Fast Pyrolysis of Industrial Biomass Waste

Author(s):  
Ch. Gerdes ◽  
D. Meier ◽  
W. Kaminsky
Keyword(s):  
2012 ◽  
Vol 40 (5) ◽  
pp. 493-498 ◽  
Author(s):  
Feng Peng ◽  
Pi-Wen He ◽  
Yin Luo ◽  
Xiang Lu ◽  
Ying Liang ◽  
...  

2016 ◽  
Vol 18 (20) ◽  
pp. 5643-5650 ◽  
Author(s):  
Ke Tian ◽  
Wu-Jun Liu ◽  
Shun Zhang ◽  
Hong Jiang

The production of phenol in high yield and selectivity by direct catalytic hydroxylation of benzene (HOB) is challenging.


2018 ◽  
Vol 3 (7) ◽  
pp. 33
Author(s):  
Asmaa Ali Mohammed Ali ◽  
Mustafa Abbas Mustafa ◽  
Kamal Eldin Eltayeb Yassin

The increasing demand for transportation fuel, due to increased urbanization, is now compounded by depleting and unstable crude oil reserves. Furthermore, the volatile market and the negative environmental impact of fossil fuels have driven the usage of biomass as a potential energy source. Of particular interest are biomass waste and baobab shells present an interesting option. The objective of this study is to produce bio oil by a fast pyrolysis process from baobab shells. The effect of reaction temperature, biomass particle size and fluidizing gas flow rate on the liquid product yield are investigated. The maximum liquid yield obtained was 36.6% at 500 OC at a N2 gas flowrate of 11.6 l/min and a particle size of less than 0.5 mm.


2011 ◽  
Vol 201-203 ◽  
pp. 708-713
Author(s):  
Rui Li ◽  
Liang Jing Jing ◽  
Ming Ming He

Biomass fast pyrolysis technology is one of most promising methods to utilize biomass resources, for its high production of pyrolysis liquid named bio-oil. And the fast pyrolysis fluidized reactor is widely used because of the advantages of simple structure, and easy to enlarge. The understanding of computational fluid dynamics (CFD) of its fluidized bed is necessary basis for particulate heat transfer and pyrolysis kinetics research. In this paper, modern hydrodynamic theory and calculation means is employed to simulate the cold state of fluid behavior in the pilot-scale fluidized pyrolysis reactor. The simulation results are in good agreement with the empirical equation and experimental data, with resultant error lower than 10%. Based on the cold state simulation, we modeled the fluid flow behavior in the fluidized reactor during fast pyrolysis under high temperature, and calculated the fluidization velocity and the distribution of solid phase fraction.


Materials ◽  
2021 ◽  
Vol 14 (11) ◽  
pp. 2969
Author(s):  
Paweł Kazimierski ◽  
Paulina Hercel ◽  
Tomasz Suchocki ◽  
Jakub Smoliński ◽  
Agnieszka Pladzyk ◽  
...  

The routine pruning and cutting of fruit trees provides a considerable amount of biowaste each year. This lignocellulosic biomass, mainly in the form of branches, trunks, rootstocks, and leaves, is a potential high-quality fuel, yet often is treated as waste. The results of a feasibility study on biochar production by pyrolysis of residues from orchard pruning were presented. Three types of biomass waste were selected as raw materials and were obtained from the most common fruit trees in Poland: apple (AP), pear (PR), and plum (PL) tree prunings. Two heating rates and three final pyrolysis temperatures were applied. For the slow (SP) and fast pyrolysis (FP) processes, the heating rates were 15 °C/min and 100 °C/min, respectively. The samples were heated from 25 °C up to 400, 500, and 600 °C. Chemical analyses of the raw materials were conducted, and the pyrolysis product yields were determined. A significant rise of higher heating value (HHV) was observed for the solid pyrolysis products, from approximately 23.45 MJ/kg for raw materials up to approximately 29.52 MJ/kg for pyrolysis products at 400 °C, and 30.53 MJ/kg for pyrolysis products at 600 °C. Higher carbon content was observed for materials obtained by fast pyrolysis conducted at higher temperatures.


Sign in / Sign up

Export Citation Format

Share Document