Reactive extraction for downstream separation of 1,3-propanediol

The downstream separation of 1,3-propanediol from dilute aqueous solution was studied. A process combining reversible reaction of 1, 3-propanediol with acetaldehyde to 2-methyl-1,3-dioxane and a simultaneous extraction of the product by organic solvent appears to be technically feasible and attractive. The dioxane yield was 91-92%, the overall conversion of 1,3-propanediol was ca. 98%, and recovery of dioxane into the organic extractant was 75%.     

Debottlenecking the 1,3-propanediol pathway by metabolic engineering

The history of 1,3-propanediol (1,3-PD) conversion from being a specialty chemical to being a bulk chemical illustrates that the concerted effort of different metabolic engineering approaches brings the most successful results. In order to metabolically tailor the 1,3-PD production pathway multiple strategies have been pursued. Knocking-out genes responsible for by-products formation, intergeneric transfer and overexpression of the genes directly involved in the pathway, manipulation with internal redox balance, introduction of a synthetic flux control point, and modification of the substrate mechanism of transport are some of the strategies applied. The metabolic engineering of the microbial 1,3-PD production exploits both native producers and microorganisms with acquired ability to produce the diol via genetic manipulations. Combination of the appropriate genes from homologous and heterologous hosts is expected to bring a desired objective of production of 1,3-PD cheaply, efficiently and independently from non-renewable resources. The state-of-the-art of the 1,3-PD pathway metabolic engineering is reviewed in this paper.     

Conversion of glycerol to 1,3-propanediol by a newly isolated thermophilic strain

Of 60 different thermophilic enrichment cultures, 16 converted glycerol anaerobically to 1,3-propanediol. Two PD-forming strains were further enriched, isolated, and characterised. For the most active strain, AT1, the optimal cultivation parameters for pH and temperature were determined as 5.8 to 6.0 and 58°C, respectively. In batch-fermentations with AT1, 6.4 g propanediol per litre was formed with a productivity of 0.17 g l^–1 h^–1.     

Continuous countercurrent salting-out extraction of 1,3-propanediol from fermentation broth in a packed column

The possibility of continuous extraction of 1,3-propanediol in a experimental packed column was investigated using a salting-out extraction system of dipotassium phosphate/ethanol. Mass transfer of 1,3-propanediol takes place from the dispersed phase (salt-rich solution) to the continuous phase (ethanol). The influences of flow rate of dispersed phase and size of packing material on partition coefficient and recovery of 1,3-propanediol were investigated and the results were compared with those obtained in spray column and test tube. Furthermore, the influences of various system compositions on hold up of dispersed phase, mass transfer coefficient, and system stability were also studied in the column packed by stainless steel Dixon 3 × 3 mm. It was found that the packed column showed a good extraction efficiency and stability. Besides, 1,3-propanediol recovery of 90.30% was obtained during a 11 h continuous operation when the real fermentation broth was used. At the same time, 94.4% of phosphate could be recovered when 0.2 volume of anhydrous ethanol was added into the raffinate phase at pH 4.0.     

补料分批发酵过程中两阶段发酵生产1,3-丙二醇

在补料分批发酵过程中提高比生长速率不仅减少乙醇、甲酸的生成,而且提高1,3-丙二醇的得率和比生产速率.发酵后期甘油的浓度在15～26 g/L时有利于提高1,3-丙二醇的生产.采取在发酵前期控制菌体较高比生长速率和发酵后期控制适宜甘油浓度相结合的策略,有效地提高了1,3-丙二醇的生产,降低副产物乳酸和乙醇的生成.     

1,3-丙二醇发酵中甘油代谢及产物抑制作用

对微生物法甘油转化成1,3-丙二醇过程中代谢规律及代谢控制的相关酶作以简述,并着重分析了丁酸梭菌发酵生产中乙酸、丁酸等副产物对细胞的抑制作用,对未来的研究发展方向进行了展望。     

pH对克雷伯氏菌1,3-丙二醇合成关键酶酶活及发酵特性的影响

在5 L发酵罐进行甘油脉冲流加发酵,分析了不同pH值对克雷伯氏肺炎杆菌发酵特性的影响,pH 6.5为菌体最佳生长条件,克雷伯氏肺炎杆菌合成1,3-丙二醇的产量最高。在1,3-丙二醇合成速率较大的对数中前期,进行甘油脉冲流加发酵,提高甘油浓度促进甘油脱水酶、1,3-丙二醇氧化还原酶和甘油脱氢酶活性。不同pH值的脉冲试验表明,甘油脱水酶,2,3-丁二醇脱氢酶比酶活随着pH值的升高而升高,1,3-丙二醇氧化还原酶,乳酸脱氢酶比酶活在pH6.5最高,因此偏酸性的发酵条件和对数期维持一定的甘油浓度能够促进1,3-丙二醇的合成。     

Fermentation of raw glycerol to 1,3-propanediol by new strains ofClostridium butyricum

Industrial glycerol obtained through the transesterification process using rapeseed oil did not support growth of several strains ofClostridium butyricum obtained from bacterial culture collections. Ten new strains ofC. butyricum were obtained from mud samples from a river, a stagnant pond, and a dry canal. These new isolates fermented the commercial glycerol and produced 1,3-propanediol as a major fermentation product with concomitant production of acetic and butyric acids. Four of the ten isolates were able to grow on industrial glycerol obtained from rapeseed oil. One strain,C. butyricum E5, was very resistant to high levels of glycerol and 1,3-propanediol. Using fed-batch fermentation, 109 g L^–1 of industrial glycerol were converted into 58 g of 1,3-propanediol, 2.2 g of acetate and 6.1 g of butyrate per liter.     

Enzymatic asymmetrization of prochiral 2-benzyl-1,3-propanediol through esterification in solvent media

The enzymatic esterification of the prochiral substrate, 2-benzyl-1,3-propanediol, has been studied in solvent media. Among the five tested lipases, Lipozyme and Novozym 435 led to higher reaction rates. Novozym 435 catalyzed faster reactions at low water activity and in solvents having log P above 2. However, the two positions of the diol, pro-(R) and pro-(S), led to the same reaction rate trends and no prochiral selectivity was obtained. When using Lipozyme in toluene, the reaction rates for the formation of both (R) and (S) products presented an optimum at a water activity of 0.22. In this case, the prochiral selectivity increased with the water activity, from a value of 5 at a_w < 0.01, to a value of 8 at a_w = 0.22, at which point it remained constant.     

不同pH调节剂对补料批式发酵产1,3-丙二醇的影响

对肺炎克雷伯氏菌（Klebsiellapneumoniae）发酵生产1,3-丙二醇（1,3-Propanediol,1,3．PD）的补碱策略进行了研究。分别利用NaOH、氨水、KOH三种溶液作为pH调节剂,优化三种pH调节剂并得到按一定比例混合的混合碱。当采用混合碱调控发酵pH值为7．0时,1,3-丙二醇的产量达到了55dL,比无pH调控（对照）发酵过程发酵水平提高了10．6倍。     

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.     

产1，3-丙二醇重组大肠杆菌JM109（pEtac—dhaB—tac—yqhD）的构建

在生物柴油的生产过程中,最高可得到约10％的副产物甘油,副产物甘油的去向将成为生物柴油大规模产业化发展所面临的严峻问题。以生物柴油副产物甘油为原料耦合生产1,3-丙二醇,不仅解决了生物柴油副产物甘油的出路问题,同时降低了1,3-丙二醇的生产成本。本研究在前期工作的基础上,分别获得了来源于肺炎克雷伯氏茵的甘油脱水酶编码基因dhaB和来源于大肠杆菌的1,3-PD氧化还原酶同工酶编码基因yqhD,利用表达载体pEtac串联构建了重组质粒pEtac—dhaB—tac—yqhD,将其转化大肠杆菌得到产1,3-丙二醇重组大肠杆菌JM109（pEtac—dhaB-tac—yqhD）,降低了代谢中间产物3-羟基丙醛的积累,提高了1,3-丙二醇的产量。     

Site-Specific and Asymmetric Hydrolysis of Prochiral 2-Phenyl-1,3-propanediol Diacetate by a Bacterial Esterase from an Isolated Strain

Bacillus cereus 809A and Burkholderia sp. 711C were isolated from soil. These strains demonstrate hydrolysis activity towards prochiral 2-phenyl-1,3-propanediol diacetate and accumulated the corresponding chiral monoacetates into the reaction mixture. When 2-phenyl 1,3-propanediol diacetate was used as a substrate, the produced monoacetates with Burkholderia sp. 711C were obtained in a racemic form but that produced by Bacillus cereus 809A showed an excess of the (S)-form. The resting cell reaction revealed that for Bacillus cereus 809A, there was an enrichment of one of the enantiomers of the monoacetate such that the enantiomeric excess (e.e.) of the (S)-form was over 95%. The purified enzyme from Bacillus cereus 809A hydrolyzed diacetate to monoacetate, and the e.e. value of the (S)-form increased by prolonged reaction in a way similar to the resting cell reaction. From N-terminal amino acids, this esterase is conserved in some strains of Bacillus for which the genomic sequences have been reported.     

Microbial asymmetric oxidation of 2-butyl-1,3-propanediol

Microbial asymmetric oxidation of 2-butyl-1,3-propanediol was investigated for an efficient synthesis of S- and R-enantiomers of 2-hydroxymethylhexanoic acid (2-HMHA). From an intensive survey of the stocked bacterial strains, Acetobacter pasteurianus IAM 12073 and Pseudomonas putida IFO 3738 were found to show the highest S- and R-2-HMHA-producing activity, respectively. Under optimized conditions, A. pasteurianus (351 mg dry cell weight) and P. putida (642 mg dry cell weight) cells produced 12.0 g l⁻¹ S-2-HMHA with 89% enantiomeric excess (e.e.) at 24 h of incubation and 5.1 g l⁻¹ R-2-HMHA with 94% e.e. at 35 h of incubation from 2-butyl-1,3-propanediol.     

High-level expression of the 1,3-propanediol oxidoreductase from klebsiella pneumoniae in escherichia coli

As one of four key enzymes in glycerol dismutation process, 1,3-propanediol oxidoreductase (EC.1.1.1.202) is important in converting glycerol to 1,3-propanediol in Klebsiella pneumoniae. The dhaT gene encoding 1,3-propanediol oxidoreductase was amplified by polymerase chain reaction (PCR) using the genome DNA of K. pneumoniae as template, and then cloned into cloning vector pMD18-T. After DNA sequence was determined, the dhaT gene was subcloned into Escherichia coli expression vector pET-22b (+) and pET-28a (+). Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) analysis revealed that both the recombinant E. coli BL21 (DE3) (pET-22b (+)-dhaT) and E. coli BL21(DE3)(pET-28a (+)-dhaT) expressed predicted 42-kDa 1,3-propanediol oxidoreductase after induced by isopropyl-β-d-thiogalactopyranoside (IPTG), and the recombinant enzyme of E. coli BL21 (DE3) (pET-28a (+)-dhaT) was mostly in soluble form, and exhibited high activity (96.8 U/mL culture). The recombinant enzyme was purified and biochemically characterized. The apparent K _m values of the enzyme for 1,3-propanediol and NAD⁺ were 8.5 and 0.21 mM, respectively. The enzyme had maximum activity at pH 9.5 and 30°C.     

Cross-linking of DNA in liver and testes of rats fed 1,3-propanediol

1,3-Propanediol (PAD) was fed to rats for 15 weeks, and its effects on hepatic and testicular DNA were studied. The control rats were fed a casein-based diet that contained 10% tocopherol-stripped corn oil with 30 IU of d,l-α-tocopherol acetate/kg; the experimental rats were fed the same diet with 500 ppm of PAD. Homogenates prepared from the livers of each group of rats converted 1,3-propanediol to malondialdehyde (MDA) with equal efficacy, but homogenates of testes did not catalyze this conversion. After 10–15 weeks of feeding the diets, the hepatic DNA of the rats fed PAD had less template activity, more bound tryptophan and more DNA-protein and interstrand DNA cross-links than that of the control rats. As measured by template activity and bound tryptophan, testicular DNA of the experimental rats was not different from that of the control rats; however, there was slightly more cross-linking in the testicular DNA of experimental rats than in that of control rats. Testes of the experimental rats contained more lipid-soluble fluorophores than did those of the control rats. The results are consistent with the conclusion that PAD was converted to MDA in vivo and that MDA is the reactive species that caused the observed biological damage.     

产1,3-丙二醇基因工程菌发酵条件的研究

利用途径工程的方法,将来源于克雷伯氏菌(Klebsiella pneumoniae)的甘油脱水酶基因dhaB和1,3-丙二醇氧化还原酶基因dhaT构建成多顺反子重组质粒pSE-dhaB-dhaT并在大肠杆菌JM 109中进行表达,在大肠杆菌中构建一条新的产1,3-丙二醇代谢途径。研究表明,重组菌株JM 109/pSE-dhaB-dhaT在微好氧条件下,尝试用廉价的乳糖为诱导物、维生素B12为辅酶,可以将甘油转化为1,3-丙二醇,产量达15.34 g/L,甘油转化率为35.7%,对低成本生产1,3-丙二醇作了有益的探索。     

Anaerobic degradation of 1,3-propanediol by sulfate-reducing and by fermenting bacteria

Three strains of strictly anaerobic Gram-negative, non-sporeforming, motile bacteria were enriched and isolated from freshwater sediments with 1,3-propanediol as sole energy and carbon source. Strain OttPdl was a sulfate-reducing bacterium which grew also with lactate, ethanol, propanol, butanol, 1,4-butanediol, formate or hydrogen plus CO₂, the latter only in the presence of acetate. In the absence of sulfate, most of these substrates were fermented to the respective fatty acids in syntrophic cooperation with Methanospirillum hungatei. Sulfur, thiosulfate, or sulfite were reduced, nitrate not. The other two isolates degraded propanediol only in coculture with Methanospirillum hungatei. Strain OttGlycl grew in pure culture with acetoin and with glycerol in the presence of acetate. Strain WoAcl grew in pure culture only with acetoin. Both strains did not grow with other substrates, and did not reduce nitrate, sulfate, sulfur, thiosulfate or sulfite. The isolates were affiliated with the genera Desulfovibrio and Pelobacter. The pathways of propanediol degradation and the ecological importance of this process are discussed.     

Crystallization and phase behavior of 1,3-propanediol esters II. 1,3-propanediol distearate/1,3-propanediol dipalmitate (SS/PP) and 1,3-propanediol distearate/1,3-propanediol dimyristate (SS/MM) binary systems

Polymorphic influences on the phase behavior of two types of binary mixtures of saturated monoacid 1,3-propanediol esters (PADEs), dipalmitate/distearate (PP/SS) and dimyristate/distearate (MM/SS) were examined by X-ray diffraction (XRD), differential scanning calorimetry (DSC), and by solid fat content (SFC), hardness and microscopy measurements. Three stacking modes have been found in the PP/SS binary system. Mixed SS-PP bilayers were detected in all mixtures, SS-SS bilayers in x(PP)=0.0-0.4 mixtures and PP-PP bilayers in x(PP)=0.6-0.1 mixtures. Two different but close beta polymorphs and one beta' polymorph were detected for this system. beta' was only detected in x(PP)=0.5-0.9 mixtures for the mixed bilayers. For the MM/SS binary system, only MM-MM and SS-SS bilayers were detected and both solid phases crystallized in two different beta forms. XRD data evidenced clearly that the MM and SS components were completely immiscible in the solid state. The phase diagrams constructed using DSC data, exhibited a typical eutectic-type phase boundary. The presence of eutectics, the shape of the solidus lines as well as the analysis of the individual enthalpies of melting indicated typical phase separation for both systems. A thermodynamic study based on the Hildebrand equation and using the Bragg-Williams approximation for non-ideality of mixing confirmed the phase separation in the solid phase and suggested that the PP and SS were miscible in the liquid phase and that SS formed an ideal mixing with MM. Avrami analysis of SFC vs. time curves indicated heterogeneous nucleation and spherulitic crystal development from sporadic nuclei, and suggested that the nucleation rate was higher for the mixture at the eutectic composition. The relative hardness was correlated with the enthalpies, the final SFC and the microscopy measurements.     

Evaluation of solid phase extraction for downstream separation of propane-1,3-diol and butan-1-ol from fermentation broth

Today, glycerol is mainly a by-product of fat splitting and biodiesel production. This study examined the use of chemically modified silica gels for downstream separation of propane-1,3-diol and butan-1-ol from fermentation broths obtained through the glycerol fermentation process. The developed method was found to be simple and efficient for the isolation and purification of butan-1-ol from the other components in the fermentation mixture. However, in the case of the separation of propane-1,3-diol from fermentation broth, the silica gel sorbents were ineffective.