Slow pyrolysis of bio-oil and studies on chemical and physical properties of the resulting new bio-carbon

2018 ◽  
Vol 172 ◽  
pp. 2748-2758 ◽  
Author(s):  
Stefanie Arnold ◽  
Arturo Rodriguez-Uribe ◽  
Manjusri Misra ◽  
Amar K. Mohanty
Author(s):  
Muhammad Shahbaz ◽  
Ahmed AlNouss ◽  
Prakash Parthasarathy ◽  
Ali H. Abdelaal ◽  
Hamish Mackey ◽  
...  

Abstract Prior information on the pyrolysis product behaviour of biomass components-cellulose, hemicellulose and lignin is critical in the selection of feedstock as components have a significant influence on the pyrolysis products yield. In this study, the effect of biomass components on the yield of slow pyrolysis products (char, bio-oil and syngas) is investigated using a validated ASPEN Plus® model. The model is simulated at a temperature of 450 °C, a heating rate of 10 °C/min and a solid residence time of 30 min. The results indicated that at the given conditions, lignin contributed 2.4 and 2.5 times more char yield than cellulose and hemicellulose. The hemicellulose contributed 1.33 times more syngas yield than lignin while the cellulose and hemicellulose contributed 8.67 times more bio-oil yield than lignin. Moreover, the cost involved in the production of char using lignin (110 $/ton) is significantly economical than using cellulose (285 $/ton) and hemicellulose (296 $/ton). The net CO2 emission of lignin pyrolysis is 4.14 times lower than cellulose pyrolysis and 3.94 times lower than hemicellulose pyrolysis. It can be concluded that lignin pyrolysis is more advantageous than cellulose and hemicellulose pyrolysis. In the selection of feedstock for the slow pyrolysis, the feedstock with more lignin content is preferred. Graphical abstract


2016 ◽  
Vol 220 ◽  
pp. 378-383 ◽  
Author(s):  
Yan Yue ◽  
Qimei Lin ◽  
Muhammad Irfan ◽  
Qun Chen ◽  
Xiaorong Zhao
Keyword(s):  

2011 ◽  
Vol 102 (2) ◽  
pp. 1928-1932 ◽  
Author(s):  
Shuangning Xiu ◽  
Abolghasem Shahbazi ◽  
Vestel B. Shirley ◽  
Lijun Wang

2017 ◽  
Vol 5 (4) ◽  
pp. 4051-4063 ◽  
Author(s):  
Kotaiah Naik Dhanavath ◽  
Kalpit Shah ◽  
Satyavathi Bankupalli ◽  
Suresh K. Bhargava ◽  
Rajarathinam Parthasarathy

Author(s):  
Stefano Cordiner ◽  
Alessandro Manni ◽  
Vincenzo Mulone ◽  
Vittorio Rocco

Purpose Thermochemical conversion processes are one of the possible solutions for the flexible production of electric and thermal power from biomass. The pyrolysis degradation process presents, among the others, the interesting features of biofuels and high energy density bio-oil production potential high conversion rate. In this paper, numerical results of a slow batch and continuous fast pyrolyzers, are presented, aiming at validating both a tridimensional computational fluid dynamics-discrete element method (CFD–DEM) and a monodimensional distributed activation energy model (DAEM) represents with data collected in dedicated experiments. The purpose of this paper is then to provide reliable models for industrial scale-up and direct design purposes. Design/methodology/approach The slow pyrolysis experimental system, a batch of small-scale constant-pressure bomb for allothermic conversion processes, is presented. A DEM numerical model has been implemented by means of a modified OpenFOAM solver. The fast pyrolysis experimental system and a lab scale screw reactor designed for biomass fast pyrolysis conversion are also presented along with a 1D numerical model to represent its operation. The model which is developed for continuous stationary feeding conditions and based on a four-parallel reaction chemical framework is presented in detail. Findings The slow pyrolysis numerical results are compared with experimental data in terms of both gaseous species production and reduction of the bed height showing good predictive capabilities. Fast pyrolysis numerical results have been compared to the experimental data obtained from the fast pyrolysis process of spruce wood pellet. The comparison shows that the chemical reaction modeling based on a Gaussian DAEM is capable of giving results in very good agreement with the bio-oil yield evaluated experimentally. Originality/value As general results of the proposed activities, a mixed experimental and numerical approach has demonstrated a very good potential in developing design tools for pyrolysis development.


2019 ◽  
Vol 123 ◽  
pp. 78-88 ◽  
Author(s):  
Raquel V.S. Silva ◽  
Vinícius B. Pereira ◽  
Karen T. Stelzer ◽  
Tamyres A. Almeida ◽  
Gilberto A. Romeiro ◽  
...  

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