Semi-continuous feeding and gasification of alfalfa and wheat straw pellets in a lab-scale fluidized bed reactor
•Alfalfa and wheat straw pellets were gasified in a lab-scale fluid-bed reactor.•ER varied between 0.20 and 0.35 at which several parameters investigated.•ER=0.35 was found optimum for alfalfa at which process performance improved.•ER=0.30 revealed optimum for wheat straw at which gasification was e...
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| Published in | Energy conversion and management Vol. 99; pp. 50 - 61 |
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| Main Authors | , , |
| Format | Journal Article |
| Language | English |
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Elsevier Ltd
15.07.2015
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| Abstract | •Alfalfa and wheat straw pellets were gasified in a lab-scale fluid-bed reactor.•ER varied between 0.20 and 0.35 at which several parameters investigated.•ER=0.35 was found optimum for alfalfa at which process performance improved.•ER=0.30 revealed optimum for wheat straw at which gasification was effective.
Small scale air-blown fluidized bed gasification of alfalfa and wheat straw pellets were conducted for semi-continuous solid feeding and range of operating conditions varied due to the modifications in equivalence ratio (ER) (0.20–0.35) achieved both by varying solid and air input. Alfalfa pellets displayed an improvement in several gasification variables such as gas lower heating value (∼4.1MJ/Nm3), specific gas yield (1.66Nm3/kg), cold gas efficiency (∼42%) and carbon conversion efficiency (∼72%) as ER maximized to 0.35 which was found optimum for this feedstock for the present course of experiments. Gasification parameters of wheat straw pellets on the other hand were characterized by a great degree of variation as the ER progressively increased. The optimum performance of this biomass was likely to achieve at ER=0.30 when gas lower heating value and cold gas efficiency maximized to ∼4MJ/Nm3 and ∼37% respectively. Moreover, a substantial drop in tar yield (58.7g/Nm3) at this ER was also indicative to the optimal thermal conversion at this point of operation. Overall, both the feedstocks presented promising alternatives for utilization into the small-scale fluidized bed gasification which is increasingly emerging as a sustainable solution towards processing lignocellulosic biomass. |
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| AbstractList | •Alfalfa and wheat straw pellets were gasified in a lab-scale fluid-bed reactor.•ER varied between 0.20 and 0.35 at which several parameters investigated.•ER=0.35 was found optimum for alfalfa at which process performance improved.•ER=0.30 revealed optimum for wheat straw at which gasification was effective.
Small scale air-blown fluidized bed gasification of alfalfa and wheat straw pellets were conducted for semi-continuous solid feeding and range of operating conditions varied due to the modifications in equivalence ratio (ER) (0.20–0.35) achieved both by varying solid and air input. Alfalfa pellets displayed an improvement in several gasification variables such as gas lower heating value (∼4.1MJ/Nm3), specific gas yield (1.66Nm3/kg), cold gas efficiency (∼42%) and carbon conversion efficiency (∼72%) as ER maximized to 0.35 which was found optimum for this feedstock for the present course of experiments. Gasification parameters of wheat straw pellets on the other hand were characterized by a great degree of variation as the ER progressively increased. The optimum performance of this biomass was likely to achieve at ER=0.30 when gas lower heating value and cold gas efficiency maximized to ∼4MJ/Nm3 and ∼37% respectively. Moreover, a substantial drop in tar yield (58.7g/Nm3) at this ER was also indicative to the optimal thermal conversion at this point of operation. Overall, both the feedstocks presented promising alternatives for utilization into the small-scale fluidized bed gasification which is increasingly emerging as a sustainable solution towards processing lignocellulosic biomass. Small scale air-blown fluidized bed gasification of alfalfa and wheat straw pellets were conducted for semi-continuous solid feeding and range of operating conditions varied due to the modifications in equivalence ratio (ER) (0.20-0.35) achieved both by varying solid and air input. Alfalfa pellets displayed an improvement in several gasification variables such as gas lower heating value (~4.1 MJ/Nm super(3)), specific gas yield (1.66 Nm super(3)/kg), cold gas efficiency (~42%) and carbon conversion efficiency (~72%) as ER maximized to 0.35 which was found optimum for this feedstock for the present course of experiments. Gasification parameters of wheat straw pellets on the other hand were characterized by a great degree of variation as the ER progressively increased. The optimum performance of this biomass was likely to achieve at ER = 0.30 when gas lower heating value and cold gas efficiency maximized to ~4 MJ/Nm super(3) and ~37% respectively. Moreover, a substantial drop in tar yield (58.7 g/Nm super(3)) at this ER was also indicative to the optimal thermal conversion at this point of operation. Overall, both the feedstocks presented promising alternatives for utilization into the small-scale fluidized bed gasification which is increasingly emerging as a sustainable solution towards processing lignocellulosic biomass. |
| Author | Arauzo, Jesús Nielsen, Henrik Kofoed Sarker, Shiplu |
| Author_xml | – sequence: 1 givenname: Shiplu surname: Sarker fullname: Sarker, Shiplu email: Shiplu.sarker@uia.no organization: University of Agder, Faculty of Engineering and Science, Jon Lilletuns vei 9, Service boks, 4898 Grimstad, Norway – sequence: 2 givenname: Jesús surname: Arauzo fullname: Arauzo, Jesús organization: University of Zaragoza, Thermochemical Process Group, Aaragon Institute of Engineering Research (I3A), I+D building, C/Mariano Esquillor s/n, E-50018 Zaragoza, Spain – sequence: 3 givenname: Henrik Kofoed surname: Nielsen fullname: Nielsen, Henrik Kofoed organization: University of Agder, Faculty of Engineering and Science, Jon Lilletuns vei 9, Service boks, 4898 Grimstad, Norway |
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| Title | Semi-continuous feeding and gasification of alfalfa and wheat straw pellets in a lab-scale fluidized bed reactor |
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