Journal of Industrial and Engineering Chemistry, Vol.19, No.3, 938-943, May, 2013
Optimization the process variables for the fractionation of Saccharina japonica to enhance glucan content
E-mail:
Saccharina japonica was fractionated by dilute sulfuric acid to increase the glucan content. The optimal fractionation conditions were determined as follows: reaction temperature 141.14 ℃, reaction time 27.85 min and catalyst concentration 0.30%. The CCD model predicted 32.83% glucan content under these conditions. Experiments confirmed the maximum glucan content of 32.67% under the optimal reaction conditions, which was 4.7-fold higher than that of the raw S. japonica (6.95%). With the residual solid, an enzymatic digestibility of 89.38% was obtained using 15 FPU/g-glucan of cellulase enzyme loading, which was 2.6-fold higher than that of the raw S. japonica (34.85%).
- An HJ, Wilhelm WE, Searcy SW, Biomass Bioenerg., 35(9), 3763 (2011)
- Naik SN, Goud VV, Rout PK, Dalai AK, Renewable & Sustainable Energy Reviews., 14, 578 (2010)
- Demirbas MF, Appl. Energy, 88(10), 3473 (2011)
- Alvira P, Tomas-Pejo E, Ballesteros M, Negro MJ, Bioresour. Technol., 101(13), 4851 (2010)
- Nigam PS, Singh A, Progress in Energy and Combustion Science., 37, 52 (2011)
- Singh A, Nigam PS, Murphy JD, Bioresour. Technol., 102(1), 10 (2011)
- Goh CS, Lee KT, Renewable & Sustainable Energy Reviews., 14, 842 (2010)
- John RP, Anisha GS, Nampoothiri KM, Pandey A, Bioresour. Technol., 102(1), 186 (2011)
- Singh A, Olsen SI, Appl. Energy, 88(10), 3548 (2011)
- Sarkar N, Ghosh SK, Bannerjee S, Aikat K, Renewable Energy., 37, 19 (2012)
- Anastasakis K, Ross AB, Jones JM, Fuel, 90(2), 598 (2011)
- Borinesa MG, de Leonb RL, McHenryc MP, Renewable & Sustainable Energy Reviews., 15, 4432 (2011)
- Xu D, Gao ZQ, Zhang XW, Qi ZH, Meng CX, Zhuang ZM, Ye NH, Bioresour. Technol., 102(21), 9912 (2011)
- Jung KW, Kim DH, Shin HS, Bioresour. Technol., 102(3), 2745 (2011)
- Jung KW, Kim DH, Kim HW, Shin HS, International Journal of Hydrogen Energy., 36, 9626 (2011)
- Demirbas A, Energy Conv. Manag., 51(12), 2738 (2010)
- Lee SM, Lee JH, Bioresour. Technol., 102(10), 5962 (2011)
- Bae YJ, Ryu C, Jeon JK, Park J, Suh DJ, Suh YW, Chang D, Park YK, Bioresour. Technol., 102(3), 3512 (2011)
- Lee SM, Lee JH, J. Ind. Eng. Chem., 18(1), 16 (2012)
- Lee SM, Kim JH, Cho HY, Joo H, Lee JH, J. Korean Ind. Eng. Chem., 20(5), 517 (2009)
- Bezerra MA, Santelli RE, Oliveira EP, Villar LS, Escaleira LA, Talanta., 76, 965 (2008)
- Selig M, Weiss N, Ji Y, National Renewable Energy Laboratory, NREL/TP-510- 42629 (2008)
- Sluiter A, Hames B, Ruiz R, Scarlata C, Sluiter J, Templeton D, Crocker D, National Renewable Energy Laboratory, NREL/TP-510-42618 (2011)
- Hames B, Scarlata C, Sluiter A, National Renewable Energy Laboratory, NREL/TP- 510-42625 (2008)
- Sluiter A, Ruiz R, Scarlata C, Sluiter J, Templeton D, National Renewable Energy Laboratory, NREL/TP-510-42619 (2005)
- Sluiter A, Hames B, Ruiz R, Scarlata C, Sluiter J, Templeton D, National Renewable Energy Laboratory, NREL/TP-510-42622 (2008)
- Lee SM, Lee JH, Appl. Chem. Eng., 23(2), 164 (2012)