Cryoprotection of red blood cells by a 2,3-butanediol containing mainly the levo and dextro isomers.

A 2,3-butanediol containing 96.7% (w/w) racemic mixture of the levo and dextro isomers and only 3.1% (w/w) of the meso isomer (called 2,3-butanediol 97% dl) has been used for the cryoprotection of red blood cells. The erythrocytes were cooled to -196 degrees C at rates between 2 and 3500 degrees C/min, followed by slow or rapid warming. Up to 20% (w/w) of this polyalcohol, only the classical peak of survival is observed, as with up to 20% (w/w) 1,2-propanediol or 1,3-butanediol. Twenty percent 2,3-butanediol 97% dl can protect red blood cells very efficiently. The maximum survival, of 90%, as with 20% glycerol, is a little lower than with 20% 1,2-propanediol and higher than with 20% 1,3-butanediol. Fifteen percent 2,3-butanediol protects fewer red blood cells than 15% glycerol or 1,2-propanediol, with a maximum survival of about 80%. The best cryoprotection by 30% 2,3-butanediol 97% dl is obtained at the slowest cooling and warming rates, where survival approaches 90%. After a minimum, an increase of survival is observed at the fastest cooling rates, which would correspond to complete vitrification. These rates are lower than with 30%, 1,2-propanediol or 1,3-butanediol, in agreement with the higher glass-forming tendency of 2,3-butanediol 97% dl solutions. In agreement with the remarkable physical properties of its aqueous solutions, the present experiments also suggest that 2,3-butanediol containing mainly the levo and dextro isomers could be a very useful cryoprotectant for organ cryopreservation. However, it would perhaps be better to use it in combination with other cryoprotectants, since it is a little more toxic than glycerol or 1,2-propanediol at high concentrations.     

Fermentation of glycerol to 1,3-propanediol and 2,3-butanediol by Klebsiella pneumoniae

Klebsiella pneumoniae was shown to convert glycerol to 1,3-propanediol, 2,3-butanediol and ethanol under conditions of uncontrolled pH. Formation of 2,3-butanediol starts with some hours' delay and is accompanied by a reuse of the acetate that was formed in the first period. The fermentation was demonstrated in the type strain of K. pneumoniae, but growth was better with the more acid-tolerant strain GT1, which was isolated from nature. In continuous cultures in which the pH was lowered stepwise from 7.3 to 5.4, 2,3-butanediol formation started at pH 6.6 and reached a maximum yield at pH 5.5, whereas formation of acetate and ethanol declined in this pH range. 2,3-Butanediol and acetoin were also found among the products in chemostat cultures grown at pH 7 under conditions of glycerol excess but only with low yields. At any of the pH values tested, excess glycerol in the culture enhanced the butanediol yield. Both effects are seen as a consequence of product inhibition, the undissociated acid being a stronger trigger than the less toxic diols and acid anions. The possibilities for using the fermentation type described to produce 1,3-propanediol and 2,3-butanediol almost without by-products are discussed. Received: 4 February 1998 / Received revision: 30 March 1998 / Accepted: 13 April 1998     

Production of 2,3-butanediol by Klebsiella oxytoca

Summary High glucose concentrations result in high levels of 2,3-butanediol, improved yield and productivity, and a decrease in cell growth in batch cultures of Klebsiella oxytoca. A maximum of 84.2 g butanediol/l and a yield of 0.5 was obtained with an initial glucose concentration of 262.6g/l. Adding the substrate in two steps in a modified fed-batch operation resulted in 85.5 g butanediol/l, 6.4 g acetoin/l and 3.4 g ethanol/l with a net yield of 0.5. Increasing the cell density to 60g/l resulted in productivities as high as 3.22 g/l.h.     

Study of 2,3-butanediol formation by serratiamarcescens

Summary Serratia marcescens can be used for the fermentation of sugar for the formation of 2,3-butanediol. Presence of 1% calcium carbonate increases the formation of the diol and 0.292% of phosphate gives the maximum percentage yield of the diol. The optimumph for the formation of the diol has been found to be 7.     

High production of 2,3-butanediol from glycerol without 1,3-propanediol formation by Raoultella ornithinolytica B6

Applied Microbiology and Biotechnology - Conversion of crude glycerol derived from biodiesel processes to value-added chemicals has attracted much attention. Herein, Raoultella ornithinolytica B6...     

Present state and perspective of downstream processing of biologically produced 1,3-propanediol and 2,3-butanediol

1,3-Propanediol and 2,3-butanediol are two promising chemicals which have a wide range of applications and can be biologically produced. The separation of these diols from fermentation broth makes more than 50% of the total costs in their microbial production. This review summarizes the present state of methods studied for the recovery and purification of biologically produced diols, with particular emphasis on 1,3-propoanediol. Previous studies on the separation of 1,3-propanediol primarily include evaporation, distillation, membrane filtration, pervaporation, ion exchange chromatography, liquid–liquid extraction, and reactive extraction. Main methods for the recovery of 2,3-butanediol include steam stripping, pervaporation, and solvent extraction. No single method has proved to be simple and efficient, and improvements are especially needed with regard to yield, purity, and energy consumption. Perspectives for an improved downstream processing of biologically produced diols, especially 1,3-propanediol are discussed based on our own experience and recent work. It is argued that separation technologies such as aqueous two-phase extraction with short chain alcohols, pervaporation, reverse osmosis, and in situ extractive or pervaporative fermentations deserve more attention in the future.     

Assay of physiological levels of 2,3-butanediol diastereomers in blood and urine by gas chromatography-mass spectrometry

We present an assay for 2,3-butanediol by gas chromatography-mass spectrometry of its trimethylsilyl ethers. 2R,3R- and/or 2S,3S-2,3-butanediol and meso-2,3-butanediol are quantitated with corresponding internal standards of [2,3-2H2]butanediol. Limits of detection are 1 and 0.1 microM for split and splitless injections, respectively. Blood concentrations of 2,3-butanediol in nonalcoholics are 0.5 +/- 0.3 (SD) microM for 2R,3R- and/or 2S,3S-2,3-butanediol and 0.8 +/- 0.4 microM for meso-2,3-butanediol (n = 9). Two hours after alcohol ingestion, blood levels had risen in eight of nine subjects to 1.2 +/- 0.7 microM for 2R,3R-/2S,3S-2,3-butanediol and to 1.2 +/- 0.6 microM for meso-2,3-butanediol. Baseline urinary excretion of 2,3-butanediol is 0.4 +/- 0.2 mumol/mmol creatinine for 2R,3R-/2S,3S-2,3-butanediol and 0.9 +/- 0.5 mumol/mmol creatinine for meso-2,3-butanediol.     

Biological production of 2,3-butanediol

2,3-Butanediol (2,3-BDL), which is very important for a variety of chemical feedstocks and liquid fuels, can be derived from the bioconversion of natural resources. One of its well known applications is the formation of methyl ethyl ketone, by dehydration, which can be used as a liquid fuel additive. This article briefly reviews the basic properties of 2,3-BDL and the metabolic pathway for the microbial formation of 2,3-BDL. Both the biological production of 2,3-BDL and the variety of strains being used are introduced. Genetically improved strains for BDL production which follow either the original mechanisms or new mechanisms are also described. Studies on fermentation conditions are briefly reviewed. On-line analysis, modeling, and control of BDL fermentation are discussed. In addition, downstream recovery of 2,3-BDL and the integrated process (being important issues of BDL production) are also introduced.     

Lipase-catalyzed diacylation of 1,3-butanediol

Summary A kinetic resolution of 1,3-butanediol was accomplished by lipase-catalyzed enantioselective diacylations in organic solvent. Diacylation of 1,3-butanediol was carried out using immobilized lipase SP382 (from Candida sp.) to produce (R) -1,3-diacetoxybutane with 85.8% e.e.. And then, this optically active product was chemically hydrolyzed to diol, and re-acylated with lipase SP382 to (R) -1,3-diacetoxybutane with over 98% e.e..     

Stereospecificity of Corynebacterium glutamicum 2,3-butanediol dehydrogenase and implications for the stereochemical purity of bioproduced 2,3-butanediol

Applied Microbiology and Biotechnology - The stereochemistry of 2,3-butanediol (2,3-BD) synthesis in microbial fermentations is important for many applications. In this work, we showed that...     

生物法生产2,3-T二醇研究进展

2,3-丁二醇是一种重要的化工原料,可广泛应用于多个领域.二战期间由于合成橡胶需要大量1,3-丁二烯,2,3-丁二醇生产空前发展.近年来,由于聚对苯二甲酸丁烯树脂、γ-丁内酯,Spandex弹性纤维及其前体的需求增长,2,3-丁二醇的需求和产量也稳步增长.多年来,生物法生产2,3-丁二醇虽然得到了广泛的研究,但一直没有实现工业化.从产生2,3-丁二醇的菌种及2,3-丁二醇的生理意义、代谢途径、旋光异构体的形成机理、影响发酵的因素与产物的提纯等方面对生物法生产2,3-丁二醇进行了综述并提出了生物法生产2,3-丁二醇要解决的几个问题.     

Production of 2,3-butanediol by newly isolated Enterobacter cloacae

Enterobacter cloacae NRRL B-23289 was isolated from local decaying wood/corn soil samples while screening for microorganisms for conversion of l-arabinose to fuel ethanol. The major product of fermentation by the bacterium was meso-2,3-butanediol (2,3-BD). In a typical fermentation, a BD yield of 0.4 g/g arabinose was obtained with a corresponding productivity of 0.63 g/l per hour at an initial arabinose concentration of 50 g/l. The effects of initial arabinose concentration, temperature, pH, agitation, various monosaccharides, and multiple sugar mixtures on 2,3-BD production were investigated. BD productivity, yield, and byproduct formation were influenced significantly within these parameters. The bacterium utilized sugars from acid plus enzyme saccharified corn fiber and produced BD (0.35 g/g available sugars). It also produced BD from dilute acid pretreated corn fiber by simultaneous saccharification and fermentation (0.34 g/g theoretical sugars). Received: 17 December 1998 / Revision received: 9 March 1999 / Accepted: 20 March 1999     

Production of optically active 2,3-butanediol by Bacillus polymyxa

Bacillus polymyxa produces (R, R)-2,3-butanediol from a variety of carbohydrates. Other metabolites are also produced including acetoin, acetate, lactate, and ethanol. The excretion of each metabolite was found to depend on the relative availability of oxygen to the culture. When the relative oxygen uptake rate was high, enhanced yields of acetate and acetoin were noted. At an intermediate oxygen availability, the butanediol yield was maximal. When the availability of oxygen was more restricted, higher yields of lactate and ethanol occurred. The cells appeared to regulate themselves such that energy generation is optimal subject to the constraint that the cells do not produce more reducing equivalents than can be oxidized by the electron transport system. The dependence of each product yield on the relative oxygen availability was determined, and this knowledge was used to carry out a fed-batch fermentation that attained a final butanediol concentration of over 40 g/L in 50 h.     

生物法生产2,3-丁二醇研究进展

2,3-丁二醇是一种重要的化工原料,可广泛应用于多个领域。二战期间由于合成橡胶需要大量1,3-丁二烯,2,3-丁二醇生产空前发展。近年来,由于聚对苯二甲酸丁烯树脂、γ-丁内酯,Spandex弹性纤维及其前体的需求增长,2,3-丁二醇的需求和产量也稳步增长。多年来,生物法生产2,3-丁二醇虽然得到了广泛的研究,但一直没有实现工业化。本文从产生2,3-丁二醇的菌种及2,3-丁二醇的生理意义、代谢途径、旋光异构体的形成机理、影响发酵的因素与产物的提纯等方面对生物法生产2,3-丁二醇进行了综述并提出了生物法生产2,3-丁二醇要解决的几个问题。     

2，3-丁二醇的发酵及盐析分离工艺

采用克雷伯氏菌（Klebsiella pneumoniae CICC 10011）发酵生产2,3-丁二醇,并对2,3-丁二醇的盐析分离工艺进行了考察。通过实验确定了以葡萄糖为底物微氧批式流加发酵的条件,发酵液中2,3-丁二醇和3-羟基丁酮的质量浓度分别为90．98g/L和12．40g/L,2,3-丁二醇的摩尔转化率为82．7％,生产强度达到2．1g/（L·h）。对发酵液中2,3-丁二醇的盐析分离研究表明,K2HPO4和K3PO4对2,3-丁二醇的盐析效果优于K2CO3。当发酵液浓缩70％后,加入质量分数为45％的K,HPO4,2,3-丁二醇的分配系数达到9．10,回收率为79．37％;上相中2,3-丁二醇的质量浓度达到420g／L;此时3-羟基丁酮的分配系数和回收率分别为11．9和83．48％。     

Improved 1,3-propanediol production by engineering the 2,3-butanediol and formic acid pathways in integrative recombinant Klebsiella pneumoniae

In the biotechnological process, insufficient cofactor NADH and multiple by-products restrain the final titer of 1,3-propanediol (1,3-PD). In this study, 1,3-PD production was improved by engineering the 2,3-butanediol (2,3-BD) and formic acid pathways in integrative recombinant Klebsiella pneumoniae. The formation of 2,3-BD is catalysed by acetoin reductase (AR). An inactivation mutation of the AR in K. pneumoniae CF was generated by insertion of a formate dehydrogenase gene. Inactivation of AR and expression of formate dehydrogenase reduced 2,3-BD formation and improved 1,3-PD production. Fermentation results revealed that intracellular metabolic flux was redistributed pronouncedly. The yield of 1,3-PD reached 0.74 mol/mol glycerol in flask fermentation, which is higher than the theoretical yield. In 5 L fed-batch fermentation, the final titer and 1,3-PD yield of the K. pneumoniae CF strain reached 72.2 g/L and 0.569 mol/mol, respectively, which were 15.9% and 21.7% higher than those of the wild-type strain. The titers of 2,3-BD and formic acid decreased by 52.2% and 73.4%, respectively. By decreasing the concentration of all nonvolatile by-products and by increasing the availability of NADH, this study demonstrates an important strategy in the metabolic engineering of 1,3-PD production by integrative recombinant hosts.     

Separation of meso and racemic 2,3-butanediol by aqueous liquid chromatography

Fermentation of xylose by Klebsiella pneumoniae (ATCC 8724) producers meso and nonmeso 2,3-butaneodiol. The enzyme Kinetic of 2,3-butanediol stereoisomer formation from acetone is currently under study in our laboratory. Modeling of these kinetics requires resolution of meso and racemic 2,3-butanediol and positive identification of these resolved components. We report their resolution by aqueous liquid chromatography on both an analytical and a preparative scale. The resolved stereoisomer were identified by a combination of gas chromatography, gas chromatography/mass spectroscopy, ¹³C-NMR spectroscopy, optical activity, and, melting points of the m-dinitrobenzoyl eaters of meso and racemic 2,3-butanediol. An aqueous liquid chromatographic technique for resolving and qualifying major components of a butanediol fermentation mixture in 40 min is presented.     

Uptake of proteins by red blood cells

During hypotonic hemolysis red cells can take up ¹²⁵I-myoglobin and ¹²⁵I-immunoglobulin G. Cells which contain these proteins have distinctive cell morphology and are called gray ghosts. The association of protein with gray ghosts is fairly stable: these cells retain half of the proteins after 3 days. Passive diffusion of protein into the internal cell volume is the most plausible mechanism for uptake, and several lines of evidence indicate that the loaded proteins are freely diffusable within the red cells. Bacteriophage T4 is not taken up during hemolysis so uptake through large gaps in the red cell membrane with subsequent resealing seems unlikely. If an efficient procedure for fusing loaded gray ghosts to culture cells can be devised, it will be possible to introduce selected macromolecules into the cytoplasm of culture cells quite easily.