

2010 ◽  
Vol 38 (5) ◽  
pp. 554-559 ◽  
Author(s):  
Jun DU ◽  
Ping LIU ◽  
Zuo-hua LIU ◽  
Da-gui SUN ◽  
Chang-yuan TAO

Author(s):  
Xu Chen ◽  
Zihao Liu ◽  
Shujuan Li ◽  
Sunwen Xia ◽  
Ning Cai ◽  
...  

Energies ◽  
2019 ◽  
Vol 12 (18) ◽  
pp. 3474 ◽  
Author(s):  
Yichen Liu ◽  
James J. Leahy ◽  
Jacek Grams ◽  
Witold Kwapinski

Fast pyrolysis of Miscanthus, its hydrolysis residue and lignin were carried with a pyrolysis-gas chromatography/mass spectrometry (Py-GC/MS) followed by online vapor catalytic upgrading with sulfated ZrO2, sulfated TiO2 and sulfated 60 wt.% ZrO2-TiO2. The most evident influence of the catalyst on the vapor phase composition was observed for aromatic hydrocarbons, light phenols and heavy phenols. A larger amount of light phenols was detected, especially when 60 wt.% ZrO2-TiO2 was present. Thus, a lower average molecular weight and lower viscosity of bio-oil could be obtained with this catalyst. Pyrolysis was also performed at different pressures of hydrogen. The pressure of H2 has a great effect on the overall yield and the composition of biomass vapors. The peak area percentages of both aromatic hydrocarbons and cyclo-alkanes are enhanced with the increasing of H2 pressure. The overall yields are higher with the addition of either H2 or sulfated catalysts. This is beneficial as phenols are valuable chemicals, thus, increasing the value of bio-oil. The results show that the hydrolysis residue has the potential to become a resource for phenol production.


2012 ◽  
Vol 512-515 ◽  
pp. 338-342 ◽  
Author(s):  
Ping Lan ◽  
Li Hong Lan ◽  
Tao Xie ◽  
An Ping Liao

In the preparation of hydrogen, the bio-oil from pyrolysis of biomass must be further upgraded (catalytic steam reforming)SO as to improve its quality.However the catalyst used in the steam reforming reaction is easy to lose its activity due to being coked' SO that it is important to study the coke formation and its efects on the catalyst activity in the steam reforming process.Fourier Transform Infrared Spectroscopy were used to analyze the precursor of coke on the catalyst Ni/MgO-La2O3-Al2O3 used in steam reforming reaction and the mechanism of coking Was also discussed based on it.The results indicate that precursors of coke deposited inside the pore of the molecular sieve are mainly paraffin, alcohols, aldehydes and ketones, and aromatic compounds.


2014 ◽  
Vol 86 (5) ◽  
pp. 859-865 ◽  
Author(s):  
Andrea de Rezende Pinho ◽  
Marlon Brando Bezerra de Almeida ◽  
Fabio Leal Mendes ◽  
Vitor Loureiro Ximenes

AbstractThis paper shows how some existing refining technologies such as fluid catalytic cracking (FCC) can be modified to process bio-oil, derived from agricultural lignocellulosic wastes such as the sugar cane straw. Tests carried out in demonstration scale (150 kg/h) show the potential of these alternative materials to produce lignocellulosic gasoline or aromatic compounds, suitable to the petrochemical industry.


2010 ◽  
Vol 24 (10) ◽  
pp. 5727-5734 ◽  
Author(s):  
Matteo Calonaci ◽  
Roberto Grana ◽  
Emma Barker Hemings ◽  
Giulia Bozzano ◽  
Mario Dente ◽  
...  

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