Abbreviations
- A:
-
hemicellulose
- A i :
-
frequency factor for rate constantk i, min−1
- B:
-
xylose and soluble xylose oligomer
- C:
-
decomposed product
- CA, CAF, CAS, CAo, CAFo, CASo :
-
concentration of xylan as a xylose
- CB, CBF, CBS :
-
concentration of xylose
- CHo :
-
(total xylan as a xylose)/(total liquid volume)
- CP :
-
average product concentration, w/v%
- dcw :
-
the density of crystalline wood, 1.54 g/mL
- E i :
-
activation energy for rate constantk i
- f:
-
τ1/τ1
- HF, Hs :
-
the fraction of fast and slow hemicellulose
- k i :
-
reaction rate constant, min−1
- L :
-
reactor length, cm
- N i :
-
acid concentration exponent
- R :
-
universal gas constant
- SB, SBF, SBS :
-
CB/CAo, CBF/CAFo, CBS/CASo
- t:
-
time, min
References
Lee, Y. Y. et al., (1978),Biotechnology & Bioengineering Symposium, No. 8, 75.
Limbaugh, M. L. (1980), M.S. Thesis, Auburn University, AL.
Cahela, D. R. and Lee, Y. Y. (1983),Biotechnol. Bioeng. 25, 3.
Veeraraghaven, S. et al. (1982). “Kinetic Modeling and Reactor Development for Hemicellulose Hydrolysis,” presented at AIChE National Meeting, Orlando, FL, February.
Kobayashi, T. and Sakai, Y. (1956),Bull. Agr. Chem. Soc. Japan 20, No. 1, 1.
Oshima, M. (1965), “Wood Chemistry, Processing Engineering Aspect,” Noyes Development Corporation, New York.
Conner, A. H. (1984),Wood and Fiber Sci. 16(2), 268.
Maloney, M. T. et al. (1985),Biotechnol. Bioeng. 27, 355.
Grohmann, K., Torget, R., and Himmel, M. (1985),Biotech. Bioeng. Symposium,15, 59.
Kim, S. B. (1986), Ph.D. Dissertation, Auburn University, AL.
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Kim, B.J., Lee, Y.Y. & Torget, R. An optimal temperature policy of percolation process as applied to dilute-acid hydrolysis of biphasic hemicellulose. Appl Biochem Biotechnol 39, 119–129 (1993). https://doi.org/10.1007/BF02918982
Issue Date:
DOI: https://doi.org/10.1007/BF02918982