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Whole cell biocatalysis in the presence of supercritical and compressed solvents.

机译:在超临界和压缩溶剂存在下的全细胞生物催化。

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Supercritical fluids have successfully mimicked organic solvents as media for non-traditional biocatalysis using enzyme preparations. However, the use of compressed fluid technology for whole cell biocatalysis, including extractive fermentations, has lagged the technologies developed in organic solvents. This is largely due to the choice of compressed solvent, supercritical carbon dioxide, which has been demonstrated to inhibit cellular metabolism and growth. This work investigates the potential of compressed hydrocarbons for the in situ extraction of volatile fermentation products.; The anaerobic, thermophilic bacterium, Clostridium thermocellum , is of interest since it can convert biomass feedstocks directly to ethanol. However, C. thermocellum is limited by low ethanol concentrations; hence, a method of in situ product removal may be necessary to increase productivity. Furthermore, organic acid formation tends to reduce ethanol yields. This work demonstrates for the first time, fermentation using whole cells in the presence of compressed hydrocarbons. This success suggests the feasibility of compressed solvents for extractive fermentation to remove ethanol and reduce product inhibition.; The ability of a traditional measure of solvent biocompatibility, the octanol-water partition coefficient (log P), to describe the reduced metabolic activity of C. thermocellum in the presence of compressed solvents was examined. The log P was extended to elevated temperatures and pressures for the purpose of correlating metabolic activities. Using the Group Contribution Associating-Equation of State, the log P values for various compressed solvents were calculated. Results indicate that log P is not capable of describing biocompatibility with compressed solvents or with the phase change of the extractive solvent.; Organic solvents have been used to induce shifts in product selectivity with whole cells and enzymes. This work shows product selectivity shifts in resting cells due to hydrostatic pressure or the presence of compressed solvents. Decreased lactate formation was hypothesized to be due to the inhibition of membrane transport proteins. Furthermore, acetate inhibition by hydrostatic pressure may be caused by changes in the membrane structure or the thermodynamic sensitivity of end-product formation. This work suggests the potential for the manipulation of product selectivity of non-barophilic microorganisms using hydrostatic and hyperbaric pressure to enhance bioconversion rates and optimize desirable products.
机译:超临界流体已经成功地模仿了有机溶剂作为使用酶制剂进行非传统生物催化的介质。但是,将压缩流体技术用于包括提取发酵在内的全细胞生物催化技术落后于在有机溶剂中开发的技术。这主要是由于选择了压缩溶剂超临界二氧化碳,该物质已被证明可以抑制细胞的代谢和生长。这项工作研究了压缩烃对挥发性发酵产物的原位提取的潜力。厌氧,嗜热细菌 Clostridium thermocellum 很有趣,因为它可以将生物质原料直接转化为乙醇。但是, C。低浓度的乙醇限制了热纤维素的使用;因此,可能需要采用原位去除产品的方法来提高生产率。此外,有机酸的形成倾向于降低乙醇的产率。这项工作首次证明了在压缩烃存在下使用全细胞进行发酵。该成功表明压缩溶剂用于萃取发酵以除去乙醇并减少产物抑制的可行性。溶剂生物相容性的传统量度(辛醇-水分配系数,log P)具有描述C降低的代谢活性的能力。检查了在压缩溶剂存在下的热纤维素。为了使代谢活性相关,将log P扩展到升高的温度和压力。使用状态的基团贡献关联方程式,计算了各种压缩溶剂的log P值。结果表明,log P不能描述与压缩溶剂或萃取溶剂的相变的生物相容性。有机溶剂已被用于诱导全细胞和酶产物选择性的改变。这项工作表明由于静水压力或压缩溶剂的存在,静止池中产物的选择性转移。假定乳酸形成减少是由于膜转运蛋白的抑制。此外,流体静压力对乙酸盐的抑制作用可能是由膜结构的变化或最终产物形成的热力学敏感性引起的。这项工作表明了利用静水压力和高压来操纵非嗜碱性微生物的产物选择性的潜力,以提高生物转化率并优化所需产物。

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