Bacterial cellulose production by fed-batch fermentation in molasses medium

Batch and fed-batch fermentations for bacterial cellulose (BC) production using molasses as a carbon source by Acetobacter xylinum BPR2001 were carried out in a jar fermentor. For improvement of BC production, molasses was subjected to H2SO4-heat treatment. The maximum BC concentration by this treated molasses increased 76%, and the specific growth rate increased 2-fold compared with that by untreated molasses. In batch fermentation, when the initial sugar concentrations of H2SO4-heat-treated molasses were varied from 20 to 70 g/L, the highest value of maximum BC concentration of 5.3 g/L was observed at 20 g/L. BC production in intermittent fed-batch (IFB) fermentation was conducted referring to the data in batch fermentation, and the highest BC production of 7.82 g/L was obtained when 0.2 L of molasses medium was added five times. When continuous fed-batch (CFB) fermentations were conducted, maximum BC concentration was obtained with a feeding rate of 6.3 g-sugar/h, which was derived from the optimal IFB experiment.     

A cost-effective cane molasses medium for enhanced cell-bound phytase production by Pichia anomala

AIM: Formulation of an inexpensive cane molasses medium for improved cell-bound phytase production by Pichia anomala. METHODS AND RESULTS: Cell-bound phytase production by Pichia anomala was compared in synthetic glucose-beef extract and cane molasses media. The yeast was cultivated in 250 ml flasks containing 50 ml of the medium, inoculated with a 12 h-old inoculum (3 x 10(6) CFU ml(-1)) and incubated at 25 degrees C for 24 h at 250 rev min(-1). Different cultural parameters were optimized in cane molasses medium in batch fermentation. The cell-bound phytase content increased significantly in cane molasses medium (176 U g(-1) dry biomass) when compared with the synthetic medium (100 U g(-1) dry biomass). In fed-batch fermentation, a marked increase in biomass (20 g l(-1)) and the phytase yield (3000 U l(-1)) were recorded in cane molasses medium. The cost of production in cane molasses medium was pound 0.006 per 1000 U, which is much lower when compared with that in synthetic medium (pound 0.25 per 1000 U). CONCLUSIONS: An overall 86.6% enhancement in phytase yield was attained in optimized cane molasses medium using fed-batch fermentation when compared with that in synthetic medium. Furthermore, the production in cane molasses medium is cost-effective. SIGNIFICANCE AND IMPACT OF THE STUDY: Phytase yield was improved in cane molasses when compared with the synthetic medium, and the cost of production was also significantly reduced. This enzyme can find application in the animal feed industry for improving the nutritional status of feed and combating environmental pollution.     

Utilization of Molasses Sugar for Lactic Acid Production by Lactobacillus delbrueckii subsp. delbrueckii Mutant Uc-3 in Batch Fermentation

Efficient lactic acid production from cane sugar molasses by Lactobacillus delbrueckii mutant Uc-3 in batch fermentation process is demonstrated. Lactic acid fermentation using molasses was not significantly affected by yeast extract concentrations. The final lactic acid concentration increased with increases of molasses sugar concentrations up to 190 g/liter. The maximum lactic acid concentration of 166 g/liter was obtained at a molasses sugar concentration of 190 g/liter with a productivity of 4.15 g/liter/h. Such a high concentration of lactic acid with high productivity from molasses has not been reported previously, and hence mutant Uc-3 could be a potential candidate for economical production of lactic acid from molasses at a commercial scale.     

Optimization of nutritional supplements for enhanced lactic acid production utilizing sugar refinery by-products

The present study investigated the synergistic effect of nutritional supplements (amino acid and Tween 80) on lactic acid production by Lactobacillus delbruckii utilizing a sugar refinery by product (cane molasses) in a submerged fermentation process. Initially, the effect of individual factors on lactic acid yield was studied by supplementing amino acids and their combinations, Tween 80 and cane molasses at varying concentrations in production medium. A combination of l-phenylalanine and l-lysine gave a maximum lactic acid yield of 47.89?±?0.1 g/L on a dry cell weight basis at individual factor level. Similarly, maximum lactic acid yield was obtained by supplementing the production medium with 40.0 g/L and 2.0 g/L Tween 80 and cane molasses, respectively, at individual factor level. In order to further improve the lactic acid yield, nutritional supplements were optimized by central composite rotatable design (CCRD) using Minitab 15 software. Shake flask cultivation under optimized conditions, i.e., cane molasses (32.40 g/L), Tween 80 (2.0 g/L) and l-phenylalanine and l-lysine (34.0 mg/L) gave a lactic acid yield of 64.86?±?0.2 g/L, corresponding to 95.0 % of the predicted yield of 67.78?±?0.3 g/L. Batch cultivation performed in 7.5 L bioreactor (working volume: 3.0 L) under optimized conditions gave maximum lactic acid yield and productivity of 79.12?±?0.2 g/L and 3.40 g/L·h, which is higher than previous studies with reduced fermentation time. Screening of lactic acid producing bacteria and characterization of lactic acid was also done.     

利用甘蔗糖蜜发酵生产花生四烯酸的研究

通过培养高山被孢霉利用糖蜜来发酵生产花生四烯酸(ARA),研究了不同甘蔗糖蜜预处理方法对ARA发酵生产的影响。研究表明:H2SO4法是最利于ARA发酵生产的糖蜜预处理方法。利用预处理的甘蔗糖蜜发酵生产ARA,通过单因素实验设计,确定了最优的培养条件,包括初始还原糖80 g/L,N源6 g/L,接种量20%,初始pH6.0和培养温度25℃,在此条件下发酵,干细胞质量、油脂含量、ARA产量和糖利用率分别达到28.5 g/L、11.7g/L、3.68 g/L和94.5%。     

Ergosterol production from molasses by genetically modified <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Ergosterol is an economically important metabolite produced by fungi. Recombinant Saccharomyces cerevisiae YEH56(pHXA42) with increased capacity of ergosterol formation was constructed by combined overexpression of sterol C-24(28) reductase and sterol acyltransferase in the yeast strain YEH56. The production of ergosterol by this recombinant strain using cane molasses (CM) as an inexpensive carbon source was investigated. An ergosterol content of 52.6 mg/g was obtained with 6.1 g/l of biomass from CM medium containing 60 g/l of total sugar in 30 h in shake flask. The ergosterol yield was enhanced through the increasing cell biomass by supplementation of urea to a concentration of 6 g/l in molasses medium. Fermentation was performed in 5-l bioreactor using the optimized molasses medium. In batch fermentation, the effect of agitation velocity on ergosterol production was examined. The highest ergosterol yield was obtained at 400 rpm that increased 60.4 mg/l in comparison with the shake flask culture. In fed-batch fermentation, yeast cells were cultivated, firstly, in the starting medium containing molasses with 20 g/l of total sugar, 1.68 g/l of phosphate acid, and 6 g/l of urea (pH 5.4) for 5 h, then molasses containing 350 g/l of total sugar was fed exponentially into the bioreactor to keep the ethanol level in the broth below 0.5%. After 40 h of cultivation, the ergosterol yield reached 1,707 mg/l, which was 3.1-fold of that in the batch fermentation.     

Economical succinic acid production from cane molasses by Actinobacillus succinogenes

In this work, production of succinic acid by Actinobacillus succinogenes CGMCC1593 using cane molasses as a low cost carbon source was developed. In anaerobic bottles fermentation, succinic acid concentration of 50.6+/-0.9 g l(-1) was attained at 60 h using an optimum medium containing molasses pretreated with sulfuric acid, resulting in a succinic acid yield of 79.5+/-1.1% and sugar utilization of 97.1+/-0.6%. When batch fermentation was carried out in a 5-l stirred bioreactor with pretreated molasses, 46.4 g l(-1) of succinic acid was attained at 48 h and faster cells growth was also observed. Fed batch fermentation was performed to minimize the substrate (sugar) inhibition effect, giving 55.2 g l(-1) of succinic acid and 1.15 g l(-1)h(-1) of productivity at 48 h. The present study suggests that the inexpensive cane molasses could be utilized for the economical and efficient production of succinic acid by A. succinogenes.     

响应面法优化甘蔗糖蜜发酵产丁醇

以甘蔗糖蜜为底物,用响应面法对高丁醇比突变菌株拜氏梭菌(Clostridium beijerinckii)ART124发酵生产丁醇的培养条件进行优化.首先利用Plackett - Burman试验设计筛选出影响丁醇生产的3个重要因素CaCO3和NH4 HCO3和K2HPO4的用量,再通过最陡爬坡路径逼近最大向应区域,最后根据响应面中心组合设计理论,确定主要影响因素的最佳条件:CaCO3、NH4HCO3和K2HPO4的质量浓度分别为2.65、2.16和0.43 g/L.利用数学模型分析预测得甘蔗糖蜜质量浓度为30 g/L时,最佳的丁醇产量为8.10 g/L,比优化前提高了53.14％.在最佳工艺条件下得到的实验结果与模型预测值很吻合,说明所建立的模型是有效的.     

Enhanced production of raw starch degrading enzyme using agro-industrial waste mixtures by thermotolerant Rhizopus microsporus for raw cassava chip saccharification in ethanol production

In the present study, solid-state fermentation for the production of raw starch degrading enzyme was investigated by thermotolerant Rhizopus microsporus TISTR 3531 using a combination of agro-industrial wastes as substrates. The obtained crude enzyme was applied for hydrolysis of raw cassava starch and chips at low temperature and subjected to nonsterile ethanol production using raw cassava chips. The agro-industrial waste ratio was optimized using a simplex axial mixture design. The results showed that the substrate mixture consisting of rice bran:corncob:cassava bagasse at 8?g:10?g:2?g yielded the highest enzyme production of 201.6?U/g dry solid. The optimized condition for solid-state fermentation was found as 65% initial moisture content, 35°C, initial pH of 6.0, and 5?×?10⁶ spores/mL inoculum, which gave the highest enzyme activity of 389.5?U/g dry solid. The enzyme showed high efficiency on saccharification of raw cassava starch and chips with synergistic activities of commercial α-amylase at 50°C, which promotes low-temperature bioethanol production. A high ethanol concentration of 102.2?g/L with 78% fermentation efficiency was achieved from modified simultaneous saccharification and fermentation using cofermentation of the enzymatic hydrolysate of 300?g raw cassava chips/L with cane molasses.     

Optimization of process parameters for ethanol production from sugar cane molasses by Zymomonas mobilis using response surface methodology and genetic algorithm

Ethanol is a potential energy source and its production from renewable biomass has gained lot of popularity. There has been worldwide research to produce ethanol from regional inexpensive substrates. The present study deals with the optimization of process parameters (viz. temperature, pH, initial total reducing sugar (TRS) concentration in sugar cane molasses and fermentation time) for ethanol production from sugar cane molasses by Zymomonas mobilis using Box–Behnken experimental design and genetic algorithm (GA). An empirical model was developed through response surface methodology to analyze the effects of the process parameters on ethanol production. The data obtained after performing the experiments based on statistical design was utilized for regression analysis and analysis of variance studies. The regression equation obtained after regression analysis was used as a fitness function for the genetic algorithm. The GA optimization technique predicted a maximum ethanol yield of 59.59 g/L at temperature 31 °C, pH 5.13, initial TRS concentration 216 g/L and fermentation time 44 h. The maximum experimental ethanol yield obtained after applying GA was 58.4 g/L, which was in close agreement with the predicted value.     

重组大肠杆菌利用蔗糖及糖蜜发酵生产丁二酸

富含蔗糖的甘蔗糖蜜可作为制备丁二酸的廉价原料。然而生产丁二酸的潜力菌株大肠杆菌Escherichia coli AFP111不能代谢蔗糖。为了使其具有蔗糖代谢能力,将E.coli W中非PTS蔗糖利用系统蔗糖通透酶的编码基因csc B,果糖激酶的编码基因csc K和蔗糖水解酶的编码基因csc A克隆并表达到AFP111中,获得重组菌株AFP111/p MD19T-csc BKA。经厌氧发酵验证,重组菌株72 h消耗20 g/L蔗糖,丁二酸产量达到12 g/L。在3L发酵罐中采用有氧阶段培养菌体、厌氧阶段发酵的两阶段发酵方式,厌氧发酵30 h,重组菌株以蔗糖和糖蜜为碳源丁二酸产量分别为34 g/L和30 g/L。结果表明,通过外源引入非PTS蔗糖利用系统,重组菌株具有较强的代谢蔗糖生长及合成丁二酸的能力,并且能够利用廉价糖蜜发酵制备丁二酸。     

Production of ethanol from molasses at 45 °C using Kluyveromyces marxianus IMB3 immobilized in calcium alginate gels and poly(vinyl alcohol) cryogel

The thermotolerant, ethanol-producing yeast strain Kluyveromyces marxianus IMB3 has been immobilized in calcium alginate gel and poly(vinyl alcohol) cryogel (PVAC) beads. The immobilized preparations were used as biocatalyst in fed-batch reactor systems for prolonged periods. The substrate utilized in each case consisted of sugar cane molasses diluted to yield a sugar load of 140?g/l. During the first cycle the maximum ethanol concentration produced by the alginate system was 57?g/l, representing 80% of the maximum theoretical yield. In the system employing the PVAC-immobilized biocatalyst, ethanol production increased to a maximum of 52–53?g/l, representing 73% of the maximum theoretical yield. In both cases, maximum ethanol concentration was achieved within a 72-hour period. When each system was operated on a fed-batch basis for a prolonged period of time the average ethanol concentrations produced in the alginate- and the PVAC-immobilized systems were 21 and 45?g/l, respectively. The results suggest that the PVAC-based immobilization system may provide a more practical alternative to alginate for the production of ethanol by K. marxianus IMB3 in continuous or semi-continuous fermentation systems.     

甘蔗渣和糖蜜混合发酵制备燃料丁醇

以抗逆突变株Clostridium beijerinckii IB4为研究对象,葡萄糖为C源,对其进行补料分批发酵过程的优化,同时将该优化工艺应用于甘蔗渣和糖蜜混合发酵制备燃料丁醇。结果表明:在5 L发酵罐中,先加入作为还原糖的甘蔗渣酸解糖液10 g/L,16 h后补加甘蔗糖蜜30 g/L,于35℃、100 r/min发酵50 h,丁醇和总溶剂产量分别达到11.1和15.3 g/L,丁醇比例高达72.5%。     

Influence of cultivation conditions on citrate production by Aspergillus niger in a semi-pilot-scale plant

The influence of some fermentation parameters on the semi-pilot scale (alteration of growth conditions,e.g., sugar concentration, incubation temperature and initial pH) on citrate production was demonstrated in parent and mutant strains ofAspergillus niger. Raw material from sugar industry (cane molasses) was examined as basal fermentation medium in a stirred stainless-steel 15-L fermentor. After growth on medium with 150 g/L sugar, the parent strain produced 51.2 g/L citric acid; the mutant strain achieved production maximum of 96.2 g/L. Comparing the growth, kinetic (volumetric substrate uptake rate, rate of substrate consumption and volumetric productivity rate) and production parameters it was found that the mutant strain grows more rapidly, with slightly changed morphology (intermediate, shiny round pellets with diameter 0.6–0.7 mm), and exhibits a higher citrate production and higher efficiency of sugar utilization.     

Fermentation of biodiesel-derived glycerol by Bacillus amyloliquefaciens: effects of co-substrates on 2,3-butanediol production

Cultivation in glycerol instead of sugars inhibits 2,3-butanediol (2,3-BD) production by Bacillus amyloliquefaciens. In this study, we report that B. amyloliquefaciens readily produces 2,3-BD from biodiesel-derived glycerol in the presence of beet molasses as a co-substrate. Unexpectedly, the molasses stimulated 2,3-BD production and simultaneously reduced the duration of fermentation. Productivity of 2,3-BD was enhanced at the start of fermentation, and yields increased under continuous molasses supply. Subsequently, 2,3-BD production in molasses-supplemented fed-batch culture was observed. Prior to inoculation of fed-batch fermentation culture, 15 g/l of molasses was added to the bioreactor. After 6 h of incubation, the bioreactor was fed with a solution containing 80 % glycerol and 15 % molasses. The 2,3-BD concentration, yield, and productivity significantly improved, reaching 83.3 g/l, 0.42 g/g, and 0.87 g/l·h, respectively. To our knowledge, these results are the highest report for 2,3-BD fermentation from biodiesel-derived glycerol.     

Enhanced propionic acid production from Jerusalem artichoke hydrolysate by immobilized Propionibacterium acidipropionici in a fibrous-bed bioreactor

Propionic acid is an important chemical that is widely used in the food and chemical industries. To enhance propionic acid production, a fibrous-bed bioreactor (FBB) was constructed and Jerusalem artichoke hydrolysate was used as a low-cost renewable feedstock for immobilized fermentation. Comparison of the kinetics of immobilized-cell fermentation using the FBB with those of fed-batch free-cell fermentation showed that immobilized-cell fermentation gave a much higher propionic acid concentration (68.5 vs. 40.6 g/L), propionic acid yield (0.434 vs. 0.379 g/g) and propionic acid productivity (1.55 vs. 0.190 g/L/h) at pH 6.5. Furthermore, repeated batch fermentation, carried out to evaluate the stability of the FBB system, showed that long-term operation with a high average propionic acid yield of 0.483 g/g, high productivity of 3.69 g/L/h and propionic acid concentration of 26.2 g/L were achieved in all eight repeated batches during fermentation for more than 200 h. It is thus concluded that the FBB culture system can be utilized to realize the economical production of propionic acid from Jerusalem artichoke hydrolysate during long-term operation.     

The use of tamarind waste to improve ethanol production from cane molasses

Tamarind wastes such as tamarind husk, pulp, seeds, fruit and the effluent generated during tartaric acid extraction were used as supplements to evaluate their effects on alcohol production from cane molasses using yeast cultures. Small amounts of these additives enhanced the rate of ethanol production in batch fermentations. Tamarind fruit increased ethanol production (9.7%, w/v) from 22.5% reducing sugars of molasses as compared to 6.5% (w/v) in control experiments lacking supplements after 72 h of fermentation. In general, the addition of tamarind supplements to the fermentation medium showed more than 40% improvement in ethanol production using higher cane molasses sugar concentrations. The direct fermentation of aqueous tamarind effluent also yielded 3.25% (w/v) ethanol, suggesting its possible use as a diluent in molasses fermentations. This is the first report, to our knowledge, in which tamarind-based waste products were used in ethanol production. Received 2 April 1998/ Accepted in revised form 13 November 1998     

Production of Fructose and Ethanol from Cane Molasses Using Saccharomyces cerevisiae ATCC 36858

The purpose of this research was to study the possibility of the production of ethanol and enriched fructose syrups from sugar cane molasses using the yeast Saccharomyces cerevisiae ATCC 36858. In batch experiments with a total sugar concentration of between 96.7 g/l and 323.5 g/l, the fructose yield was above 90% of the theoretical value. The ethanol yield and volumetric productivity were in the range of 66% and 77% of the theoretical value, and between 0.53 g ethanol/l × h and 3.15 g ethanol/l × h, respectively. The fructose fraction in the carbohydrates content of the produced syrups was more than 95% when the total initial sugar concentration in the medium was below 273.8 g/l. Some oligosaccharides and glycerol were also produced in all tested media. The maximum amount of produced oligosaccharides including raffinose accounted for 13.4 g/l in the cane molasses medium with 323.5 g/l sugars in the initial phase of the fermentation process. The oligosaccharides produced and raffinose were completely consumed by the end of the fermentation process when the total initial sugar concentration was less than 191.3 g/l. The glycerol concentration was below 9.9 g/l. These findings are useful in the production of ethanol and high fructose syrups using sugar cane molasses.     

Efficient production of butyric acid from Jerusalem artichoke by immobilized Clostridium tyrobutyricum in a fibrous-bed bioreactor

Butyric acid is an important specialty chemical with wide industrial applications. The feasible large-scale fermentation for the economical production of butyric acid requires low-cost substrate and efficient process. In the present study, butyric acid production by immobilized Clostridium tyrobutyricum was successfully performed in a fibrous-bed bioreactor using Jerusalem artichoke as the substrate. Repeated-batch fermentation was carried out to produce butyric acid with a high butyrate yield (0.44 g/g), high productivity (2.75 g/L/h) and a butyrate concentration of 27.5 g/L. Furthermore, fed-batch fermentation using sulfuric acid pretreated Jerusalem artichoke hydrolysate resulted in a high butyric acid concentration of 60.4 g/L, with the yield of 0.38 g/g and the selectivity of ∼85.1 (85.1 g butyric acid/g acetic acid). Thus, the production of butyric acid from Jerusalem artichoke on a commercial scale could be achieved based on the system developed in this work.     

Development and characterization of butanol — Resistant strain ofClostridium acetobutylicum in molasses medium

The production of acetone—butanol—ethanol solvents from cane molasses by locally isolated culture ofClostridium acetobutylicum was limited by butanol toxicity (1.6 mol/L). The butanol tolerance of the isolated culture was increased up to 4.8 mol/L by a serial enrichment method. The butanol-resistant strain had greater efficiency for the conversion of saccharides to mixed solvents and produced 52% more butanol at the expense of acetone and ethanol than the original strain. Moreover, the fermentation profile of parent and butanol-resistant strains in anerobic fermentation of cane molasses demonstrated the superiority of the latter in terms of growth rate, time of onset of butanol production, sugar utilization, final butanol concentration and other parameters.