In this paper kinetics of xylose dehydration into furfural using acetic acid as catalystwas studied comprehensively and systematically. The reaction order of both furfural and xylose dehydration was determined and the reaction activation energy was obtained by nonlinear regression. The effect of acetic acid concentration was also investigated. Reaction rate constants were gained. Reaction rate constant of xylose dehydration is k
1
= 4.189×10
10
[A
]
0.1676
exp (-(108.6×1000)/(RT))
reaction rate constant of furfural degradation is k
2
=1.271×10
4
[A
]
0.1375
exp (-(63.413×1000)/(RT)) and reaction rate constant of condensation reaction is k
3
=3.4051×10
10
[A
]
0.1676
exp(-(104.99×1000)/(RT)) . Based on this
the kinetics equation of xylose dehydration into furfural in acetic acid was set up according to theory of Dunlop and Furfural generating rate equation is [d[F
]]
/[dt
]
= k
1
[X
]
0
e
-k
1
t
-k
2
[F
]
-k
3
[X
]
0
e
-k
1
t
[F
]
.
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references
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Acetic acid- and furfural-based adaptive evolution of Saccharomyces cerevisiae strains for improving stress tolerance and lignocellulosic ethanol production
High-performance 19-channel monolithic CHA zeolite membranes for vapor-permeation dehydration of acetic acid
Steam reforming of acetic acid over Ni/biochar of low metal-loading: Involvement of biochar in tailoring reaction intermediates renders superior catalytic performance
Enhanced bimetallic CuCo nanoparticles on nitrogen-doped carbon for selective hydrogenation of furfural to furfuryl alcohol through strong electronic interactions
Immobilization of trophic anaerobic acetogen for semi-continuous syngas fermentation
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