Analysis of exposed cellulose surfaces in pretreated wood biomass using carbohydrate‐binding module (CBM)–cyan fluorescent protein (CFP)

In enzymatic saccharification of lignocellulosics, the access of the enzymes to exposed cellulose surfaces is a key initial step in triggering hydrolysis. However, knowledge of the structure–hydrolyzability relationship of the pretreated biomass is still limited. Here we used fluorescent‐labeled recombinant carbohydrate‐binding modules (CBMs) from Clostridium josui as specific markers for crystalline cellulose (CjCBM3) and non‐crystalline cellulose (CjCBM28) to analyze the complex surfaces of wood tissues pretreated with NaOH, NaOH–Na₂S (kraft pulping), hydrothermolysis, ball‐milling, and organosolvolysis. Japanese cedar wood, one of the most recalcitrant softwood species was selected for the analysis. The binding analysis clarified the linear dependency of the exposure of crystalline and non‐crystalline cellulose surfaces for enzymatic saccharification yield by the organosolv and kraft delignification processes. Ball‐milling for 5–30 min increased saccharification yield up to 77%, but adsorption by the CjCBM–cyan fluorescent proteins (CFPs) was below 5%. Adsorption of CjCBM–CFPs on the hydrothermolysis pulp were less than half of those for organosolvolysis pulp, in coincidence with low saccharification yields. For all the pretreated wood, crystallinity index was not directly correlated with the overall saccharification yield. Fluorescent microscopy revealed that CjCBM3–CFP and CjCBM28–CFP were site‐specifically adsorbed on external fibrous structures and ruptured or distorted fiber surfaces. The assay system with CBM–CFPs is a powerful measure to estimate the initiation sites of hydrolysis and saccharification yields from chemically delignified wood pulps. Biotechnol. Bioeng. 2010; 105: 499–508. © 2009 Wiley Periodicals, Inc.     

里氏木霉与黑曲霉混合发酵产纤维素酶及其水解特性

研究了利用里氏木霉和黑曲霉混合培养产纤维素酶,以黑曲霉孢子悬浮液的不同活化浓度及不同的活化时间来寻找2个菌种发挥最大协同作用的结合点以及所产纤维素酶的水解特性。以里氏木霉单一培养和黑曲霉单一培养为参照进行对比研究。底物为农林废弃物之一的玉米秸秆,经过蒸气爆破预处理后,用作产酶C源。结果表明:黑曲霉孢子悬浮液活化浓度为10个/mL,活化时间为12 h时,滤纸酶比酶活最高,达3.32 U/mL,高于里氏木霉单一培养的2.25 U/mL,β-葡萄糖苷酶比酶活达1.32 U/mL,高于里氏木霉单一培养的0.57 U/mL。为进一步验证混合菌产纤维素酶的水解效果,利用混合菌产纤维酶的酶液及里氏木霉产纤维素酶的酶液进行酶水解实验,当酶用量为20 U/g绝干纤维素,底物质量浓度为100 g/L条件下水解48 h,混合菌所产酶液酶解得率达70.00%,高于里氏木霉所产酶液的酶解得率63.05%。实验表明里氏木霉与黑曲霉混合培养产酶是可行的,并优于单一菌种培养。     

Enzymatic saccharification of sugar cane bagasse by continuous xylanase and cellulase production from cellulomonas flavigena PR‐22

Cellulase (CMCase) and xylanase enzyme production and saccharification of sugar cane bagasse were coupled into two stages and named enzyme production and sugar cane bagasse saccharification. The performance of Cellulomonas flavigena (Cf) PR‐22 cultured in a bubble column reactor (BCR) was compared to that in a stirred tank reactor (STR). Cells cultured in the BCR presented higher yields and productivity of both CMCase and xylanase activities than those grown in the STR configuration. A continuous culture with Cf PR‐22 was run in the BCR using 1% alkali‐pretreated sugar cane bagasse and mineral media, at dilution rates ranging from 0.04 to 0.22 1/h. The highest enzymatic productivity values were found at 0.08 1/h with 1846.4 ± 126.4 and 101.6 ± 5.6 U/L·h for xylanase and CMCase, respectively. Effluent from the BCR in steady state was transferred to an enzymatic reactor operated in fed‐batch mode with an initial load of 75 g of pretreated sugar cane bagasse; saccharification was then performed in an STR at 55°C and 300 rpm for 90 h. The constant addition of fresh enzyme as well as the increase in time of contact with the substrate increased the total soluble sugar concentration 83% compared to the value obtained in a batch enzymatic reactor. This advantageous strategy may be used for industrial enzyme pretreatment and saccharification of lignocellulosic wastes to be used in bioethanol and chemicals production from lignocellulose. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:321–326, 2016     

Comparative study of corn stover pretreated by dilute acid and cellulose solvent‐based lignocellulose fractionation: Enzymatic hydrolysis,supramolecular structure,and substrate accessibility

Liberation of fermentable sugars from recalcitrant biomass is among the most costly steps for emerging cellulosic ethanol production. Here we compared two pretreatment methods (dilute acid, DA, and cellulose solvent and organic solvent lignocellulose fractionation, COSLIF) for corn stover. At a high cellulase loading [15 filter paper units (FPUs) or 12.3 mg cellulase per gram of glucan], glucan digestibilities of the corn stover pretreated by DA and COSLIF were 84% at hour 72 and 97% at hour 24, respectively. At a low cellulase loading (5 FPUs per gram of glucan), digestibility remained as high as 93% at hour 24 for the COSLIF‐pretreated corn stover but reached only ～60% for the DA‐pretreated biomass. Quantitative determinations of total substrate accessibility to cellulase (TSAC), cellulose accessibility to cellulase (CAC), and non‐cellulose accessibility to cellulase (NCAC) based on adsorption of a non‐hydrolytic recombinant protein TGC were measured for the first time. The COSLIF‐pretreated corn stover had a CAC of 11.57 m²/g, nearly twice that of the DA‐pretreated biomass (5.89 m²/g). These results, along with scanning electron microscopy images showing dramatic structural differences between the DA‐ and COSLIF‐pretreated samples, suggest that COSLIF treatment disrupts microfibrillar structures within biomass while DA treatment mainly removes hemicellulose. Under the tested conditions COSLIF treatment breaks down lignocellulose structure more extensively than DA treatment, producing a more enzymatically reactive material with a higher CAC accompanied by faster hydrolysis rates and higher enzymatic digestibility. Biotechnol. Bioeng. 2009;103: 715–724. © 2009 Wiley Periodicals, Inc.     

Biological pretreatment of corn stover with Phlebia brevispora NRRL‐13108 for enhanced enzymatic hydrolysis and efficient ethanol production

Biological pretreatment of lignocellulosic biomass by white‐rot fungus can represent a low‐cost and eco‐friendly alternative to harsh physical, chemical, or physico‐chemical pretreatment methods to facilitate enzymatic hydrolysis. In this work, solid‐state cultivation of corn stover with Phlebia brevispora NRRL‐13018 was optimized with respect to duration, moisture content and inoculum size. Changes in composition of pretreated corn stover and its susceptibility to enzymatic hydrolysis were analyzed. About 84% moisture and 42 days incubation at 28°C were found to be optimal for pretreatment with respect to enzymatic saccharification. Inoculum size had little effect compared to moisture level. Ergosterol data shows continued growth of the fungus studied up to 57 days. No furfural and hydroxymethyl furfural were produced. The total sugar yield was 442 ± 5 mg/g of pretreated corn stover. About 36 ± 0.6 g ethanol was produced from 150 g pretreated stover per L by fed‐batch simultaneous saccharification and fermentation (SSF) using mixed sugar utilizing ethanologenic recombinant Eschericia coli FBR5 strain. The ethanol yields were 32.0 ± 0.2 and 38.0 ± 0.2 g from 200 g pretreated corn stover per L by fed‐batch SSF using Saccharomyces cerevisiae D5A and xylose utilizing recombinant S. cerevisiae YRH400 strain, respectively. This research demonstrates that P. brevispora NRRL‐13018 has potential to be used for biological pretreatment of lignocellulosic biomass. This is the first report on the production of ethanol from P. brevispora pretreated corn stover. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:365–374, 2017     

Tissue-specific biomass recalcitrance in corn stover pretreated with liquid hot-water: enzymatic hydrolysis (part 1)

Lignin content, composition, distribution as well as cell wall thickness, structures, and type of tissue have a measurable effect on enzymatic hydrolysis of cellulose in lignocellulosic feedstocks. The first part of our work combined compositional analysis, pretreatment and enzyme hydrolysis for fractionated pith, rind, and leaf tissues from a hybrid stay-green corn, in order to identify the role of structural characteristics on enzyme hydrolysis of cell walls. The extent of enzyme hydrolysis follows the sequence rind < leaves < pith with 90% conversion of cellulose to glucose in 24 h in the best cases. Physical fractionation of corn stalks or other C(4) grasses into soft and hard tissue types could reduce cost of cellulose conversion by enabling reduced enzyme loadings to hydrolyze soft tissue, and directing the hard tissue to other uses such as thermal processing, combustion, or recycle to the land from which the corn was harvested.     

Exploring cellular adhesion and differentiation in a micro‐/nano‐hybrid polymer scaffold

Polymer scaffolds play an important role in three dimensional (3‐D) cell culture and tissue engineering. To best mimic the archiecture of natural extracellular matrix (ECM), a nano‐fibrous and micro‐porous combined (NFMP) scaffold was fabricated by combining phase separation and particulate leaching techniques. The NFMP scaffold possesses architectural features at two levels, including the micro‐scale pores and nano‐scale fibers. To evaluate the advantages of micro/nano combination, control scaffolds with only micro‐pores or nano‐fibers were fabricated. Cell grown in NFMP and control scaffolds were characterized with respect to morphology, proliferation rate, diffentiation and adhesion. The NFMP scaffold combined the advantages of micro‐ and nano‐scale structures. The NFMP scaffold nano‐fibers promoted neural differentiation and induced “3‐D matrix adhesion”, while the NFMP scaffold micro‐pores facilitated cell infiltration. This study represents a systematic comparison of cellular activities on micro‐only, nano‐only and micro/nano combined scaffolds, and demonstrates the unique advantages of the later. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Surface carbohydrate analysis and bioethanol production of sugarcane bagasse pretreated with the white rot fungus, Ceriporiopsis subvermispora and microwave hydrothermolysis

Effects of pretreatments with a white rot fungus, Ceriporiopsis subvermispora, and microwave hydrothermolysis of bagasse on enzymatic saccharification and fermentation were evaluated. The best sugar yield, 44.9 g per 100 g of bagasse was obtained by fungal treatments followed by microwave hydrothermolysis at 180 °C for 20 min. Fluorescent-labeled carbohydrate-binding modules which recognize crystalline cellulose (CjCBM3-GFP), non-crystalline cellulose (CjCBM28-GFP) and xylan (CtCBM22-GFP) were applied to characterize the exposed polysaccharides. The microwave pretreatments with and without the fungal cultivation resulted in similar levels of cellulose exposure, but the combined treatment caused more defibration and thinning of the plant tissues. Simultaneous saccharification and fermentation of the pulp fractions obtained by microwave hydrothermolysis with and without fungal treatment, gave ethanol yields of 35.8% and 27.0%, respectively, based on the holocellulose content in the pulp. These results suggest that C. subvermispora pretreatment could be beneficial part of the process to produce ethanol from bagasse.     

Enzymatic digestion of alkaline‐sulfite pretreated sugar cane bagasse and its correlation with the chemical and structural changes occurring during the pretreatment step

Sugar cane bagasse is recalcitrant to enzymatic digestion, which hinders the efficient conversion of its polysaccharides into fermentable sugars. Alkaline‐sulfite pretreatment was used to overcome the sugar cane bagasse recalcitrance. Chemical and structural changes that occurred during the pretreatment were correlated with the efficiency of the enzymatic digestion of the polysaccharides. The first 30 min of pretreatment, which removed approximately half of the initial lignin and 30% of hemicellulose seemed responsible for a significant enhancement of the cellulose conversion level, which reached 64%. After the first 30 min of pretreatment, delignification increased slightly, and hemicellulose removal was not enhanced; however, acid groups continued to be introduced into the residual lignin. Water retention values were 145% to the untreated bagasse and 210% to the bagasse pretreated for 120 min and fiber widths increased from 10.4 to 30 μm, respectively. These changes were responsible for an additional increase in the efficiency of enzymatic hydrolysis of the cellulose, which reached 92% with the 120 min pretreated sample. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:890–895, 2013     

Study on syntheses and anticoagulant action of heparin/rare earth nano‐oxides hybrid material

Four hybrid materials of RE₂O₃‐TDI‐Heparin (TDI = Toluene 2,4–diisocyanate, RE = La, Eu, Nd, Sc) were prepared by the method of graft. The materials were characterized by IR, TG, and SEM, which confirmed that the heparin was grafted on the surface of TDI modified rare earth nano‐oxides. The cell adhesion experiment and the anticoagulant experiment demonstrated that the materials have lower cell toxicity, better cell adhesion as well as better anticoagulant action. In addition, the clotting time of hybrid materials were shortened compared with the heparin. © 2010 Wiley Periodicals, Inc. Biopolymers 93: 887–892, 2010.     

Multicomponent cellulase production by Cellulomonas biazotea NCIM‐2550 and its applications for cellulosic biohydrogen production

Among four cellulolytic microorganisms examined, Cellulomonas biazotea NCIM‐2550 can grow on various cellulosic substrates and produce reducing sugar. The activity of cellulases (endoglucanase, exoglucanase, and cellobiase), xylanase, amylase, and lignin class of enzymes produced by C. biazotea was mainly present extracellularly and the enzyme production was dependent on cellulosic substrates (carboxymethyl cellulose [CMC], sugarcane bagasse [SCB], and xylan) used for growth. Effects of physicochemical conditions on cellulolytic enzyme production were systematically investigated. Using MnCl₂ as a metal additive significantly induces the cellulase enzyme system, resulting in more reducing sugar production. The efficiency of fermentative conversion of the hydrolyzed SCB and xylan into clean H₂ energy was examined with seven H₂‐producing pure bacterial isolates. Only Clostridiumbutyricum CGS5 exhibited efficient H₂ production performance with the hydrolysate of SCB and xylan. The cumulative H₂ production and H₂ yield from using bagasse hydrolysate (initial reducing sugar concentration = 1.545 g/L) were approximately 72.61 mL/L and 2.13 mmol H₂/g reducing sugar (or 1.91 mmol H₂/g cellulose), respectively. Using xylan hydrolysate (initial reducing sugar concentration = 0.345 g/L) as substrate could also attain a cumulative H₂ production and H₂ yield of 87.02 mL/L and 5.03 mmol H₂/g reducing sugar (or 4.01 mmol H₂/g cellulose), respectively. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Ultra scale‐down studies of the effect of shear on cell quality; Processing of a human cell line for cancer vaccine therapy

Whole cell therapy is showing potential in the clinic for the treatment of many chronic diseases. The translation of laboratory‐scale methods for cell harvesting and formulation to commercial‐scale manufacturing offers major bioprocessing challenges. This is especially the case when the cell properties determine the final product effectiveness. This study is focused on developing an ultra scale‐down method for assessing the impact of the hydrodynamic environment on human cells that constitute the therapeutic product. Small volumes of a prostate cancer cell line, currently being developed in late phase II clinical trials as an allogeneic whole cell vaccine therapy for prostate cancer, were exposed to hydrodynamic shear rates similar to those present in downstream process, formulation and vial filling operations. A small scale rotating disc shear device (20 mL) was used over a range of disc speeds to expose cells to maximum shear rates ranging from 90 × 10³ to 175 × 10³ s^‐1 (equivalent maximum power dissipation rates of 14 × 10³ to 52 × 10³ W kg^‐1). These cells were subsequently analyzed for critical cell quality attributes such as the retention of membrane integrity and cell surface marker profile and density. Three cell surface markers (CD9, CD147, and HLAA‐C) were studied. The cell markers exhibited different levels of susceptibility to hydrodynamic shear but in all cases this was less than or equal to the loss of membrane integrity. It is evident that the marker, or combination or markers, which might provide the required immunogenic response, will be affected by hydrodynamic shear environment during bioprocessing, if the engineering environment is not controlled to within the limits tolerated by the cell components. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Influence of xylan on the enzymatic hydrolysis of steam‐pretreated corn stover and hybrid poplar

The focus of this study was to alter the xylan content of corn stover and poplar using SO₂‐catalyzed steam pretreatment to determine the effect on subsequent hydrolysis by commercial cellulase preparations supplemented with or without xylanases. Steam pretreated solids with xylan contents ranging from ～1 to 19% (w/w) were produced. Higher xylan contents and improved hemicellulose recoveries were obtained with solids pretreated at lower severities or without SO₂‐addition prior to pretreatment. The pretreated solids with low xylan content (<4% (w/w)) were characterized by fast and complete cellulose to glucose conversion when utilizing cellulases. Commercial cellulases required xylanase supplementation for effective hydrolysis of pretreated substrates containing higher amounts of xylan. It was apparent that the xylan content influenced both the enzyme requirements for hydrolysis and the recovery of sugars during the pretreatment process. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Preparation,characterization and luminescent properties of dense nano‐silica hybrids loaded with 1,8‐naphthalic anhydride

Novel luminescent dense nano‐silica hybrid materials (DNSS) modified with different amounts of (3‐aminopropyl)triethoxysilane (APTES) and 1,8‐naphthalic anhydride (NA) were successfully synthesized via two steps combined with post‐grafting methods. Powder X‐ray diffraction (XRD), N₂‐sorption analysis, Fourier transform infrared (FT‐IR) spectroscopy, transmission electron microscopy (TEM), thermogravimetric analysis (TGA), photoluminescence (PL) spectroscopy and elemental analysis, as well as time‐resolved decays were employed to characterize the resultant hybrid materials. The results revealed that luminescent organic molecules had been successfully loaded onto the amine‐modified surface of nano‐silica spheres. In addition, their fluorescence intensity and characteristic peak of emission spectra changed with increasing amount of APTES and NA additive. In particular, the characteristic peak showed a red shift from 390 to 450 nm, however, this was inconsistent with results calculated on the basis of the elemental analysis data, most probably because of the dispersion behaviors of NA molecules from the aggregating to the monolayer state. These observations demonstrated the existence of a quantum confinement effectiveness of NA–DNSS samples, and therefore a possible mechanism was put forward. Copyright © 2013 John Wiley & Sons, Ltd.     

Binding modules alter the activity of chimeric cellulases: Effects of biomass pretreatment and enzyme source

Improving the catalytic activity of cellulases requires screening variants against solid substrates. Expressing cellulases in microbial hosts is time‐consuming, can be cellulase specific, and often leads to inactive forms and/or low yields. These limitations have been obstacles for improving cellulases in a high‐throughput manner. We have developed a cell‐free expression system and used it to express 54 chimeric bacterial and archaeal endoglucanases (EGs), with and without cellulose binding modules (CBMs) at either the N‐ or C‐terminus, in active enzyme yields of 100–350 µg/mL. The platform was employed to systematically study the role of CBMs in cellulose hydrolysis toward a variety of natural and pretreated solid substrates, including ionic‐liquid pretreated Miscanthus and AFEX‐pretreated corn stover. Adding a CBM generally increased activity against crystalline Avicel, whereas for pretreated substrates the effect of CBM addition depended on the source of cellulase. The cell‐free expression platform can thus provide insights into cellulase structure‐function relationships for any substrate, and constitutes a powerful discovery tool for evaluating or engineering cellulolytic enzymes for biofuels production. Biotechnol. Bioeng. 2010;107:601–611. © 2010 Wiley Periodicals, Inc.     

β‐poly(l‐malic acid) production by fed‐batch culture of Aureobasidium pullulans ipe‐1 with mixed sugars

β‐poly(l ‐malic acid) (PMLA) is a biopolyester, which has attracted growing attention due to its potential applications in medicine and other industries. In this study, the biosynthetic pathway of PMLA and the fermentation strategies with mixed sugars were both investigated to enhance PMLA production by Aureobasidium pullulans ipe‐1. Metabolic intermediates and inhibitors were used to study the biosynthetic pathway of PMLA. It showed that exogenous addition of l ‐malic acid, succinic acid, TFA, and avidin had negligible effect on PMLA production, while pyruvic acid and biotin were the inhibitors, indicating that PMLA biosynthesis was probably related to phosphoenolpyruvate via oxaloacetate catalyzed by phosphoenolpyruvate carboxylase. Sucrose was suitable for achieving the highest PMLA concentration, while fructose generated a higher yield of PMLA (PMLA produced per biomass). Furthermore, the fed‐batch culture using fed solution with different sugar mixture for PMLA production was implemented. During the fed‐batch culture with mixed solution, fructose could increase PMLA production. Compared with the batch culture, the feeding with mixed sugar (sucrose and glucose) increased PMLA concentration by 23.9%, up to 63.2 g/L, and the final volume of the broth was increased by 25%. These results provide a good reference for process development and optimization of PMLA production.     

Enhanced hydrogen and 1,3‐propanediol production from glycerol by fermentation using mixed cultures

The conversion of glycerol into high value products, such as hydrogen gas and 1,3‐propanediol (PD), was examined using anaerobic fermentation with heat‐treated mixed cultures. Glycerol fermentation produced 0.28 mol‐H₂/mol‐glycerol (72 mL‐H₂/g‐COD) and 0.69 mol‐PD/mol‐glycerol. Glucose fermentation using the same mixed cultures produced more hydrogen gas (1.06 mol‐H₂/mol‐glucose) but no PD. Changing the source of inoculum affected gas production likely due to prior acclimation of bacteria to this type of substrate. Fermentation of the glycerol produced from biodiesel fuel production (70% glycerol content) produced 0.31 mol‐H₂/mol‐glycerol (43 mL H₂/g‐COD) and 0.59 mol‐PD/mol‐glycerol. These are the highest yields yet reported for both hydrogen and 1,3‐propanediol production from pure glycerol and the glycerol byproduct from biodiesel fuel production by fermentation using mixed cultures. These results demonstrate that production of biodiesel can be combined with production of hydrogen and 1,3‐propanediol for maximum utilization of resources and minimization of waste. Biotechnol. Bioeng. 2009; 104: 1098–1106. © 2009 Wiley Periodicals, Inc.     

Influence of steam pretreatment severity on post‐treatments used to enhance the enzymatic hydrolysis of pretreated softwoods at low enzyme loadings

It is recognized that some form of post‐treatment will usually be required if reasonable hydrolysis yields (>60%) of steam pretreated softwood are to be achieved when using low enzyme loadings (5 FPU/g cellulose). In the work reported here we modified/removed lignin from steam pretreated softwood while investigating the influence that the severity of pretreatment might have on the effectiveness of subsequent post‐treatments. Although treatment at a lower severity could provide better overall hemicellulose recovery, post‐treatment was not as effective on the cellulosic component. Pretreatment at medium severity resulted in the best compromise, providing reasonable recovery of the water soluble hemicellulose sugars and the use of post‐treatment conditions that significantly increased the enzymatic hydrolysis of the water insoluble cellulosic component. Post‐treatment with alkaline hydrogen peroxide or neutral sulfonation resulted in 62% cellulose hydrolysis at an enzyme loading of 5 FPU/g cellulose, which was four times greater than was obtained when the cellulosic fraction was not post‐treated. When the enzyme loading was increased to 15 FPU/g cellulose, the post‐treated cellulosic fraction was almost completely hydrolyzed to glucose. Despite the higher lignin content (44%) of the sulfonated substrate, similar hydrolysis yields to those achieved after alkaline peroxide post‐treatment (14% lignin content) indicated that, in addition to lignin removal, lignin modification also plays an important role in influencing the effectiveness of hydrolysis when low enzyme loadings are used. Biotechnol. Bioeng. 2011;108: 2300–2311. © 2011 Wiley Periodicals, Inc.     

Utilizing a nano‐sorbent for the selective solid‐phase extraction of vanillic acid prior to its determination by photoluminescence spectroscopy

Vanillic acid (VA) is a phenolic acid, and acts as a natural antioxidant in fruits, vegetables and plants. The extraction and determination of trace levels of VA in plants is important, because stimulation of protein synthesis and activation of antioxidant enzymes occur in the presence of phenolic acids at trace levels. In this research, a photoluminescence spectroscopic method was developed for the quantification of VA in plant samples after separation and pre‐concentration. Selective extraction of VA from aqueous solution was performed using a solid‐phase extraction column packed with nickel–aluminum layered double hydroxide as a nano‐sorbent. After elution of extracted analyte from the column using 3 mL of a 3 mol/L NaOH solution, its concentration was determined spectrofluorometrically at λ_em = 357 nm with excitation at λ_ex = 280 nm. The spectrofluorometry method gave a linear response for VA within the range 20.0–900.0 µg/L, with a correlation coefficient of 0.9982. The limit of detection and sorption capacity were 7.6 µg/L and 66.2 mg/g, respectively. The method was validated by comparing the obtained results with gas chromatographic data. This method was used to determine VA in Chenopodium album and Prangos asperula plants. Copyright © 2014 John Wiley & Sons, Ltd.     

1,3‐propanediol production from glucose by mixed‐culture fermentation of Zygosacharomyces rouxii and Klebsiella pneumonia

1,3‐propanediol is an important chemical widely used in polymer production. In this study, two strains, Zygosacharomyces rouxii JL2011 and Klebsiella pneumoniae S6, were used as a mixed culture for 1,3‐propanediol production directly from glucose. Two important parameters including inoculation time of K. pneumoniae S6 at stage of mixed culture and initial cell ratio of Z. rouxii JL2011 to K. pneumoniae S6 in mixed fermentation were optimized in culture flasks. In those experiments, the best results were obtained with a yield of 6.8 g/L 1,3‐propanediol from glucose when K. pneumoniae S6 was inoculated after 48 h in the culture of Z. rouxii JL2011 by mixed culture of Z. rouxii JL2011 and K. pneumoniae S6 with initial cell ratio of 1:200. In a 7‐L bioreactor, the maximum 1,3‐propanediol production could reach up to 15.2 g/L. Thus, this study presents an effective process for 1,3‐propanediol microbial production from glucose by using mixed culture of Z. rouxii JL2011 and K. pneumoniae S6. This work does not only demonstrate a new way to produce 1,3‐propanediol from a low‐cost feedstock, but may also make a valuable contribution to the development of a cost‐effective fermentation based on renewable resources.