Enhancing bioethanol productivity by a yeast-immobilized catalytically active membrane in a fermentation-pervaporation coupling process

被引:26
作者
Cao, Zhongqi [1 ]
Xia, Chunjie [3 ]
Jia, Wei [4 ]
Qing, Weihua [2 ]
Zhang, Weidong [1 ]
机构
[1] Beijing Univ Chem Technol, Beijing Key Lab Membrane Sci & Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
[2] New Jersey Inst Technol, John A Reif Jr Dept Civil & Environm Engn, Newark, NJ 07102 USA
[3] Southern Illinois Univ, Dept Civil & Environm Engn, Carbondale, IL USA
[4] City Univ Hong Kong, Sch Energy & Environm, Kowloon, Tat Chee Ave, Hong Kong, Peoples R China
关键词
Bioethanol production; Catalytic membrane; Yeast immobilization; Pervaporation membrane reactor; Fermentation; ETHANOL-PRODUCTION; CONVERSION ENHANCEMENT; RECOVERY; SEPARATION; ACID; ESTERIFICATION; REMOVAL; PERFORMANCE; FABRICATION; TOLERANCE;
D O I
10.1016/j.memsci.2019.117485
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Bioethanol is a promising substitute for fossil fuels and is mainly produced through yeast fermentation. However, in conventional batch fermentation process extracellular ethanol accumulation restricts yeast excretion of intracellular ethanol, and results in suppressed yeast viability and ethanol productivity. The present study reports a yeast-immobilized catalytically active membrane for efficient extracellular ethanol removal towards enhanced bioethanol productivity in pervaporation membrane reactor. The membrane was fabricated by immersion phase inversion through coating a porous yeast/polyethersulfone catalytic layer on a polydimethylsiloxane (PDMS) pervaporation membrane. Benefited from the high porosity of biocatalytic layer, the immobilized yeast exhibited superior fermentation capacity in high substrate concentration when compared with free yeasts. Most importantly, by comparing the fermentation performances in catalytically active membrane reactor (CAMR), inert membrane reactor and batch reactor, CAMR exhibited the highest ethanol productivity (3.05 g L-1 h(-1)) and yeast mass concentration (26.41 g L-1), indicating a superior yeast growth rate and viability in CAMR. We attribute this to a "genuine" in situ removal ability of the bio-catalytically active membrane: the extracellular ethanol was promptly removed from the vicinity of the yeast, promoting a more rapid excretion of the inhibitor (intracellular ethanol) and thus maximally eliminated undesirable inhibition of the intracellular ethanol.
引用
收藏
页数:9
相关论文
共 55 条
  • [1] Second generation bioethanol production: A critical review
    Aditiya, H. B.
    Mahlia, T. M. I.
    Chong, W. T.
    Nur, Hadi
    Sebayang, A. H.
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2016, 66 : 631 - 653
  • [2] Permeability, permeance and selectivity: A preferred way of reporting pervaporation performance data
    Baker, Richard W.
    Wijmans, J. G.
    Huang, Yu
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2010, 348 (1-2) : 346 - 352
  • [3] Influence of magnesium ions on heat shock and ethanol stress responses of Saccharomyces cerevisiae
    Birch, RM
    Walker, GM
    [J]. ENZYME AND MICROBIAL TECHNOLOGY, 2000, 26 (9-10) : 678 - 687
  • [4] Effects of yeast immobilization on bioethanol production
    Borovikova, Diana
    Scherbaka, Rita
    Patmalnieks, Aloizijs
    Rapoport, Alexander
    [J]. BIOTECHNOLOGY AND APPLIED BIOCHEMISTRY, 2014, 61 (01) : 33 - 39
  • [5] Castellar MR, 1998, J CHEM TECHNOL BIOT, V73, P377, DOI 10.1002/(SICI)1097-4660(199812)73:4<377::AID-JCTB973>3.0.CO
  • [6] 2-I
  • [7] PVA composite catalytic membranes for hyacinth flavour synthesis in a pervaporation membrane reactor
    Ceia, T. F.
    Silva, A. G.
    Ribeiro, C. S.
    Pinto, J. V.
    Casimiro, M. H.
    Ramos, A. M.
    Vital, J.
    [J]. CATALYSIS TODAY, 2014, 236 : 98 - 107
  • [8] ETHANOL TOLERANCE OF YEAST
    DAMORE, T
    STEWART, GG
    [J]. ENZYME AND MICROBIAL TECHNOLOGY, 1987, 9 (06) : 322 - 330
  • [9] Production of bioethanol and other bio-based materials from sugarcane bagasse: Integration to conventional bioethanol production process
    Dias, Marina O. S.
    Ensinas, Adriano V.
    Nebra, Silvia A.
    Maciel Filho, Rubens
    Rossell, Carlos E. V.
    Wolf Maciel, Maria Regina
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (9A) : 1206 - 1216
  • [10] Application of hydrocyclone for removal of yeasts from alcohol fermentations broth
    Habibian, A.
    Pazouki, M.
    Ghanaie, H.
    Abbaspour-Sani, K.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2008, 138 (1-3) : 30 - 34