Jute stick pyrolysis for bio-oil production in fluidized bed reactor

被引：110

作者：

Asadullah, M. ^{[1
]}

Rahman, M. Anisur ^{[1
]}

Ali, M. Mohsin ^{[1
]}

Motin, M. Abdul ^{[1
]}

Sultan, M. Borhanus ^{[1
]}

Alam, M. Robiul ^{[1
]}

Rahman, M. Sahedur ^{[1
]}

机构：

[1] Rajshahi Univ, Dept Appl Chem & Chem Technol, Rajshahi 6205, Bangladesh

来源：

BIORESOURCE TECHNOLOGY | 2008年 / 99卷 / 01期

关键词：

jute stick; pyrolysis; bio-oil; renewable fuel; fluidized-bed reactor;

D O I：

10.1016/j.biortech.2006.12.002

中图分类号：

S2 [农业工程];

学科分类号：

0828 ;

摘要：

Pyrolysis of jute stick for bio-oil production has been investigated in a continuous feeding fluidized bed reactor at different temperatures ranging from 300 degrees C to 600 degrees C. At 500 degrees C, the yields of bio-oil, char and non-condensable gas were 66.70 wt%, 22.60 wt% and 10.70 wt%, respectively based on jute stick. The carbon based non-condensable gas was the mixture of carbon monoxide, carbon dioxide, methane, ethane, ethene, propane and propene. The density and viscosity of bio-oil were found to be 1.11 g/mL and 2.34 cP, respectively. The lower heating value (LHV) of bio-oil was found to be 18.25 MJ/kg. Since bio-oil contains some organic acids such as formic acid, acetic acid, etc., the pH and acid value of the bio-oil were found to be around 4 and 135 mg KOH/g, respectively. The water, lignin, solid and ash contents of bio-oil were determined and found to be around 15 wt%, 4.90 wt%, 0.02 wt% and 0.10 wt%, respectively. (C) 2006 Elsevier Ltd. All rights reserved.

引用

页码：44 / 50

页数：7

共 50 条

[1] Bio-Oil Production from Fast Pyrolysis of Cotton Stalk in Fluidized Bed Reactor [J].

Najaf Ali ;

Mahmood Saleem ;

Khurram Shahzad ;

Arshad Chughtai .

Arabian Journal for Science and Engineering, 2015, 40 :3019-3027

[2] Bio-Oil Production from Fast Pyrolysis of Cotton Stalk in Fluidized Bed Reactor [J].

Ali, Najaf ;

Saleem, Mahmood ;

Shahzad, Khurram ;

Chughtai, Arshad .

ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING, 2015, 40 (11) :3019-3027

[3] Fast pyrolysis of microalgae remnants in a fluidized bed reactor for bio-oil and biochar production [J].

Wang, Kaige ;

Brown, Robert C. ;

Homsy, Sally ;

Martinez, Liliana ;

Sidhu, Sukh S. .

BIORESOURCE TECHNOLOGY, 2013, 127 :494-499

[4] Flash pyrolysis of biomass for bio-oil in a fluidized bed reactor [J].

Wang, SR ;

Luo, ZY ;

Yu, CJ ;

Liao, YF ;

Hong, J ;

Cen, KF ;

Dong, LJ .

ENERGY AND ENVIRONMENT, VOLS 1 AND 2, 2003, :245-250

[5] Bio-oil production via fast pyrolysis of shrub residues in a fluidized-bed reactor [J].

Yang Haiqing ;

Wang Qirui ;

Sang Yuqiang ;

Fan Guoqiang .

ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2016, 38 (08) :1125-1131

[6] Production of Bio-oil from Pine Sawdust by Rapid Pyrolysis in a Fluidized-bed Reactor [J].

Suttibak, S. ;

Sriprateep, K. ;

Pattiya, A. .

ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2015, 37 (13) :1440-1446

[7] Bio-oil production from fast pyrolysis of Cladophora glomerata in a fluidized bed reactor [J].

Ebadi, A. G. ;

Hisoriev, H. .

BULGARIAN CHEMICAL COMMUNICATIONS, 2017, 49 (02) :504-508

[8] Fast Pyrolysis of Corn Straw for Bio-oil Production in a Bench-scale Fluidized Bed Reactor [J].

Liu, R. ;

Deng, C. ;

Wang, J. .

ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2010, 32 (01) :10-19

[9] Flash Pyrolysis of Lemon Grass (Cymbopogon flexuosus) for Bio-oil Production in an Electrically Heated Fluidized Bed Reactor [J].

P. Madhu ;

T. Stephen Livingston ;

H. Kanagasabapathy .

Waste and Biomass Valorization, 2018, 9 :1037-1046

[10] Fast pyrolysis of raw and acid-washed cattle manure in a fluidized bed reactor for the production of bio-oil [J].

Jeon, Jae-Rak ;

Hidayat, Syarif ;

Kim, Jinsoo ;

Hwang, Hyun Tae ;

Kim, Seung-Soo .

JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2025, 186

← 1 2 3 4 5 →