ZHOU Jingping, LIU Wei, YANG Chunyan, et al. Strengthening Nisin Production by Using the Coupling Technology of Foam Fractionation and Microcapsule Cells Immobilizing Two Strains Fermentation[J]. Science and Technology of Food Industry, 2021, 42(17): 179−186. (in Chinese with English abstract). doi: 10.13386/j.issn1002-0306.2020120101.
Citation: ZHOU Jingping, LIU Wei, YANG Chunyan, et al. Strengthening Nisin Production by Using the Coupling Technology of Foam Fractionation and Microcapsule Cells Immobilizing Two Strains Fermentation[J]. Science and Technology of Food Industry, 2021, 42(17): 179−186. (in Chinese with English abstract). doi: 10.13386/j.issn1002-0306.2020120101.

Strengthening Nisin Production by Using the Coupling Technology of Foam Fractionation and Microcapsule Cells Immobilizing Two Strains Fermentation

More Information
  • Received Date: December 13, 2020
  • Available Online: July 05, 2021
  • This work was aimed at strengthening Nisin production by coupling foam fractionation with microcapsule cells fermentation, in which Lactococcus lactis subsp.lactis (L.lactis) and Saccharomyces cerevisiae (S.cerevisiae) were co-cultivated to relieve the product inhibition from lactic acid. The concentrations of sodium alginate and chitosan were optimized to prepare liquid-core microcapsules for immobilizing L.lactis and S.cerevisiae. Results indicated that the Nisin titer in co-cultivation fermentation broth was as high as 3436.3 IU/mL by using lactose as carbon source and setting initial inoculation ratio of L.lactis and S.cerevisiae at 102:1. The optimal preparation conditions of sodium alginate/chitosan/sodium alginate (ACA) liquid-core microcapsules were sodium alginate concentration of 15 g/L and chitosan concentration of 5.5 g/L. Under the suitable conditions of foam fractionation coupled with microcapsule cells fermentation after cultivation for 21 h, pore diameter of gas distributor 180 μm and volumetric air flow rate 40 mL/min, the enrichment ration and recovery percentage of Nisin reached 5.8 and 63.1%, respectively. The total yield of Nisin in fermentation broth was 3973.2 IU/mL. The coupling technology of microcapsule cells immobilizing two strains fermentation and foam fractionation could effectively overcome the obstacles of product inhibition and strain cell loss, thus facilitating the high-density and continuous fermentation for Nisin production.
  • [1]
    Khan I, Oh D H. Integration of nisin into nanoparticles for application in foods[J]. Innovative Food Science & Emerging Technologies,2016,34:376−384.
    [2]
    Müller-Auffermann K, Grijalva F, Jacob F, et al. Nisin and its usage in breweries: A review and discussion[J]. Journal of the Institute of Brewing,2015,121(3):309−319. doi: 10.1002/jib.233
    [3]
    Punyauppa-path S, Phumkhachorn P, Rattanachaikunsopon P. Nisin: Production and mechanism of antimicrobial action[J]. International Journal of Current Research and Review,2015,7(2):47−54.
    [4]
    李海娜, 朱希强, 郭学平, 等. 复合诱变选育乳链菌肽高产菌株[J]. 中国生化药物杂质,2011,32(5):378−381. [Li H N, Zhu X Q, Guo X P, et al. Breeding of high-yield strain of nisin by compound mutation[J]. Chinese Journal of Biochemical Pharmaceutics,2011,32(5):378−381.
    [5]
    Jiang L, Liu Y, Yan G, et al. Aeration and fermentation strategies on nisin production[J]. Biotechnology Letters,2015,37(10):2039−2045. doi: 10.1007/s10529-015-1886-1
    [6]
    Pongtharangkul T, Demirci A. Effects of fed-batch fermentation and pH profiles on nisin production in suspended-cell and biofilm reactors[J]. Applied Microbiology and Biotechnology,2006,73(1):73−79. doi: 10.1007/s00253-006-0459-6
    [7]
    Desjardins P, Meghrous J, Lacroix C. Effect of aeration and dilution rate on nisin Z production during continuous fermentation with free and immobilized Lactococcuslactis UL719 in supplemented whey permeate[J]. International Dairy Journal,2001,11(11-12):943−951. doi: 10.1016/S0958-6946(01)00128-5
    [8]
    高艳飞, 吴兆亮, 胡楠, 等. 降低生产成本的葡萄糖部分代替蔗糖的乳链菌肽发酵工艺[J]. 中国食品添加剂,2016,4:127−132. [Gao Y F, Wu Z L, Hu N, et al. Fermentation technology of reducing production cost of nisin by using partial substitution of glucose for sucrose[J]. China Food Additives,2016,4:127−132. doi: 10.3969/j.issn.1006-2513.2016.03.013
    [9]
    Subha V, Quintoil M N, Porteen K, et al. Bacteriocin production by immobilized Lactobacillus casei in paneer whey is enhanced upon continuous fermentation[J]. Indian Veterinary Journal,2017,94(9):64−66.
    [10]
    Feldeková E, Solichová K, Horáčková Š, et al. The impact of l-lanthionine supplementation on the production of nisin by lactococci[J]. European Food Research and Technology,2020,246(4):845−851. doi: 10.1007/s00217-020-03449-4
    [11]
    Sun Z, Zhong J, Liang X, et al. Novel mechanism for nisin resistance via proteolytic degradation of nisin by the nisin resistance protein NSR[J]. Antimicrobial Agents and Chemotherapy,2009,53(5):1964−1973. doi: 10.1128/AAC.01382-08
    [12]
    陈艺强, 李光进, 金陈斌, 等. 高纯度Nisin的制备及工业生产条件的优化[J]. 食品工业科技,2017,38(11):281−284. [Chen Y Q, Li G J, Jin C B, et al. Preparation of high-purity Nisin and the optimization of industrial scale production conditions[J]. Science and Technology of Food Industry,2017,38(11):281−284.
    [13]
    Tolonen M, Saris P E J, Siika-aho M. Production of nisin with continuous adsorption to Amberlite XAD-4 resin using Lactococcuslactis N8 and L. lactis LAC48[J]. Applied Microbiology and Biotechnology,2004,63(6):659−665. doi: 10.1007/s00253-003-1413-5
    [14]
    Jozala A F, Lopes A M, de LencastreNovaes L C, et al. Aqueous two-phase micellar system for nisin extraction in the presence of electrolytes[J]. Food and Bioprocess Technology,2013,6(12):3456−3461. doi: 10.1007/s11947-012-1008-1
    [15]
    Tafreshi S Y H, Mirdamadi S, Khatami S. Comparison of different nisin separation and concentration methods: Industrial and cost-effective perspectives[J]. Probiotics and Antimicrobial Proteins,2020,12:1226−1234. doi: 10.1007/s12602-019-09607-9
    [16]
    Jia L, Zhou J, Cao J, et al. Foam fractionation for promoting rhamnolipids production by Pseudomonas aeruginosa D1 using animal fat hydrolysate as carbon source and its application in intensifying phytoremediation[J]. Chemical Engineering and Processing-Process Intensification,2020,158:108177−108187. doi: 10.1016/j.cep.2020.108177
    [17]
    Yi G, Liu Q, Lin J, et al. Repeated batch fermentation for surfactin production with immobilized Bacillus subtilis BS-37: Two-stage pH control and foam fractionation[J]. Journal of Chemical Technology & Biotechnology,2017,92:530−535.
    [18]
    Zhang D, Dong K, Xu D, et al. Process improvement for fermentation coupling with foam separation: A convenient strategy for cell recycle[J]. Asia-Pacific Journal of Chemical Engineering,2015,10:466−475. doi: 10.1002/apj.1893
    [19]
    Kawai M, Harada R, Yoda N, et al. Suppression of lactate production by using sucrose as a carbon source in lactic acid bacteria[J]. Journal of Bioscience and Bioengineering,2020,129:47−51. doi: 10.1016/j.jbiosc.2019.06.017
    [20]
    Kördikanlıoğlu B, Şimşek Ö, Saris P E. Nisin production of Lactococcuslactis N 8 with hemin-stimulated cell respiration in fed-batch fermentation system[J]. Biotechnology Progress,2015,31(3):678−685. doi: 10.1002/btpr.2075
    [21]
    Cheng Q, Shi X, Liu Y, et al. Production of nisin and lactic acid from corn stover through simultaneous saccharification and fermentation[J]. Biotechnology & Biotechnological Equipment,2018,32(2):420−426.
    [22]
    Aydoğan Ö, Bayraktar E, Mehmetoğlu Ü. Aqueous two-phase extraction of lactic acid: Optimization by response surface methodology[J]. Separation Science and Technology,2011,46(7):1164−1171. doi: 10.1080/01496395.2010.550270
    [23]
    Nam H G, Park K M, Lim S S, et al. Adsorption equilibria of succinic acid and lactic acid on amberchrom CG300C resin[J]. Journal of Chemical & Engineering Data,2011,56(3):464−471.
    [24]
    Wang L, York S W, Ingram L O, et al. Simultaneous fermentation of biomass-derived sugars to ethanol by a co-culture of an engineered Escherichia coli and Saccharomyces cerevisiae[J]. Bioresource Technology,2019,273:269−276. doi: 10.1016/j.biortech.2018.11.016
    [25]
    Hamedi J, Yazdiyan F. Enhancing of nisin production in a bioreactor by co-culture of Lactococcuslactis and Yarrowialipolytica[J]. Applied Biology,2019,31:21−32.
    [26]
    Cui X, Zhang D, Zheng H, et al. Study on the process of fermentation coupling with foam fractionation and membrane module for nisin production[J]. Asia-Pacific Journal of Chemical Engineering,2014,9:623−628.
    [27]
    Patel S K, Jeon M S, Gupta R K, et al. Hierarchical macroporous particles for efficient whole-cell immobilization: Application in bioconversion of greenhouse gases to methanol[J]. ACS Applied Materials & Interfaces,2019,11(21):18968−18977.
    [28]
    Gao Y, Zheng H, Hu N, et al. Technology of fermentation coupling with foam separation for improving the production of nisin using a κ-carrageenan with loofa sponges matrix and an hourglass-shaped column[J]. Biochemical Engineering Journal,2018,133:140−148. doi: 10.1016/j.bej.2018.02.008
    [29]
    Moreno-García J, García-Martínez T, Mauricio J C, et al. Yeast immobilization systems for alcoholic wine fermentations: Actual trends and future perspectives[J]. Frontiers in Microbiology,2018,9:241.
    [30]
    Hou D, Yu W, Zhang D, et al. Culture of yeast cells immobilized by alginate-chitosan microcapsules in aqueous-organic solvent biphasic system[J]. Journal of Oceanology and Limnology,2019,37(3):863−870. doi: 10.1007/s00343-019-8126-9
    [31]
    Liu W, Zhou J, Tan F, et al. Improvement of nisin production by using the integration strategy of co-cultivation fermentation, foam fractionation and pervaporation[J]. LWT,2021,142:1−9.
    [32]
    Zheng H, Zhang D, Guo K, et al. Online recovery of nisin during fermentation coupling with foam fractionation[J]. Journal of Food Engineering,2015,162:25−30. doi: 10.1016/j.jfoodeng.2015.04.006
    [33]
    Ariana M, Hamedi J. Enhanced production of nisin by co-culture of Lactococcuslactis sub sp. lactis and Yarrowialipolytica in molasses based medium[J]. Journal of Biotechnology,2017,256:21−26. doi: 10.1016/j.jbiotec.2017.07.009
    [34]
    Wu Z, Wang L, Jing Y, et al. Variable volume fed-batch fermentation for nisin production by Lactococcuslactis subsp. lactis W28[J]. Applied Biochemistry and Biotechnology,2009,152(3):372−382. doi: 10.1007/s12010-008-8335-8
    [35]
    张倩雯, 王春霞, 杨丽芸, 等. 影响酿酒酵母发酵过程的因素分析[J]. 中国酿造,2015,34(12):14−19. [Zhang Q W, Wang C X, Yang L Y, et al. Analysis of factors affecting the fermentation process of Saccharomyces Cerevisiae[J]. China Brewing,2015,34(12):14−19. doi: 10.11882/j.issn.0254-5071.2015.12.004
    [36]
    Palma M, Guerreiro J F, Sá-Correia I. Adaptive response and tolerance to acetic acid in Saccharomyces cerevisiae and Zygosaccharomyces bailii: A physiological genomics perspective[J]. Frontiers in Microbiology,2018,9:1−16. doi: 10.3389/fmicb.2018.00001
    [37]
    Stadie J, Gulitz A, Ehrmann M A, et al. Metabolic activity and symbiotic interactions of lactic acid bacteria and yeasts isolated from water kefir[J]. Food Microbiology,2013,35(2):92−98. doi: 10.1016/j.fm.2013.03.009
    [38]
    Zou J, Guo X, Shen T, et al. Construction of lactose-consuming Saccharomyces cerevisiae for lactose fermentation into ethanol fuel[J]. Journal of Industrial Microbiology and Biotechnology,2013,40(3-4):353−363. doi: 10.1007/s10295-012-1227-5
    [39]
    Lu D, Zhang Y, Niu S, et al. Study of phenol biodegradation using Bacillus amyloliquefaciens strain WJDB-1 immobilized in alginate–chitosan–alginate (ACA) microcapsules by electrochemical method[J]. Biodegradation,2012,23(2):209−219. doi: 10.1007/s10532-011-9500-2
    [40]
    Liu W, Wu Z, Wang Y, et al. Rhamnolipid assisted recovery of lycopene from the tomato-based processing wastewater using foam fractionation[J]. Journal of Food Engineering,2015,164:63−69. doi: 10.1016/j.jfoodeng.2015.04.024
    [41]
    Hofmann A, Schembecker G, Merz J. Role of bubble size for the performance of continuous foam fractionation in stripping mode[J]. Colloids and Surfaces A: Physicochemical and Engineering Aspects,2015,473:85−94.
    [42]
    Boonyasuwat S, Chavadej S, Malakul P, et al. Surfactant recovery from water using a multistage foam fractionator: Part I effects of air flow rate, foam height, feed flow rate and number of stages[J]. Separation Science and Technology,2005,40(9):1835−1853. doi: 10.1081/SS-200064595

Catalog

    Article Metrics

    Article views (302) PDF downloads (21) Cited by()

    /

    DownLoad:  Full-Size Img  PowerPoint
    Return
    Return