Parametric study of pyrolysis and steam gasification of rice straw in presence of K2CO3

2016 ◽  
Vol 33 (9) ◽  
pp. 2567-2574 ◽  
Author(s):  
Humair Ahmed Baloch ◽  
Tianhua Yang ◽  
Haipeng Sun ◽  
Jie Li ◽  
Sabzoi Nizamuddin ◽  
...  
2016 ◽  
Vol 18 (4) ◽  
pp. 1031-1042 ◽  
Author(s):  
Humair Ahmed Baloch ◽  
Tianhua Yang ◽  
Rundong Li ◽  
Sabzoi Nizamuddin ◽  
Xingping Kai ◽  
...  

Fuel ◽  
2012 ◽  
Vol 93 ◽  
pp. 37-43 ◽  
Author(s):  
Kenji Murakami ◽  
Kengo Kasai ◽  
Takahiro Kato ◽  
Katsuyasu Sugawara

2011 ◽  
Vol 71-78 ◽  
pp. 2389-2395 ◽  
Author(s):  
Yuan Mou Wu ◽  
Jin Song Zhou ◽  
Zhong Yang Luo

Biomass oxygen-steam gasification associated with synthesis technology known as indirect biomass liquefaction is regarded as one of the most promising technologies of biomass utilization. In this paper, a comprehensive gasification model was developed for the simulation of rice straw oxygen-steam gasification using ASPEN PLUS. The gasification process was divided into two parts: pyrolysis and gasification. The RYield module was used to simulate the pyrolysis process with an external FORTURN program to calculate the pyrolysis products while the gasification process was calculated by the RCSTR module. With the help of the model, the gasification of rice straw was simulated under different residence time, different temperature and different amount of steam. The results showed that the proper residence time and temperature is 1.5s and 1300°C, respectively. The optimum amount of steam is steam/biomass=0.12 while the addition of oxygen is oxygen/biomass=0.2.


2012 ◽  
Vol 66 (7) ◽  
Author(s):  
Afsin Gungor ◽  
Murat Ozbayoglu ◽  
Cosku Kasnakoglu ◽  
Atilla Biyikoglu ◽  
Bekir Uysal

AbstractIn this parametric study, the effects of coal and oxidiser type, air-to-fuel ratio, steam-to-fuel ratio, reactor temperature, and pressure on H2 and CO amounts at the gasifier output, H2/CO, and higher heating value of the syngas produced have been calculated using a coal gasification model. Model simulations have been performed to identify the optimum values which are assumed to be 100 % for both cold gas efficiency and carbon conversion efficiency in the gasification process. From this study, it may be observed that the moisture content of the coal type is of crucial importance for the air gasification process; the O2 content of similar coals (taking into consideration the moisture and H2 content) is of significant importance for the air gasification process. When compared with air gasification, air-steam gasification becomes a more effective coal gasification method. The optimum working condition for air-steam gasification is to carry out the process at one atmosphere. High gasifier temperatures are not needed for the air-steam gasification of coal.


Author(s):  
Hong Nam Nguyen ◽  
Toshiki Tsubota

Abstract A complete parametric study of bagasse pellets under high-temperature steam gasification in relevant industrial operating conditions was investigated. Regarding thermal behaviors, the maximum rate of weight loss (Rmax = 0.55%/°C) occurred at the temperature Tmax = 305 °C. The final pyrolysis temperature and heating rate were proportional to the mechanical strength, the bulk density, as well as the char yield and energy yield. However, the changes were not significant after 600 °C. Regarding steam gasification kinetics, an increase from 850 to 1000 °C and from 0.1 to 0.4 atm accelerated 10 times and two times the conversion rate of bagasse pellet char, respectively. Gasification kinetics of a pellet char produced at 2000 °Cmin−1 was 1.4 higher compared with a pellet char produced at 5 °C min−1. An empirical model that takes into account all the changes in the reactive surface could successfully predict the conversion of the bagasse pellet char during high-temperature steam gasification. Experimental results and the kinetic model proposed could be useful for the calculation of industrial or academic codes, necessary for the conception of new efficient gasifiers.


1977 ◽  
Vol 27 (1) ◽  
pp. 93-98
Author(s):  
Naim A. Fadl ◽  
Magdi Z. Sefain ◽  
Mohomed Rakha
Keyword(s):  

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