Integrated production for biodiesel and 1,3-propanediol with lipase-catalyzed transesterification and fermentation

Biodiesel, a renewable alternative to fossil energy, has shown great prospects for global proliferation in the past decade. Lipase catalyzed transesterification for biodiesel production, as a biological process with many advantages has drawn increasing attention. As a by-product, glycerol accounts for about 10% w/w of biodiesel during the process of biodiesel production. As a result, the conversion of glycerol has become a common problem which has to be resolved if considering large amount of biodiesel production. Glycerol can be fermented into 1,3-propanediol, a high value added chemical with a promising future in the polymers, for example, polytrimethylene terephthalate, and also fermentation approaches for 1,3-propanediol production which have drawn more and more attention due to advantages such as relatively low investment, mild reaction conditions and using renewable sources as the starting materials. Based on the latest technology advancements in lipase-mediated transformation for biodiesel production, the aerobic fermentation technology and genetic engineering for 1,3-propanediol production, and the integrated production of 1,3-propanediol from crude glycerol could be a promising way to improve the profit of the whole process during biodiesel production.     

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.     

Aqueous two-phase extraction of 2,3-butanediol from fermentation broths by isopropanol/ammonium sulfate system

A novel aqueous two-phase system consisted of 2-propanol/ammonium sulfate was used for the extraction of 2,3-butanediol from fermentation broths. The maximum partition coefficient and recovery of 2,3-butanediol reached 9.9 and 93.7%, respectively, and more than 99% of the cells and about 85% of the soluble proteins were removed when 34% (w/w) 2-propanol and 20% (w/w) ammonium sulfate were used. The separated cells could be re-used as inocula for subsequent fermentations. The aqueous two-phase system described in this study may have potential application in the extraction of 2,3-butanediol produced by industrial fermentation processes.     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

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.     

Production of 1,3-propanediol by Klebsiella pneumoniae from glycerol broth

Broth containing 152 g glycerol l⁻¹ from Candida krusei culture was converted to 1,3-propanediol by Klebsiella pneumoniae. Residual glucose in the broth promoted growth of K. pneumoniae while acetate was inhibitory. After desalination treatment of glycerol broth by electrodialysis, the acetate in the broth was removed. A fed-batch culture with electrodialytically pretreated broth as␣substrate was developed giving 53 g 1,3- propanediol l⁻¹ with a yield of 0.41 g g⁻¹ glycerol and a productivity of 0.94 g l⁻¹ h⁻¹.     

一株1,3-丙二醇生产菌的分离鉴定及其发酵特性

从活性污泥中分离筛选得到一株能代谢甘油生产1,3-丙二醇(1,3-PD)的菌株2-1,通过形态学鉴定、生理生化试验、16S rRNA序列分析对菌株分类学地位进行鉴定,用MEGA 4.1软件构建的系统发育树显示菌株2-1与Klebsiella pneumoniae(CP001891)的亲缘关系最近。16S rDNA序列同源性比较发现,菌株2-1与模式菌株同源率为95.4%,疑似为新种。对菌株2-1在5 L发酵罐中进行发酵特性研究,分批补料发酵时得到较高的1,3-PD终浓度,达到63.5 g/L,此时生产强度为2.19 g/(L.h),底物转化率0.64 mol/mol。     

Multi-stage laccase extraction and separation using aqueous two-phase systems: Experiment and model

This work presents results of experimental and model investigation of continuous multi-stage enzyme extraction using aqueous two-phase systems for the first time. The aqueous two-phase system comprised polyethylene glycol 3000 and phosphate with additional sodium chloride buffered to pH 7. Two different laccases served as model enzymes. One of the laccases was directly taken from fungal culture supernatant, while the other laccase was solubilized lyophilisate. The modeling is based on an equilibrium stage approach. Equilibrium data were taken from single-stage experiments and approximated by different correlation equations. The model describes densities, phase equilibrium, enzyme activity partitioning between the phases. Moreover it allows to consider activity changes due to the aqueous two-phase system. Eight multi-stage mixer-settler experiments under varying operation conditions were performed to validate the proposed model; whereas the total throughput of all multi-stage extraction experiments was about 350 g h⁻¹. The average relative deviation of modeled activities from experimentally measured activities was 23%. Therefore, the model is able to calculate the behavior of the phases as well as the partitioning of the two enzymes between the two phases for a multi-stage process based on single-stage data.     

Microbial production of 1,3-propanediol: Recent developments and emerging opportunities

1,3-Propanediol, a valuable bifunctional molecule, can be produced from renewable resources using microorganisms. It has several promising properties for many synthetic reactions, particularly for polymer and cosmetic industries. By virtue of being a natural product, relevant biochemical pathways can be harnessed into fermentation processes to produce 1,3-propanediol. Various strategies for the microbial production of 1,3-propanediol are reviewed and compared in this article with their promises and constraints. Furthermore, genetic and metabolic engineering could significantly improve product yields and overcome the limitations of fermentation technology. Present review gives an overview on 1,3-propanediol production by wild and recombinant strains. It also attempts to encompass the various issues concerned in utilization of crude glycerol for 1,3-propanediol production, with particular emphasis laid on biodiesel industries. This review also summarizes the present state of strategies studied for the downstream processing and purification of biologically produced 1,3-propanediol. The future prospect of 1,3-propanediol and its potential as a major bulk chemical are discussed under the light of the current research.     

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.     

Purification of (S)-3-cyano-5-methylhexanoic acid from bioconversion broth using an acetone/ammonium sulfate aqueous two-phase system

(S)-3-Cyano-5-methylhexanoic acid ((S)-CMHA) is the key chiral intermediate of pregabalin. In this paper, an aqueous two-phase system (ATPS) was developed to extract (S)-CMHA from nitrilase-catalyzed bioconversion broth. Inorganic salts and hydrophilic solvents were screened to form ATPS, among which an acetone/ammonium sulfate ATPS was investigated in detail, including phase diagram, effect of phase composition and stability of (S)-CMHA. The maximum product recovery of 99.15% was obtained by an optimized ATPS system composed of 15% (w/w) ammonium sulfate and 35% (w/w) acetone with the removal of 99% cells and 86.27% proteins. The total (S)-CMHA yield reached 92.11% after back-extraction. The recycling use of ammonium sulfate was investigated, and 93.10% of salt in the salt-rich phase was recovered with the addition of methanol. The results demonstrated the efficiency of the two-step extraction process for separation of (S)-CMHA.     

Isolation and characterization of microorganisms able to produce 1,3-propanediol under aerobic conditions

Microbial fermentation under strictly anaerobic conditions has been conventionally used for the production of 1,3-propanediol, a key raw material required for the synthesis of polytrimethylene terephthalate (PTT) and other polyester fibers. In the current study, we have identified eight strains of microorganism which are able to produce 1,3-propanediol under aerobic condition. Those strains were isolated from garden soil, which were enriched by culturing in LB medium with glycerol added under aerobic condition. The identities of those strains were established based on their 16S rRNA sequences and physiological characteristics. Results indicated 6 strains are Citrobacter freundii and 2 strains are Klebsiella pneumoniae subsp Penumoniae. One of Klebsiella pneumoniae subsp Penumoniae strains, designated as TUAC01, demonstrated comparable levels of 1,3-propanediol oxidoreductase, glycerol dehydratase and glycerol dehydrogenase activity to the anaerobic microorganisms described in the literature. Accordingly, in larger scales (5 l) fed-batch culture the TUAC01 strain showed a remarkable 1,3-propanediol producing potency under aerobic conditions. 60.1 g/l of 1,3-propanediol was yield after 42 h incubation in an agitating bioreactor; and in air-lift bioreactor 66.3 g/l of 1,3-propanediol was yield after 58.5 h incubation. The aerobic ferment process, reduced the product cost and made the biological method of 1,3-propanediol production more attractive.     

Different functional states of ram spermatozoa analysed by partition in an aqueous two-phase system

The surface of spermatozoa plays a critical role in many stages involved in fertilisation. The plasma membrane undergoes important alterations in the male and female reproductive tract, which result in the ability of spermatozoa to fertilise eggs. One of these membrane modifications is sperm capacitation, a process by which sperm interacts with the zona pellucida receptors leading to the acrosome reaction. It has been proposed that the freezing process induces capacitation-like changes to spermatozoa, and that this premature capacitation could explain the reduction in longevity and fertilising capacity of cryopreserved mammalian spermatozoa. Our research focused on the relationship between membrane alterations occurring throughout freezing-thawing and the processes of capacitation and acrosome reaction. We used centrifugal countercurrent distribution (CCCD) analysis to compare the partition behaviour of ram spermatozoa that was either subjected to cold-shock or frozen-thawed with capacitated and acrosome reacted samples. In addition, the effect of the induced acrosome reaction on membrane integrity of ram spermatozoa was studied using biochemical markers and electron microscopy scanning. The CCCD analysis revealed important similarities between the surface characteristics of capacitated and cold-shocked sperm as well as between acrosome-reacted and frozen-thawed sperm. Cold-shocked and capacitated sperm showed an increased cell affinity for the lower dextran-rich phase as well as a decreased heterogeneity. Likewise, the induction of the acrosome reaction resulted in a loss of viability and an important decrease in cell surface heterogeneity compared to the untreated-control sample. Similar surface changes were found when semen samples were frozen with either Fiser or milk-yolk extender. These results confirm those obtained for membrane integrity by fluorescence markers. Thus, the high cell viability value found in the control sample (74.5%) was greatly decreased after cold-shock (22.2%), cryopreservation (26.38% Fiser medium, 24.8% milk-yolk medium) and acrosome reaction (6.6%), although it was preserved after inducing capacitation (46.7%). The study using electron microscopy scanning revealed dramatic structural alterations provoked by the induction of the acrosome reaction.     

Selection and optimization of an aqueous two‐phase system for the recovery of 1,3‐propandiol from fermentation broth

In this study a suitable alcohol/salt aqueous two‐phase (ATP) system was selected for the recovery of 1,3‐propandiol (1,3‐PD) from fermentation broth. From the different alcohol/salt systems studied the ethanol and dipotassium hydrogen phosphate ATP system appeared to be favorable. To examine the potential of this ATP system the partition coefficient of 1,3‐PD in synthetic solutions was first optimized with the response surface methodology. The parameters studied were concentrations of ethanol (21.99–38.81% w/w), dipotassium hydrogen phosphate (14.99–31.81% w/w) and 1,3‐PD (6.36–73.64 g/L). The optimum conditions were found to be 35.39% w/w for ethanol, 28.40% w/w for dipotassium hydrogen phosphate and 73.6 g/L for 1,3‐PD. Under these conditions the maximum partition coefficient of 1,3‐PD and the extraction yield were determined as 23.14 and 97.82%, respectively. The optimum extraction conditions were then used to guide the recovery of 1,3‐PD from a real fermentation broth. The partition coefficient and extraction yield of 1,3‐PD reached 20.28–97.20% in this case, respectively. A favorable partition of the organic acids lactate, acetate and butyrate in the bottom phase was also achieved. We have also studied the removal of cells and macromolecules from the broth. Removal ratio of cells and proteins were 96.47 and 93.05%, respectively. Thus, the ethanol/dipotassium hydrogen phosphate ATP system appears to be an interesting alternative or can be used as one useful step in the downstream processing of 1,3‐PD from fermentation broth.     

Microwave-assisted aqueous two-phase extraction of piceid, resveratrol and emodin from Polygonum cuspidatum by ethanol/ammonium sulphate systems

Microwave-assisted, aqueous two-phase extraction was investigated to obtain effective constituents, including piceid, resveratrol and emodin in Polygonum cuspidatum. An aqueous two-phase system consisting of 25% (w/w) ethanol 21% (w/w) (NH₄)₂SO₄ gave equal yields of piceid, and 1.1- and 1.9-times higher yields of resveratrol and emodin, respectively, than that achieved by microwave-assisted extraction and heat reflux extraction. Three-separate operations, extraction, clarification and concentration, are hereby integrated into a single step to get higher yields at lower cost. This is therefore a potentially useful method for the extraction and purification of target products.     

Separation and purification of laccases from two different fungi using aqueous two-phase extraction

Selective purification still poses a challenge in the downstream processing of biomolecules such as proteins and especially enzymes. In this study a polyethylene glycol 3000 (PEG 3000)–phosphate aqueous two-phase system at 25 °C and pH 7 was successfully used for laccase purification and separation. Initially, the effect of phase forming components on enzyme activities in homogenous systems was studied. In the course of the extraction experiments tie lines, enzyme source, initial enzyme activities, phase ratio and sodium chloride concentrations were varied and their influence on the activity partitioning was determined. Partitioning results were validated using clear-native-PAGE and isoelectric focusing. Based on these results, the separation of laccases from Trametes versicolor and Pleurotus sapidus was investigated using the principle of superposition. Sodium chloride was used to adjust laccase partitioning in the applied aqueous two-phase system (ATPS). Finally, two modes of operation are proposed depending on the aim of the purification task. One mode with 0.133 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and without sodium chloride separates P. sapidus laccases from T. versicolor laccases with clearance factors of 5.23 and 6.45, respectively. The other mode of operation with 0.124 g g⁻¹ of PEG3000, 0.063 g g⁻¹ of phosphate and 0.013 g g⁻¹ of sodium chloride enables a partitioning of both laccases into the bottom phase of the ATPS resulting in a purification factor of 2.74 and 96% activity recovery.     

Synergized subcritical-ultrasound-assisted aqueous two-phase extraction,purification, and characterization of Lentinus edodes polysaccharides

The effect of a synergized two-step subcritical water extraction (SWE) and simultaneous multi-frequency ultrasound-assisted alcohol/salt aqueous two-phase extraction (MFu-AATPE) on the yield, physicochemical, structural characteristics, and antioxidant activities of Lentinus edodes polysaccharides (LEPs) was investigated. Crude LEP extracted under subcritical extraction (31.14%) was purified using dual and triple frequency ultrasound-assisted aqueous two-phase systems giving a yield of 94.57% and 97% respectively. Compared with the dual-frequency sonication (20/40 kHz), the triple frequency sonication (20/40/60 kHz) gave maximum yield and improved the desalination rate by 33.6%. Congo red analysis revealed triple helix structures. Gas Chromatography analysis showed the existence of mannose, glucose, arabinose, xylose, and galactose whilst spectral similarities were observed through Fourier Transform Infrared Spectroscopy. The average molecular weight (M_w) was 83.6170 Da, 2384 Da and 2387 Da for control, dual and triple frequency samples respectively. Ultrasound treated polysaccharides displayed stronger antioxidant activities against the 2.2-diphenyl;-1 picrylhydrazyl (DPPH), 2, 2ʹ-azino-bis 3-ethylbenzothiazoline-6 sulfonic acid (ABTS) and hydroxyl radicals, thus demonstrating their potency in reducing oxidation. However, the microstructure of the triple frequency treated sample was altered compared to the dual-frequency sample. Therefore, this study demonstrated the efficacy of SWE in crude LEPs extraction and illustrated MFu-AATPE as an efficient technique that selectively isolates polysaccharides and enhances extraction efficiencies.     

Evaluation of the effects of the parameters involved in the purification of clavulanic acid from fermentation broth by aqueous two-phase systems

The purification of clavulanic acid (CA), which is an important β-lactam antibiotic produced by submerged cultivation of Streptomyces clavuligerus, was studied through the use of phosphate and polyethylene glycol-based aqueous two-phase systems. The parameters’ effect on the yield and purification was evaluated through an experimental design and the preliminary results showed that the polyethylene molecular mass and tie-line length and phase volume ratio exerted the strongest effect on the yield and distribution coefficient in the range tested. In addition, the response surface methodology was used to optimize the distribution coefficient, yield, and purification factor. The optimal conditions of yield and purification factor are in the regions where polyethylene has a low molecular mass, pH close to the isoelectric point, and lower top phase volume. A 100% yield and a 1.5-fold purification factor are obtained when extracting CA by maximizing the conditions of an aqueous two-phase system.     

Effects of over-expression of glycerol dehydrogenase and 1,3-propanediol oxidoreductase on bioconversion of glycerol into 1,3-propandediol by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> under micro-aerobic conditions

Glycerol dehydrogenase (GDH) and 1,3-propanediol (1,3-PD) oxidoreductase had been proved two key enzymes for 1,3-PD production by Klebsiella pneumoniae. Fed-batch fermentations of the recombinant K. pneumoniae strains, over-expressing the two enzymes individually, were carried out under micro-aerobic conditions, and the behaviors of the recombinants were investigated. Results showed that over-expression of 1,3-PD oxidoreductase did not affect the concentration of 1,3-PD. However, it enhanced the molar yield from 50.6 to 64.0% and reduced the concentration of by-products. Among them, the concentrations of lactic acid, ethanol and succinic acid were decreased by 51.8, 50.6 and 47.4%, respectively. Moreover, in the recombinant the maximal concentration of 3-hydroxypropionaldehyde decreased by 73.6%. Over-expression of GDH decreased the yield of ethanol and 2,3-butanediol, meanwhile it increased the concentration of acetic acid. No significant changes were observed both in 1,3-PD yield and glycerol flux distributed to oxidative branch.