Issue
Korean Chemical Engineering Research,
Vol.53, No.4, 417-424, 2015
2단 흐름형 침출공정에 의한 돼지감자 줄기의 전처리
Pretreatment of Helianthus tuberosus Residue by Two-Stage Flow Through Process
본 연구에서는 목질계 바이오매스인 돼지감자 줄기에 대한 전처리 공정을 수행하였다. 공정은 효소 당화 수율을 높이기 위하여 흐름형 침출 전처리 공정에 2단 전처리 공정으로 적용하였다. 전처리 용매로 암모니아수에 의한 탈 리그닌 효과와 황산 용액에 의한 헤미셀룰로오스의 분해가 효소당화 및 발효에 미치는 영향을 확인하였다. 암모니아수와 황산용액을 이용한 2단 전처리 공정을 수행하였다. 먼저 1단계 공정은 40분 동안 163.2 oC의 온도에서 암모니아수로 처리를 진행하였고 다음 2단계 공정은 169.7 oC에서 20분 동안 황산 용액으로 처리를 수행하여 물질수지를 구하였다. 그리고 앞의 공정과 반대의 순서로 황산 용액을 먼저 처리한 후 암모니아수를 처리한 2단 전처리 공정을 수행하였다. 이때 암모니아수를 먼저 처리한 공정에서 글루코오스 생산량은 30.7 g으로 72.4%의 수율이 나타났다. 반대로 황산 용액을 먼저 처리한 후 암모니아수를 처리한 2단 전처리 공정에서는 글루코오스 생산량이 20.9 g으로 49.3%의 수율을 보였다.
In this study, the pretreatment of Helianthus tuberosus residue had been performed. The two-stage pretreatment on flow-through process were applied in the interests of increase of sugar production yield on enzymatic saccharification. The delignification by aqueous ammonia and the fractionation of hemicellulose by sulfuric acid solution as pretreatment solution were confirmed for effects of enzymatic saccharification. Two-stage pretreatment process was performed using aqueous ammonia and sulfuric acid. The first step was performed with aqueous ammonia for 40 min at 163.2 oC and the second step was performed with sulfuric acid solution for 20 min at 169.7 oC. And then, the first step was performed with sulfuric acid solution and the second step was pretreated with aqueous ammonia. At this time, the glucose production was 30.7 g and the glucose yield was 72.4% in the first step process with aqueous ammonia. And, the glucose production was 20.9 g and the glucose yield was 49.3% in the first step process with sulfuric acid solution.
[References]
  1. Kim KH, Tucker M, Nguyen Q, Bioresour. Technol., 96, 1249, 2005
  2. Lynd LR, Wyman CE, Gerngross TU, Biotechnol. Prog., 15(5), 777, 1999
  3. Agbor VB, Cicek N, Sparling R, Berlin A, Levin DB, Biotechnol. Adv., 29, 675, 2011
  4. Kim TH, Lee YY, Appl. Biochem. Biotechnol., 121-124, 1119, 2005
  5. Holtzapple MT, Lundeen JE, Sturgis R, Appl. Biochem. Biotechnol., 34-35, 5, 1992
  6. Kim TH, Taylor F, Hicks KB, Bioresour. Technol., 99(13), 5694, 2008
  7. Kim TH, Lee YY, Bioresour. Technol., 97(2), 224, 2006
  8. Kim TH, Lee YY, Appl. Biochem. Biotechnol., 136-140, 81, 2007
  9. Iyer PV, Wu ZW, Kim SB, Lee YY, Appl. Biochem. Biotechnol., 57-58, 121, 1996
  10. VONSIVERS M, ZACCHI G, Bioresour. Technol., 51(1), 43, 1995
  11. Mackie KL, Brownell HH, West KL, Saddler JN, J. Wood Chem. Technol., 5, 405, 1985
  12. Kim JW, Kim KS, Lee JS, Park SM, Cho HY, Park JC, Kim JS, Bioresour. Technol., 102(19), 8992, 2011
  13. Ghose TK, Pure Appl. Chem., 59(2), 257, 1987
  14. Adney B, Baker J, “Measurement of Cellulase Activities,” NREL(2008).
  15. Park YC, Kim JS, Energy, 47(1), 31, 2012
  16. Kim KS, Kim JS, Korean Chem. Eng. Res., 48(6), 704, 2010
  17. Kim TH, Kim JS, Sunwoo C, Lee YY, Bioresour. Technol., 90(1), 39, 2003
  18. Kim TH, Korean J. Chem. Eng., 28(11), 2156, 2011
  19. Murai T, Yoshino T, Ueda M, Haranoya I, Ashikari T, Yoshizumi H, Tanaka A, J. Ferment. Bioeng., 86(6), 569, 1998
  20. National Renewable Energy Laboratory, Standard Biomass Analytical Procedures, http://www.nrel.gov/biomass/analytical_procedures.html
  21. Park YC, Kim JS, Korean Chem. Eng. Res., 49(4), 470, 2011