共查询到19条相似文献,搜索用时 171 毫秒
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分析比较了酸热法、二甲基亚砜法、细胞自溶法、高压均质法及酶促法对锁掷酵母的破壁效果,及对类胡萝卜素提取率的影响。结果表明,与其他4种破壁方法相比,高压均质法具有破壁效果好(破壁率达72.4%)、类胡萝卜素提取率高(67.3%)、破壁时间短、工艺简单、安全无污染等优点。通过均质压力、均质次数和菌液浓度这3个因素对高压均质法进行工艺优化,发现均质压力80 MPa、均质3次、菌液浓度为8%时,细胞破壁及类胡萝卜素提取效果最佳,分别是78.3%和82.5%。该研究结果为锁掷酵母的开发利用及类胡萝卜素的提取提供了理论依据及技术支持。 相似文献
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分析比较了酸热法、二甲基亚砜法、细胞自溶法、高压均质法及酶促法对锁掷酵母的破壁效果,及对类胡萝卜素提取率的影响。结果表明,与其他4种破壁方法相比,高压均质法具有破壁效果好(破壁率达72.4%)、类胡萝卜素提取率高(67.3%)、破壁时间短、工艺简单、安全无污染等优点。通过均质压力、均质次数和菌液浓度这3个因素对高压均质法进行工艺优化,发现均质压力80 MPa、均质3次、菌液浓度为8%时,细胞破壁及类胡萝卜素提取效果最佳,分别是78.3%和82.5%。该研究结果为锁掷酵母的开发利用及类胡萝卜素的提取提供了理论依据及技术支持。 相似文献
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从啤酒酵母中提取RNA新工艺的研究 总被引:8,自引:4,他引:4
研究了从啤酒酵母中提取RNA的新生产工艺,即在均质法和氨解法的基础上,将两者结合为均质- 氨解法。得出最佳工艺条件:酵母浓度10%,均质破壁循环2次,氨浓度0.6%,三氯乙酸浓度4%,提取30min。将上清液循环回用,RNA平均净得率>3%,第3次循环时净得率最高。 相似文献
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Bulent Keskinler Elif Erhan Galip Akay Mukerren Kaya & Betul Bayguven 《International Journal of Food Science & Technology》2004,39(1):71-78
Soluble whey proteins (WPs), adsorbed on yeast cells, were recovered by a crossflow microfiltration (MF) technique using a cellulose nitrate membrane with a pore size of 0.45 μm. The crossflow velocity was 1.5 m s?1 with a transmembrane pressure of 200 kPa at 25 °C. A series of protein rejections occured at various pH values ranging from 2 to 8. WPs adsorbed more on to yeast cells at low pH (pH < 4) than at high pH values, probably because they were positively charged at low pH. It was also shown that permeate flux increased and Modified Membrane Fouling Index values decreased at low pH levels. When the yeast concentration was 50 g L?1, the flux decreased five times compared with that in the absence of yeast. Protein recovery increased with increasing yeast concentrations. The highest protein recovery was found to be 85% at a yeast concentration of 50 g L?1 at a steady state flux rate of 10?6 m s?1 at 25 °C. When diluted solutions of whey were used, the same rejection of protein, adsorbed on yeast cells, was achieved at ten times lower amounts of yeast cells. This technique not only provides for the recovery of protein but also may give rise to the direct use of yeast cells, which are rich in protein, in the baking industry. WPs absorbed by yeast cells can be used to produce nutritionally rich products in areas where yeasts have been already used. 相似文献
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Characteristics of yeast growth and ethanol fermentation were examined in membrane bioreactor using a grape juice. After inoculation, batch fermentation was carried out for 24 h. When yeast growth reached the stationary phase, continuous fermentation was initiated. In continuous fermentation, a linear relationship was observed between cell concentration and dilution rate. In single-vessel membrane bioreactor, the cell concentrations of 18.7 g/l and 76.9 g/l (15 and 60 times higher than that of the batch fermentation, respectively) were observed at dilution rates of 0.1 h(-1) and 0.3 h(-1), respectively. The residual sugar concentration was higher than 10 g/l at the dilution rate of 0.1 h(-1), 0.2 h(-1) or 0.3 h(-1), therefore the single-vessel membrane bioreactor was not suitable for producing dry wine (sugar concentration: 4 g/l or less). In the double-vessel membrane bioreactor, it is most suitable to set the recycle ratio at 0.15 for keeping the sugar concentration below 4 g/l. The productivity of dry wine in the double-vessel membrane bioreactor was 28 times higher than that in the batch fermentation. 相似文献
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Inês Portugal Susana C. Ribeiro Ana M.R.B. Xavier Filipe Centeno Pierre Strehaiano 《International Journal of Food Science & Technology》2011,46(2):284-289
Maloalcoholic fermentation (MAF) of grape must by Schizosaccharomyces pombe immobilised in calcium‐alginate double‐layer beads (ProMalic®) was studied in Erlenmeyer flasks and in a total recycle fixed‐bed reactor operating in batch mode. The reaction is pseudo‐first order with respect to l ‐malic acid and under similar conditions deacidification is faster in the recycle reactor. This was attributed to mass transfer limitations which were confirmed in the recycle reactor by studying the influence of yeast load on the rate of MAF. Mass transfer limitations are also responsible for the lower activation energy of fermentation with the immobilised yeast (67 ± 9 kJ mol?1) in comparison with the free cells (126 ± 19 kJ mol?1). Alcoholic fermentation and MAF were performed simultaneously, both in the recycle reactor and in the industrial trials, confirming the efficacy of immobilised S. pombe to reduce grape must acidity without interfering with the main fermentation. Altogether, the present results are useful for the scale‐up of a recycle reactor to process large volumes of grape must. 相似文献
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Hiroto Kondo Hideko Yomo Susumu Furukubo Nobuyuki Fukui Kazuo Nakatani Yasutsugu Kawasaki 《Journal of the Institute of Brewing》1999,105(5):293-300
Proteinase A, excreted from yeast cells into beer during fermentation in the brewing process, has been shown to degrade foam-active proteins and to decrease foam stability. In order to improve the measurement of this enzyme in beer, a new fluorescent peptide, MOCAc-Ala-Pro-Ala-Lys-Phe-Phe-Arg-Leu-Lys (Dnp)-NH2, was synthesised and applied to the accurate and rapid estimation of proteinase A in commercial beer and fermenting wort. This novel substrate is several hundred times more sensitive to proteinase A than other previously reported synthetic substrates or native protein substrates. The concentration of proteinase A in beer is closely related to foam stability and proteinase A activity was found to increase gradually during fermentation. The concentration of proteinase A excreted from yeast cells is also closely related to the vitality of pitching yeast cells. This new method was successfully applied to the evaluation of yeast vitality and the development of optimum yeast handling procedures. 相似文献
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