Gas phase ethyl acetate production in a batch bioreactor

Gas phase ethyl acetate production was studied using a porcine pancreatic lipase powder. It was observed that gaseous ethyl acetate was produced from gaseous ethanol and acetic acid. Accordingly, the effects of amount of lipase powder, gaseous ethanol and acetic acid concentrations, and reaction temperature on the performance of a batch bioreactor were investigated. Apparent Michaelis-Menten constant of ethanol was 0.163 [μM] and there was no inhibition by ethanol over the range investigated. As acetic acid concentration increased, ethyl acetate production increased to a maximum, then decreased, thus suggesting the inhibition effects by acetic acid. Over the reaction temperature of 25–55?°C, activation energy was calculated as 3.93 kcal/gmol and initial reaction rate was obtained as follows: r?=?75.7 exp(?1975.7/T) [μM/mg of lipase/hr]     

Ethanol production from rice hull using Pichia stipitis and optimization of acid pretreatment and detoxification processes

The goal of this study was to produce ethanol from rice hull hydrolysates (RHHs) using Pichia stipitis strains and to optimize dilute acid hydrolysis and detoxification processes by response surface methodology (RSM). The optimized conditions were found as 127.14°C, solid:liquid ratio of 1:10.44 (w/v), acid ratio of 2.52% (w/v), and hydrolysis time of 22.01 min. At these conditions, the fermentable sugar concentration was 21.87 g/L. Additionally, the nondetoxified RHH at optimized conditions contained 865.2 mg/L phenolics, 24.06 g/L fermentable sugar, no hydroxymethylfurfural (HMF), 1.62 g/L acetate, 0.36 g/L lactate, 1.89 g/L glucose, and 13.49 g/L fructose + xylose. Furthermore, RHH was detoxified with various methods and the best procedures were found to be neutralization with CaO or charcoal treatment in terms of the reduction of inhibitory compounds as compared to nondetoxified RHH. After detoxification procedures, the content of hydrolysates consisted of 557.2 and 203.1 mg/L phenolics, 19.7 and 21.60 g/L fermentable sugar, no HMF, 0.98 and 1.39 g/L acetate, 0 and 0.04 g/L lactate, 1.13 and 1.03 g/L glucose, and 8.46 and 12.09 g/L fructose + xylose, respectively. Moreover, the base‐line mediums (control), and nondetoxified and detoxified hydrolysates were used to produce ethanol by using P. stipitis strains. The highest yields except that of base‐line mediums were achieved using neutralization (35.69 and 38.33% by P. stipitis ATCC 58784 and ATCC 58785, respectively) and charcoal (37.55% by P. stipitis ATCC 58785) detoxification methods. Results showed that the rice hull can be utilized as a good feedstock for ethanol production using P. stipitis. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:872–882, 2016     

Construction of a flocculating yeast for fructose production from inulin

Construction of flocculating yeast lacking for fructose utilisation was realised by integration of the FLO1 flocculation gene in the ribosomal DNA of an hexokinase deficient (hxk1, hxk2) Saccharomyces cerevisiae strain (ATCC36859). Simultaneous production of ethanol and fructose was obtained from glucose/fructose mixtures or from hydrolysed Jerusalem artichoke extracts using the transformed yeast in batch fermentations and in a continuous reactor with internal biomass recycle. This allowed the production of 5 g ethanol/L and 48 g sugars/L containing up to 99 % fructose from diluted hydrolysed Jerusalem artichoke extracts containing 60 g sugars/L. © Rapid Science Ltd. 1998     

Improved bioconversion of lignocellulosic biomass by Saccharomyces cerevisiae engineered for tolerance to acetic acid

Lignocellulosic biomass has considerable potential for the production of fuels and chemicals as a promising alternative to conventional fossil fuels. However, the bioconversion of lignocellulosic biomass to desired products must be improved to reach economic viability. One of the main technical hurdles is the presence of inhibitors in biomass hydrolysates, which hampers the bioconversion efficiency by biorefinery microbial platforms such as Saccharomyces cerevisiae in terms of both production yields and rates. In particular, acetic acid, a major inhibitor derived from lignocellulosic biomass, severely restrains the performance of engineered xylose‐utilizing S. cerevisiae strains, resulting in decreased cell growth, xylose utilization rate, and product yield. In this study, the robustness of XUSE, one of the best xylose‐utilizing strains, was improved for the efficient conversion of lignocellulosic biomass into bioethanol under the inhibitory condition of acetic acid stress. Through adaptive laboratory evolution, we successfully developed the evolved strain XUSAE57, which efficiently converted xylose to ethanol with high yields of 0.43–0.50 g ethanol/g xylose even under 2–5 g/L of acetic stress. XUSAE57 not only achieved twofold higher ethanol yields but also improved the xylose utilization rate by more than twofold compared to those of XUSE in the presence of 4 g/L of acetic acid. During fermentation of lignocellulosic hydrolysate, XUSAE57 simultaneously converted glucose and xylose with the highest ethanol yield reported to date (0.49 g ethanol/g sugars). This study demonstrates that the bioconversion of lignocellulosic biomass by an engineered strain could be significantly improved through adaptive laboratory evolution for acetate tolerance, which could help realize the development of an economically feasible lignocellulosic biorefinery to produce fuels and chemicals.     

Conversion of biomass hydrolysates and other substrates to ethanol and other chemicals by Lactobacillus buchneri*

Aims: A Lactobacillus buchneri strain NRRL B‐30929 can convert xylose and glucose into ethanol and chemicals. The aims of the study were to survey three strains (NRRL B‐30929, NRRL 1837 and DSM 5987) for fermenting 17 single substrates and to exam NRRL B‐30929 for fermenting mixed substrates from biomass hydrolysates. Methods and Results: Mixed acid fermentation was observed for all three L. buchneri strains using various carbohydrates; the only exception was uridine which yielded lactate, acetate and uracil. Only B‐30929 is capable of utilizing cellobiose, a desired trait in a potential biocatalyst for biomass conversion. Flask fermentation indicated that the B‐30929 strain can use all the sugars released from pretreated hydrolysates, and producing 1·98–2·35 g l^?1 ethanol from corn stover hydrolysates and 2·92–3·01 g l^?1 ethanol from wheat straw hydrolysates when supplemented with either 0·25× MRS plus 1% corn steep liquor or 0·5× MRS. Conclusions: The L. buchneri NRRL B‐30929 can utilize mixed sugars in corn stover and wheat straw hydrolysates for ethanol and other chemical production. Significance and Impact of the Study: These results are valuable for future research in engineering L. buchneri NRRL B‐30929 for fermentative production of ethanol and chemicals from biomass.     

Lantana camara for fuel ethanol production using thermotolerant yeast

AIM: Evaluation of Lantana camara's use as feedstock for fuel ethanol production. METHODS AND RESULTS: Lantana camara plant material was hydrolysed with 1% sulfuric acid for 18 h at room temperature, followed by heat treatment of 121 degrees C for 20 min. Hemicellulosic hydrolyzate was separated and used for detoxification by ethyl acetate and overliming. Cellulosic fraction was hydrolysed with Aspergillus niger crude cellulase enzyme for 18 h at 55 degrees C. Using 15% (dw/v) substrate 73 g l(-1) total reducing sugars were obtained to give 78.7% hydrolysis of carbohydrate content. Acid and enzyme hydrolyzates were mixed equally and used for fermentation with thermotolerant Saccharomyces cerevisiae (VS(3)). Yeast fermented L. camara hydrolyzate well with a fermentation efficiency of 83.7% to give an ethanol yield of 0.431 +/- 0.018 g ethanol pre g sugar and productivity of 0.5 +/- 0.021 g l(-1) h(-1). CONCLUSIONS: Even though inhibitors were present in L. camara hydrolyzate, maximum sugars were utilized by thermotolerant yeast. SIGNIFICANCE AND IMPACT OF THE STUDY: Use of L. camara for fuel ethanol production with improved strains and detoxification can be recommended.     

Production of ethyl acetate from dilute ethanol solutions by Candida utilis

The conversion of ethanol to ethyl acetate has an advantage as a method of ethanol recovery since ethyl acetate is amenable to simple solvent extraction. The potential of Candida utilis in this conversion was studied. The kinetics of accumulation of ethanol and ethyl acetate in glucose-grown C. utilis showed that ester formation resulted from ethanol utilization under appropriate aeration and was inhibited by Fe(3+) supplementation. Candida utilis converted ethanol to ethyl acetate optimally at pH 5.0-7.0. The five-hour rate of ester production increased as the ethanol concentration increased to 10 g/L, and rapidly declined to zero at concentrations exceeding 35 g/L. Thus, C. utilis has potential to recover dilute ethanol in the form of ethyl acetate.     

Effect of various factors on ethanol yields from lignocellulosic biomass by Thermoanaerobacterium AK₁₇

The ethanol production capacity from sugars and lignocellulosic biomass hydrolysates (HL) by Thermoanaerobacterium strain AK(17) was studied in batch cultures. The strain converts various carbohydrates to, acetate, ethanol, hydrogen, and carbon dioxide. Ethanol yields on glucose and xylose were 1.5 and 1.1 mol/mol sugars, respectively. Increased initial glucose concentration inhibited glucose degradation and end product formation leveled off at 30 mM concentrations. Ethanol production from 5 g L(-1) of complex biomass HL (grass, hemp, wheat straw, newspaper, and cellulose) (Whatman paper) pretreated with acid (0.50% H(2) SO(4)), base (0.50% NaOH), and without acid/base (control) and the enzymes Celluclast and Novozyme 188 (0.1 mL g(-1) dw; 70 and 25 U g(-1) of Celluclast and Novozyme 188, respectively) was investigated. Highest ethanol yields (43.0 mM) were obtained on cellulose but lowest on hemp leafs (3.6 mM). Chemical pretreatment increased ethanol yields substantially from lignocellulosic biomass but not from cellulose. The influence of various factors (HL, enzyme, and acid/alkaline concentrations) on end-product formation from 5 g L(-1) of grass and cellulose was further studied to optimize ethanol production. Highest ethanol yields (5.5 and 8.6 mM ethanol g(-1) grass and cellulose, respectively) were obtained at very low HL concentrations (2.5 g L(-1)); with 0.25% acid/alkali (v/v) and 0.1 mL g(-1) enzyme concentrations. Inhibitory effects of furfural and hydroxymethylfurfural during glucose fermentation, revealed a total inhibition in end product formation from glucose at 4 and 6 g L(-1), respectively.     

Selection of yeast strain and fermentation conditions for high-yield ethanol production from lactose and concentrated whey

A total of 65 yeast strains were screened for their ability to grow and ferment lactose in a standard DURHAM tube test at 30 °C. Based on the kinetic parameters for lactose and whey lactose fermentations in shake flask cultures, the strain Candida psedotropicalis 65 was chosen for further studies. Some of the cultural parameters affecting ethanolic fermentations on lactose were standardized. At an initial lactose concentration of 100–120 g/l in the medium containing concentrated whey or lactose, at 40 °C and within 48 h, the selected strain reached an ethanol concentration of 41–59 g/l, an ethanol productivity of 1.3–3.0 g/l/h, a lactose consumption of 99%, an ethanol yield 0.4–0.49 g/g and a biomass yield of 0.027 g/g.     

Continous ethyl acetate production by Kluyveromyces fragilis on whey permeate

The synthesis of ethyl acetate by Kluyveromyces fragilis on diluted whey permeate was studied. Ethanol, lactose and O₂ are the direct precursors for ethyl acetate synthesis by this yeast. Ethyl acetate production is affected by many parameters, particularly the carbon/nitrogen (C/N) ratio, Tween 80 and iron. Ethyl acetate synthesis is optimum for C/N = 45. Tween 80 lowered slightly the level of ethyl acetate whereas iron completely stopped ethyl acetate production. The level of ethanol in the feed, the dissolved O₂ (DO) and dilution rate (D) were also optimised. Thus at D = 0.24 h ^–1, for 4 g/l of ethanol in the feed and 40% DO, the productivity of ethyl acetate was optimal (0.7 g/l per hour). Correspondence to: A. Miclo     

酱香型白酒酿造拜耳接合酵母生理代谢特征及其与地衣芽孢杆菌相互作用

【目的】拜耳接合酵母(Zygosaccharomyces bailii)是酱香型白酒酿造过程优势菌株。通过研究拜耳接合酵母酿造相关生理代谢特征及其与酿造环境中其它功能菌株的相互作用,探索其在白酒酿造过程中的贡献。【方法】从酱香酒酿造中筛选一株性能优良的拜耳接合酵母,比较其与模式菌株(Z.bailii,ATCC 58445)的生理代谢特征。通过组合发酵研究其与产酱香特征风味细菌地衣芽孢杆菌的相互作用。【结果】从酱香型酒醅中筛选得到一株性状优良的拜耳接合酵母(Z.bailii 15),可耐受p H 2.0和37°C高温及8%酒精浓度(体积比),较模式株更适应酿造环境,酒精产量(33.58 g/L)也远高于模式株(19.04 g/L),且与酱香型白酒酿酒酵母MT1(34.29 g/L)相当。该菌可产多种风味物质,与模式株相比,独特产生法呢醇、十二醇、2-壬醇、2-乙基己醇、癸酸、月桂酸、辛酸、辛酸乙酯、苯乙酮、4-叔丁基苯酚。共培养体系中,30°C条件下地衣芽孢杆菌对拜耳接合酵母生长影响不大,而在37°C地衣芽孢杆菌抑制拜耳接合酵母生长。此外,地衣芽孢杆菌对拜耳接合酵母乙醇转化率有促进作用,共培养体系风味物质种类及含量也都受到很大影响。【结论】拜耳接合酵母在酱香型白酒酿造体系中产酒精、产风味方面表现优异,对酱香型白酒生产具有重要贡献。     

Fed-batch mode in shake flasks by slow-release technique

Most industrial production processes are performed in fed-batch operational mode. In contrast, the screenings for microbial production strains are run in batch mode which results in completely different physiological conditions than relevant for production conditions. This may lead to wrong selections of strains. Silicone elastomer discs containing glucose crystals were developed to realize fed-batch fermentation in shake flasks. No other device for feeding was required. Glucose was fed in this way to Hansenula polymorpha cultures controlled by diffusion. Two strains of H. polymorpha were investigated in shake flasks: the wild-type strain (DSM 70277) and a recombinant strain pC10-FMD (P(FMD)-GFP). The oxygen transfer rate (OTR) and respiratory quotient (RQ) of the cultures were monitored online in shake flasks with a Respiration Activity Monitoring System (RAMOS). Formation of biomass and green fluorescent protein (GFP), pH-drift and the metabolite dynamics of glucose, ethanol and acetic acid were measured offline. With the slow-release technique overflow metabolism could be reduced leading to an increase of 85% in biomass yield. To date, 23.4 g/L cell dry weight of H. polymorpha could be achieved in shake flask. Biomass yields of 0.38-0.47 were obtained which are in the same magnitude of laboratory scale fermentors equipped with a substrate feed pump. GFP yield could be increased by a factor of 35 in Syn6-MES mineral medium. In fed-batch mode 88 mg/L GFP was synthesized with 35.9 g/L fed glucose. In contrast, only 2.5 mg/L with 40 g/L metabolized glucose was revealed in batch mode. In YNB mineral medium over 420-fold improvement in fed-batch mode was achieved with 421 mg/L GFP at 41.3 g/L fed glucose in comparison to less than 1 mg/L in batch mode with 40 g/L glucose.     

Isolation and characterization of a Trichodermastrain capable of fermenting cellulose to ethanol

The direct fermentation of cellulosic biomass to ethanol has long been a desired goal. To this end, we screened the environment for fungal strains capable of this conversion when grown on minimal medium. One strain, identified as a member of the genus Trichoderma and designated strain A10, was isolated from cow dung and initially produced about 0.4 g ethanol l(-1). This strain cannot grow on any substrate under anaerobic conditions, but can ferment microcrystalline cellulose or several sugars to ethanol. Ethanol accumulation was eventually increased, by selection and the use of a vented fermentation flask, to 2 g l(-1) when the fermentation was carried out in submerged culture in minimal medium. The highest levels of ethanol, >5.0 g l(-1), were obtained by the fermentation of glucose. Little ethanol was produced by the fermentation of xylose, although other fermentation products such as succinate and acetate were observed. Strain A10 was also found to utilize (aerobically) a wide range of carbon sources. In addition, auxotrophic mutants were generated and used to demonstrate parasexuality by complementation between auxotrophs and between morphological mutants. The ability of this strain to use a wide variety of carbohydrates (including crystalline cellulose) combined with its minimal nutrient requirements and the availability of a genetic system suggests that the strain merits further investigation of its ability to convert biomass to ethanol.     

Leishmania donovani: Metabolite mapping of promastigotes using proton nuclear magnetic resonance spectroscopy

Proton nuclear magnetic resonance spectroscopy was used for studying the intracellular metabolite profile of promastigotes of Leishmania donovani. The major intracellular metabolites observed in the promastigotes were acetate, alanine, succinate, glycine, -glycerophosphorylcholine, acetoacetate, arginine and ethanol. A comparative study of the intracellular metabolite profile of promastigotes of different strains of L. donovani showed that, all the major intracellular metabolites were present in promastigotes of different strains. A quantitative estimation of metabolites showed a strain specific (Finger print) metabolite profile which can be used for strain/species identification/differentiation.     

Laboratory metabolic evolution improves acetate tolerance and growth on acetate of ethanologenic Escherichia coli under non-aerated conditions in glucose-mineral medium

In this work, Escherichia coli MG1655 was engineered to produce ethanol and evolved in a laboratory process to obtain an acetate tolerant strain called MS04 (E. coli MG1655: ΔpflB, ΔadhE, ΔfrdA, ΔxylFGH, ΔldhA, PpflB::pdc _Zm -adhB _Zm , evolved). The growth and ethanol production kinetics of strain MS04 were determined in mineral medium, mainly under non-aerated conditions, supplemented with glucose in the presence of different concentrations of sodium acetate at pH?7.0 and at different values of acid pH and a constant concentration of sodium acetate (2?g/l). Results revealed an increase in the specific growth rate, cell mass formation, and ethanol volumetric productivity at moderate concentrations of sodium acetate (2–10?g/l), in addition to a high tolerance to acetate because it was able to grow and produce a high yield of ethanol in the presence of up to 40?g/l of sodium acetate. Genomic analysis of the ΔpflB evolved strain identified that a chromosomal deletion of 27.3?kb generates the improved growth and acetate tolerance in MG1655 ΔpflB derivative strains. This deletion comprises genes related to the respiration of nitrate, repair of alkylated DNA and synthesis of the ompC gene coding for porin C, cytochromes C, thiamine, and colonic acid. Strain MS04 is advantageous for the production of ethanol from hemicellulosic hydrolysates that contain acetate.     

Fermentative capability and aroma compound production by yeast strains isolated from Agave tequilana Weber juice

Five yeast strains isolated from agave juice were studied for their fermentative and aromatic capacity. The experiments were performed using agave juice supplemented with ammonium sulphate, as is commonly done in tequila distilleries. Three strains classified as Saccharomyces cerevisiae showed high biomass and ethanol production, as well as higher ethanol tolerance than those classified as Kloeckera africana and Kloeckera apiculata, which showed scarce growth. The results suggest that Kloeckera strains were affected by nutritional limitation and/or toxic compounds present in agave juice. Agave juice analyses showed a lower amino acid content than those reported in grape juice. S. cerevisiae strains produced predominantly amyl and isoamyl alcohols, n-propanol, 2-phenyl ethanol, succinic acid, glycerol, methanol, isoamyl acetate, ethyl hexanoate, acetaldehyde and isobutanol, whereas Kloeckera strains showed a high production of acetic acid, 2-phenyl ethyl acetate and ethyl acetate. The methanol concentration was significantly different among the yeasts studied. The diversity between three S. cerevisiae strains were higher for the aromatic profile than for genetic level and kinetic parameter. On the other hand, the diversity of Kloeckera yeasts were lower than Saccharomyces yeasts even when belonging to two different species.     

Kinetics of the selective fermentation of glucose from glucose/fructose mixtures using Saccharomyces cerevisiae ATCC 36859

The kinetics of batch fermentation during the growth of S. cerevisiae ATCC 36859 was studied in various glucose/fructose mixtures. It was found that the growth is inhibited equally by glucose and fructose even though fructose is not consumed to any large extent by the yeast under the conditions tested here. The inhibition of growth by the substrate and ethanol is represented by linear equations. These equations were combined with the MONOD expression in order to formulate equations for the biomass growth, glucose and fructose consumption and ethanol production. Parameter estimates were obtained by fitting these equations to batch fermentation data and so developing models which indicate that the growth is completely inhibited when 62 g/l ethanol is produced by the yeast, while glucose consumption and ethanol production continue up to an ethanol concentration of 152 g/l. Products containing a high concentration of fructose are best produced by using a high initial biomass concentration.     

Criteria for the selection of strains of entomopathogenic fungi Verticillium lecanii for solid state cultivation

The objective of this study was the selection of strains of Verticillium lecanii for solid-state fermentation (SSF) containing cuticle of Sphenarium purpurascens as an inducer of proteases and chitinases. The selection criteria were: growth at low water activity (a_W), enzymatic activities (proteases and chitinases) and CO₂ production rate. Three strains of V. lecanii were studied ATCC 26854, ATCC 46578 and a wild strain (WS). The strains ATCC 26854 and WS presented the best biomass production at low a_W (0.957). Highest rates of clearing zones of casein and chitin were obtained for strains ATCC 26854 and WS. Best results of CO₂ production in SSF were obtained by using V. lecanii ATCC 26854 which showed a maximal value (2.3 mg CO₂ g IDM⁻¹ h⁻¹) at 36 h of cultivation. Although clearing zones of casein and chitin were partial criteria for strain selection. It was concluded that growth a low water activities and CO₂ production rate, were more reliable criteria for selecting strains of V. lecanii for solid state culture using cuticle of insect as the main C and N source.     

Pyruvic acid production by a lipoic acid auxotroph of Escherichia coliW1485

A lipoic acid auxotroph of Escherichia coli K-12, strain W1485lip2 (ATCC25645), produced pyruvic acid aerobically from glucose under the lipoic acid-deficient conditions, while the prototrophic parent strain, W1485 (ATCC12435), produced 2-oxoglutaric acid as the main product. The mechanism of the pyruvic acid production by strain W1485lip2 was found to be the impaired oxidative decarboxylation of pyruvic acid caused by the decrease in the activity of pyruvate dehydrogenase complex under the conditions of lipoic acid deficiency. Under the optimum culture conditions using the pH-controlled jar fermentor, 25.5?g/l pyruvic acid was obtained from 50?g/l glucose after the culture for 32–40?h at pH?6.0. The relationship between the pyruvic acid productivity and the pyruvate dehydrogenase complex activity in jar-fermentor culture was discussed.     

Increased ethanol production by metabolic modulation of cellulose fermentation in Clostridium thermocellum

Significant quantitative differences in ethanol yields along with repression in acetic acid production were observed in Clostridium thermocellum strains SS21 and SS22 in the presence of H 2 , acetone and sodium azide. Exogenous H 2 addition (1.0 atm) increased the ethanol yields to 0.40 g/g and ethanol to acetate ratio to 5.75 in strain SS21 but was inhibitory in strain SS22. Addition of acetone reversed the inhibition caused by H 2 and increased the ethanol yields and ethanol to acetate ratio of strain SS22 up to 0.40 g/g and 7.9, respectively. Enhancement in ethanol yields up to 0.40 g/g and 0.41 g/g and ethanol to acetate ratio up to 3.63 and 8.1 were observed in the presence of 0.2 mM and 0.15 mM concentration of sodium azide by strains SS21 and SS22, respectively.