Itaconic acid production by immobilizedAspergillus terreus on sucrose medium

Summary The itaconic acid production by immobilizedAspergillus terreus TTK 200-5-3 mycelium was optimized in shake flask fermentations using statistical experimental design and empirical modelling. The maximum itaconic acid concentration was calculated to be 13.3 g/l in the investigated experimental area when initial sucrose concentration was 10%, ammonium nitrate concentration 0.275% and initial pH 3. The itaconic acid product concentration using immobilized mycelium was about double of that obtained with the free mycelium.     

Itaconic acid production from wheat chaff by Aspergillus terreus

Biotechnologically produced itaconic acid is an important building block for the chemical industry and still based on pure carbon sources, detoxified molasses or starch hydrolysates. Changing these first generation feedstocks to alternative renewable resources of a second generation implies new challenges for the cultivation process of the industrial itaconic acid producer Aspergillus terreus, which is known to be very sensitive towards impurities. To select a suitable pretreatment method of a second generation feedstock, the influences of different hydrolysate components, like monosaccharides and sugar degradation products, were tested. Particular the impact of those components on itaconic acid yield, productivity, titer and morphology was investigated in detail. Wheat chaff was used as lignocellulosic biomass, which is an agricultural residue. An alkaline pretreatment method with sodium hydroxide at room temperature and a subsequent enzymatic saccharification at pH 4.8 at 50 °C with 10 FPU/g_Biomass Biogazyme 2x proved to be very suitable for a subsequent biotechnological production of itaconic acid. A purification by a cation exchanger of the wheat chaff hydrolysate resulted in a final titer of 27.7 g/L itaconic acid with a yield of 0.41 g/g_{total sugar}.     

Itaconic acid production from xylose in repeated-batch and continuous bioreactors

Summary Itaconic acid production from xylose by immobilized Aspergillus terreus TKK 200-5-2 mycelia was optimized both in repeated shake-flask fermentations and in continuous column bioreactors using statistical experimental design and empirical modelling. Using continuous 9-1 scale air-lift bioreactors, a pH of 2.5, aeration rate of 0.6 v/v per minute and residence time of 160 h gave the highest itaconic acid concentration. In air-lift bioreactors a cubic carrier size of 0.5 cm gave a 3.3-fold higher product concentration than 1-cm cubes. Packed-bed column reactors had a higher production rate than air-lift reactors. Offprint requests to: H. Kautola     

Itaconic acid production by Aspergillus terreus on raw starchy materials

Starchy materials such as corn starch, soft wheat flour, potato flour, cassava flour, sorghum starch, sweet potato and industrial potato flours, either acid or enzymatically hydrolysed, were used as substrates for itaconic acid production by Aspergillus terreus NRRL 1960. Both production and yield were highest on corn starch (18·4 g l⁻¹ and 34·0%, respectively). The degree of hydrolysis had a great influence on acid production which was highest when corn starch was saccharified at 85 DE (dextrose equivalent). In a 3 litre benchtop fermenter, itaconic acid production and productivity were 19·8 g l⁻¹ and 0·13 g l⁻¹ h⁻¹, respectively.     

Itaconic acid production by immobilized Aspergillus terreus with varied metal additions

Summary The effect of trace and alkaline metals on itaconic acid production by polyurethane-foam-immobilized Aspergillus terreus was examined in repeated shake-flask cultures according to a statistical experimental design. An increase in the glucose or copper concentration increased the need for earth alkaline metals. The experimentally obtained highest itaconic acid concentration of 51 g/l from 15% glucose with a total productivity of 3.67 g/l per day was reached during the first 14-day batch fermentation. In the fourth batch the calculated highest itaconic acid concentration of 19 g/l was reached with 25% glucose, 5 g/l of magnesium sulphate, 13 mg/l of copper sulphate and 10 g/l of calcium chloride. The immobilization of the mycelium increased the itaconic acid concentration obtained by as much as eightfold.Offprint requests to: H. Kautola     

ImmobilizedAspergillus terreus in itaconic acid production from glucose

Summary The production of itaconic acid by immobilizedAspergillus terreus TKK 200-5-1 was studied both in shake flask cultures, and in continuous column bioreactors. The effect of glucose and ammonium nitrate concentrations, and of pH were examined using a statistical experimental plan. The highest itaconic acid product concentration could be reached at the highest investigated glucose concentration of 150 g/l and the highest initial pH of 3.75, in the absence of ammonium nitrate. In a continuous packed bed column system operated fro 4.5 months itaconic acid was obtained at a productivity of 328 mg/d per gram of polyurethane foam carrier.     

Itaconic acid production using sago starch hydrolysate by Aspergillus terreus TN484-M1

Sago starch was hydrolyzed using either chemical agents, or enzymes at various pH and concentrations. Hydrolysis using 5000 AUN/ml (0.5%, w/v) glucoamylase exhibited the highest itaconic acid yield up to 0.36 g/g sago starch, whereas hydrolysis using nitric acid at pH 2.0 yielded 0.35 g/g sago starch. The medium was optimized and the composition was (g/l) 140 sago starch, 1.8 corn steep liquor, 1.2 MgSO(4).7H(2)O and 2.9 NH(4)NO(3). When the optimal conditions of hydrolysis and medium composition were applied to itaconic acid production in a 3-l jar fermentor, the itaconic acid production was 48.2 g/l with a yield of 0.34 g/g sago starch. This was filtered from the cultured broth and 37.1g of itaconic acid was recovered with a purity of 97.2%. This result showed that sago starch could be converted to a value-added product with only a simple pretreatment.     

Itaconic acid production using an air-lift bioreactor in repeated batch culture of Aspergillus terreus

Repeated itaconic acid production using an air-lift bioreactor was carried out by three methods—two with cell recycling by means of centrifugation and filtration by a stainless steel filter set inside the bioreactor and one by repeated batch culture without cell recycling. In a flask culture, repeated itaconic acid production was stable for 9 cycles (45 d) and the production rate was 0.47 g/l/h. However, in the air-lift bioreactor, it was difficult to produce itaconic acid in the repeated batch culture with cell recycling for a long period due to a decrease in fluidity resulting from an increase in mycelium concentration. In the method without cell recycling, however, repeated itaconic acid production was stable for 4 cycles (21 d) and the production rate was 0.37 g/l/h.     

Lactic acid production from sugarcane bagasse hydrolysates by Lactobacillus pentosus: Integrating xylose and glucose fermentation

Lactic acid, traditionally obtained through fermentation process, presents numerous applications in different industrial segments, including production of biodegradable polylactic acid (PLA). Development of low cost substrate fermentations could improve economic viability of lactic acid production, through the use of agricultural residues as lignocellulosic biomass. Studies regarding the use of sugarcane bagasse hydrolysates for lactic acid production by Lactobacillus spp. are reported. First, five strains of Lactobacillus spp. were investigated for one that had the ability to consume xylose efficiently. Subsequently, biomass fractionation was performed by dilute acid and alkaline pretreatments, and the hemicellulose hydrolysate (HH) fermentability by the selected strain was carried out in bioreactor. Maximum lactic acid concentration and productivity achieved in HH batch were 42.5 g/L and 1.02 g/L h, respectively. Hydrolyses of partially delignified cellulignin (PDCL) by two different enzymatic cocktails were compared. Finally, fermentation of HH and PDCL hydrolysate together was carried out in bioreactor in a hybrid process: saccharification and co-fermentation with an initial enzymatic hydrolysis. The high fermentability of these process herein developed was demonstrated by the total consumption of xylose and glucose by Lactobacillus pentosus, reaching at 65.0 g/L of lactic acid, 0.93 g/g of yield, and 1.01 g/L h of productivity. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2718, 2019     

Itaconic acid production in microorganisms

Itaconic acid, 2-methylidenebutanedioic acid, is a precursor of polymers, chemicals, and fuels. Many fungi can synthesize itaconic acid; Aspergillus terreus and Ustilago maydis produce up to 85 and 53 g l^?1, respectively. Other organisms, including Aspergillus niger and yeasts, have been engineered to produce itaconic acid. However, the titer of itaconic acid is low compared with the analogous major fermentation product, citric acid, for which the yield is > 200 g l^?1. Here, we review two types of pathway for itaconic acid biosynthesis as well as recent advances by metabolic engineering strategies and process optimization to enhance itaconic acid productivity in native producers and heterologous hosts. We also propose further improvements to overcome existing problems.     

Metabolic engineering of Clostridium tyrobutyricum for enhanced butyric acid production from glucose and xylose

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8 g/L vs. 19.4 g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28 g/L·h vs. 0.16 g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53 g/L·h vs. 0.26 g/L·h) and yield (0.32 g/g vs. 0.28 g/g). When the initial total sugar concentration was ~120 g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4 g/L, yield of 0.43 g/g sugar consumed, productivity of 0.87 g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass.     

Enhancing itaconic acid production by Aspergillus terreus

Aspergillus terreus is successfully used for industrial production of itaconic acid. The acid is formed from cis-aconitate, an intermediate of the tricarboxylic (TCA) cycle, by catalytic action of cis-aconitate decarboxylase. It could be assumed that strong anaplerotic reactions that replenish the pool of the TCA cycle intermediates would enhance the synthesis and excretion rate of itaconic acid. In the phylogenetic close relative Aspergillus niger, upregulated metabolic flux through glycolysis has been described that acted as a strong anaplerotic reaction. Deregulated glycolytic flux was caused by posttranslational modification of 6-phosphofructo-1-kinase (PFK1) that resulted in formation of a highly active, citrate inhibition-resistant shorter form of the enzyme. In order to avoid complex posttranslational modification, the native A. niger pfkA gene has been modified to encode for an active shorter PFK1 fragment. By the insertion of the modified A. niger pfkA genes into the A. terreus strain, increased specific productivities of itaconic acid and final yields were documented by transformants in respect to the parental strain. On the other hand, growth rate of all transformants remained suppressed which is due to the low initial pH value of the medium, one of the prerequisites for the accumulation of itaconic acid by A. terreus mycelium.     

Lactic acid production from xylose by the fungus Rhizopus oryzae

Lignocellulosic biomass is considered nowadays to be an economically attractive carbohydrate feedstock for large-scale fermentation of bulk chemicals such as lactic acid. The filamentous fungus Rhizopus oryzae is able to grow in mineral medium with glucose as sole carbon source and to produce optically pure l(+)-lactic acid. Less is known about the conversion by R. oryzae of pentose sugars such as xylose, which is abundantly present in lignocellulosic hydrolysates. This paper describes the conversion of xylose in synthetic media into lactic acid by ten R. oryzae strains resulting in yields between 0.41 and 0.71 g g⁻¹. By-products were fungal biomass, xylitol, glycerol, ethanol and carbon dioxide. The growth of R. oryzae CBS 112.07 in media with initial xylose concentrations above 40 g l⁻¹ showed inhibition of substrate consumption and lactic acid production rates. In case of mixed substrates, diauxic growth was observed where consumption of glucose and xylose occurred subsequently. Sugar consumption rate and lactic acid production rate were significantly higher during glucose consumption phase compared to xylose consumption phase. Available xylose (10.3 g l⁻¹) and glucose (19.2 g l⁻¹) present in a mild-temperature alkaline treated wheat straw hydrolysate was converted subsequently by R. oryzae with rates of 2.2 g glucose l⁻¹ h⁻¹ and 0.5 g xylose l⁻¹ h⁻¹. This resulted mainly into the product lactic acid (6.8 g l⁻¹) and ethanol (5.7 g l⁻¹).     

Efficient production of L-lactic acid from xylose by Pichia stipitis

Microbial conversion of renewable raw materials to useful products is an important objective in industrial biotechnology. Pichia stipitis, a yeast that naturally ferments xylose, was genetically engineered for l-(+)-lactate production. We constructed a P. stipitis strain that expressed the l-lactate dehydrogenase (LDH) from Lactobacillus helveticus under the control of the P. stipitis fermentative ADH1 promoter. Xylose, glucose, or a mixture of the two sugars was used as the carbon source for lactate production. The constructed P. stipitis strain produced a higher level of lactate and a higher yield on xylose than on glucose. Lactate accumulated as the main product in xylose-containing medium, with 58 g/liter lactate produced from 100 g/liter xylose. Relatively efficient lactate production also occurred on glucose medium, with 41 g/liter lactate produced from 94 g/liter glucose. In the presence of both sugars, xylose and glucose were consumed simultaneously and converted predominantly to lactate. Lactate was produced at the expense of ethanol, whose production decreased to approximately 15 to 30% of the wild-type level on xylose-containing medium and to 70 to 80% of the wild-type level on glucose-containing medium. Thus, LDH competed efficiently with the ethanol pathway for pyruvate, even though the pathway from pyruvate to ethanol was intact. Our results show, for the first time, that lactate production from xylose by a yeast species is feasible and efficient. This is encouraging for further development of yeast-based bioprocesses to produce lactate from lignocellulosic raw material.     

Ribonuclease production by free and immobilizedAspergillus clavatus cells

Several fungal strains ofAspergillus andPenicillium were immobilized by cryopolymerization in polyvinyl alcohol cryogel beads.Aspergillus clavatus was the best producer of extracellular ribonuclease. Enzyme productivity and growth of free and immobilized cells in shake flasks and agitated bioreactor were studied. Ribonuclease production and growth behaviour depended on concentrations of glucose, peptone and soybean in the culture medium. Enzyme production was influenced by agitation and aeration intensity. In repeated batch, shake-flask cultures, the immobilized cells showed 2 to 3.5 times higher enzyme activity than free cells. The optimal conditions in a bioreactor were at 150 rev/min agitation speed and 0.5 vol/vol.min aeration. Enzyme productivity of immobilized cells (237 units/g dry mycelium.h) was 2.1 times higher than the productivity of free cells in a bioreactor, and 2.3 times higher than that of a shake-flask culture.R.J. Manolov is with the Institute of Microbiology, Department of Enzymes, Bulgarian Academy of Sciences, Georgy Bonchev Street 26, 1113 Sofia, Bulgaria.     

Metabolic engineering of Corynebacterium glutamicum for the production of 3-hydroxypropionic acid from glucose and xylose

3-Hydroxypropionic acid (3-HP) is a promising platform chemical which can be used for the production of various value-added chemicals. In this study,Corynebacterium glutamicum was metabolically engineered to efficiently produce 3-HP from glucose and xylose via the glycerol pathway. A functional 3-HP synthesis pathway was engineered through a combination of genes involved in glycerol synthesis (fusion of gpd and gpp from Saccharomyces cerevisiae) and 3-HP production (pduCDEGH from Klebsiella pneumoniae and aldehyde dehydrogenases from various resources). High 3-HP yield was achieved by screening of active aldehyde dehydrogenases and by minimizing byproduct synthesis (gapA^A1GΔldhAΔpta-ackAΔpoxBΔglpK). Substitution of phosphoenolpyruvate-dependent glucose uptake system (PTS) by inositol permeases (iolT1) and glucokinase (glk) further increased 3-HP production to 38.6 g/L, with the yield of 0.48 g/g glucose. To broaden its substrate spectrum, the engineered strain was modified to incorporate the pentose transport gene araE and xylose catabolic gene xylAB, allowing for the simultaneous utilization of glucose and xylose. Combination of these genetic manipulations resulted in an engineered C. glutamicum strain capable of producing 62.6 g/L 3-HP at a yield of 0.51 g/g glucose in fed-batch fermentation. To the best of our knowledge, this is the highest titer and yield of 3-HP from sugar. This is also the first report for the production of 3-HP from xylose, opening the way toward 3-HP production from abundant lignocellulosic feedstocks.     

Alcohol production from glucose and xylose usingEscherichia coli containingZymomonas mobilis genes

Summary AnEscherichia coli strain containing a recombinant plasmid encoding the pyruvate decarboxylase and alcohol dehydrogenase genes fromZymomonas mobilis metabolized glucose and xylose to near theoretical yields of ethanol. Enzyme activity measurements indicate high expression levels of both plasmid-encodedZymomonas proteins in the recombinantE. coli. The expression inE. coli is under the control of a promoter in theZymomonas sequence upstream of the pyruvate decarboxylase gene. The maximum ethanol level, using 4% glucose as substrate, was 1.8% (w/v) in anaerobic conditions. In aerobic conditions the natural repression ofE. coli alcohol dehydrogenase results in less ethanol production from clones expressing onlyZymomonas pyruvate decarboxylase.     

Efficient ethanol production from glucose, lactose, and xylose by recombinant Escherichia coli

Lactose and all of the major sugars (glucose, xylose, arabinose, galactose, and mannose) present in cellulose and hemicellulose were converted to ethanol by recombinant Escherichia coli containing plasmid-borne genes encoding the enzymes for the ethanol pathway from Zymomonas mobilis. Environmental tolerances, plasmid stability, expression of Z. mobilis pyruvate decarboxylase, substrate range, and ethanol production (from glucose, lactose, and xylose) were compared among eight American Type Culture Collection strains. E. coli ATCC 9637(pLO1297), ATCC 11303(pLO1297), and ATCC 15224(pLO1297) were selected for further development on the basis of environmental hardiness and ethanol production. Volumetric ethanol productivities per hour in batch culture were 1.4 g/liter for glucose (12%), 1.3 g/liter for lactose (12%), and 0.64 g/liter for xylose (8%). Ethanol productivities per hour ranged from 2.1 g/g of cell dry weight with 12% glucose to 1.3 g/g of cell dry weight with 8% xylose. The ethanol yield per gram of xylose was higher for recombinant E. coli than commonly reported for Saccharomyces cerevisiae with glucose. Glucose (12%), lactose (12%), and xylose (8%) were converted to (by volume) 7.2% ethanol, 6.5% ethanol, and 5.2% ethanol, respectively.     

Bench-scale bioethanol production from eucalyptus by high solid saccharification and glucose/xylose fermentation method

In the bioethanol production process, high solid saccharification and glucose/xylose co-fermentation are important technologies for obtaining increased ethanol concentrations; however, bench-scale studies using combinations of these methods are limited. In this study, we hydrolyzed high solid concentration of milled eucalyptus using commercial enzymes and obtained 138.4 g/L total monomeric sugar concentration. These sugars were fermented to 53.5 g/L of ethanol by a xylose-utilizing recombinant Saccharomyces cerevisiae strain, MA-R4. These experiments were performed in bench scale (using 50 L scale solid mixer and 70 L scale fermenter). The results obtained in this study were comparable to our previous results in laboratory scale, indicating that we successfully achieved an efficient high solid saccharification and glucose/xylose co-fermentation system in bench scale.