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(WFRF:(Leion Henrik 1976 )) srt2:(2020-2024)
 

Sökning: (WFRF:(Leion Henrik 1976 )) srt2:(2020-2024) > Modelling of gas co...

Modelling of gas conversion with an analytical reactor model for biomass chemical looping combustion (bio-CLC) of solid fuels

Mei, Daofeng, 1986 (författare)
Chalmers tekniska högskola,Chalmers University of Technology,Chalmers University of Technology, Sweden
Soleimani Salim, Amir H, 1985 (författare)
Chalmers tekniska högskola,Chalmers University of Technology
Lyngfelt, Anders, 1955 (författare)
Chalmers tekniska högskola,Chalmers University of Technology,Chalmers University of Technology, Sweden
visa fler...
Leion, Henrik, 1976 (författare)
Chalmers tekniska högskola,Chalmers University of Technology,Chalmers University of Technology, Sweden
Linderholm, Carl Johan, 1976 (författare)
Chalmers tekniska högskola,Chalmers University of Technology,Chalmers University of Technology, Sweden
Mattisson, Tobias, 1970 (författare)
Chalmers tekniska högskola,Chalmers University of Technology,Chalmers University of Technology, Sweden
Soleimanisalim, Amir H (författare)
Chalmers University of Technology, Sweden
visa färre...
 (creator_code:org_t)
Elsevier BV, 2022
2022
Engelska.
Ingår i: Chemical Engineering Journal. - : Elsevier BV. - 1385-8947 .- 1873-3212. ; 433
  • Tidskriftsartikel (refereegranskat)
Abstract Ämnesord
Stäng  
  • Manganese ores are promising oxygen carriers for chemical looping combustion (CLC), due to their high reactivity with combustible gases. In this work, a manganese ore called EB (Elwaleed B, originating from Egypt) is studied for its reaction rate with CH4, CO and H2 and the data are used in an analytically solved reactor model. The reactivity of fresh and three used EB samples from previous operation in a 10 kWth pilot was examined in a batch fluidized bed reactor with CH4 and syngas (50%CO + 50%H2). In comparison with other manganese ores, the EB ore has a lower rate of reaction with CH4, while showing a significantly higher reactivity with syngas. Nevertheless, this manganese ore always presents a better conversion of CH4 and syngas than the benchmark ilmenite. Mass-based reaction rate constants were obtained using a pseudo first-order reaction mechanism: 1.1·10-4 m3/(kg·s) for CH4, 6.6·10-3 m3/(kg·s) for CO and 7.5·10-3 m3/(kg·s) for H2. These rate constants were used in an analytical reactor model to further investigate results from previous operation in the 10 kWth unit. According to the analytical model, in the 10 kWth operation, 98% of the char in the biomass fuels was gasified before leaving the fuel reactor, while the char gasification products (CO and H2) have a 90% contact efficiency with the bed material. On the contrary, the volatiles have a much lower contact efficiency with the oxygen carrier bed, i.e. 20%, leading to low conversion of volatiles released. Thus, the results emphasize the importance of improving the contact between volatiles and bed material in order to promote combustion performance in the CLC process.

Ämnesord

TEKNIK OCH TEKNOLOGIER  -- Maskinteknik -- Energiteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Mechanical Engineering -- Energy Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Kemiteknik -- Kemiska processer (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering -- Chemical Process Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Industriell bioteknik -- Bioenergi (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Industrial Biotechnology -- Bioenergy (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Maskinteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Mechanical Engineering (hsv//eng)

Nyckelord

Manganese ore
Chemical looping combustion
Bio-CLC
CO capture 2
Biomass fuel
Analytical model

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