Ethanol production from cassava and sago starch using Zymomonas mobilis

Summary Cassava and sago starch were evaluated for their feasibilities as substrates for ethanol production using Zymomonas mobilis ZM4 strain. Before fermentation, the starch materials were pretreated employing two commercial enzymes, Termamyl (thermostable -amylase) and AMG (amyloglucosidase). Using 2 l/g of Termamyl and 4 l/g of AMG, effective conversion of both cassava and sago starch into glucose was found with substrate concentration up to 30%(w/v) dry substances. Fermentation study performed using these starch hydrolysates as substrates resulted in ethanol yield at an average of 0.48g/g by Z. Mobilis ZM4.     

Direct fermentation of cassava starch to ethanol by mixed cultures of Endomycopsis fibuligera and Zymomonas mobilis: Synergism and limitations

Summary A mixed culture of Endomycopsis fibuligera NRRL 76 and Zymomonas mobilis ZM4 could directly and more efficiently ferment cassava starch (22.5% w/v) to ethanol (10.5% v/v) than the monocultures. The combination of culture filtrate of E.fibuligera containing amylases and Z.mobilis simultaneously saccharified and fermented the cassava starch to ethanol equally well. Glucoamylase (0.01%) added to the fermenting medium improved ethanol (13.2% v/v) production by the above mixed culture to almost the theoretical level (98%) indicating that this enzyme is a rate-limiting factor in E.fibuligera. Z. mobilis alone converted the enzymehydrolyzed starch only to almost theoretical level (98%).     

Ethanol production from starch by a coimmobilized mixed culture system of Aspergillus awamori and Zymomonas mobilis

The production of ethanol from starch by a coimmobilized mixed culture system of aerobic and anaerobic microorganisms in Ca-alginate gel beads was investigated. The mold Aspergillus awamori was used as an aerobic amylolytic microorganism and an anaerobic bacterium, Zymomonas mobilis, as an ethanol producer. By controlling the mixing ratio of the microorganisms in the inoculum size, a desirable coimmobilized mixed culture system, in which the aerobic mycelia grew on and near the oxygen-rich surface of the gel beads while the anaerobic bacterial cells mainly grew in the oxygen-deficient central part of the gel beads, was naturally established under the aerobic culture conditions, and ethanol could be directly produced from starch by the system. The ethanol productivity by the system in flask culture was particularly affected by the shear stress (dependent on the shaking speed) which controlled the mycelial growth on the surface of the gel beads. Under optimum culture conditions in the flask culture, the glucose produced was instantly consumed, and was not observed in the culture broth; the final concentration of ethanol produced from 100 g/L starch was 25 g/L and the yield coefficient for ethanol, Y(pls), was 0.38. The ethanol productivity by the coimmobilized mixed culture system was compared with those by other various culture systems and the advantages of the system were clarified.     

Ethanol fermentation of cassava starch by Zymomonas mobilis NRRL B-4286

Four strains of Zymomonas mobilis were compared for ethanol production from enzymatically hydrolysed cassava starch. Strain NRRL B-4286 performed efficiently, producing 80 g/litre ethanol from 171 g/litre initial sugar concentration. Addition of yeast extract, calcium pantothenate, ammonium sulphate or magnesium sulphate did not significantly increase ethanol production by this strain.     

Ethanol production by a mixed culture of flocculent strains of Zymomonas mobilis and Saccharomyces sp.

 Pure and mixed cultures of Zymomonas mobilis and Saccharomyces sp. were tested for the production of ethanol using sucrose as the carbon source. Both strains, isolated from spontaneously fermenting sugar-cane juice, are flocculent and alcohol-tolerant. The best results were obtained using a mixed culture, with a yield of 0.5 g ethanol/g sugar consumed and a volumetric productivity of 1.5 g ethanol l^-1 h^-1. No levan was produced even if a sucrose-based medium was used. Received: 20 April 1995/Received revision: 26 July 1995/Accepted: 13 September 1995     

Ethanol production from cane juice by Zymomonas mobilis

Summary Zymomonas mobilis Z 7 fermented 100 to 200 g.l^{- 1} sucrose in cane juice to ethanol without addition of cofactors or mineral salts in 1 ltr laboratory and 100 ltr pilot plant fermenters. Ethanol yields (E_yield) were from 60 to 88% with fermentation times of 20 to 29 h at 35 °C.Nomenclature V_s max g.1^-1 .h^-1 maximum sucrose hydrolysis rate - V_g max g.1^-1 .h^-1 maximum glucose uptake rate - V_fmax g.1^-1 .h^-1 maximum fructose uptake rate - V_e max g.1^-1 .h^-1 maximum ethanol production rate - S_h g.1^-1 sucrose hydrolyzed at t_ferm - G_u g.1^-1 glucose utilized at t_ferm - F_u g.1^-1 fructose utilized at t_ferm - E_max g.1^-1 ethanol produced at t_ferm - G_i g.1^-1 initial free glucose (before sucrose hydrolysis) - E_yield g.g^-1 ethanol produced divided by the theoretical ethanol yield from sucrose hydrolyzed - t_ferm h fermentation time to ethanol max     

Ethanol production from wheat flour by Zymomonas mobilis

Starch from wheat flour was enzymatically hydrolyzed and used for ethanol production by Zymmonas mobilis. The addition of a nitrogen source like ammonium sulfate was sufficient to obtain a complete fermentation of the hdyrolyzed strach. In batch culture a glucose concentration as high as 223 g/l could be fermented (conversion 99.5%) to 105 g/l of ethanol in 70 h with an ethanol yield of 0.47 g/g (92% of theoretical). In continuous culture the use of a flocculent strain and a fermentor with an internal settler resulted (D=1,4 h⁻¹) in a high ethanol productivity of 70.7 g/l·h with: ethanol concentration 49.5 g/l, ethanol yield 0.50 g/g (98% of theoretical and substrate conversion 99%.     

Ethanol production from fructose in continuous culture by free and flocculent cells of Zymomonas mobilis

Summary Zymomonas mobilis strain ZM4 was used for ethanol production from fructose (100 g/l) in continuous culture with a mineral (containing Ca pantothenate) or a rich (containing yeast extract) mediium. With both media high conversion yields were observed but the ethanol productivity was limited by the low biomass content of the fermentor. A new flocculent strain of Z.mobilis (ZM4F) was cultivated in a CSTR with an internal settler and showed a maximal productivity of 93 g/l.h (fructose conversion of 80%). When the fructose conversion was 96% an ethanol productivity of 85.6 g/l.h with an ethanol yield of 0.49 g/g (96% of theoretical) was observed.     

Ethanol production by immobilized cells of Zymomonas mobilis

Summary Columnar reactors containing immobilized cells of Zymomonas mobilis were utilized for the continuous production of ethanol from glucose. Two different immobilization strategies were investigated. In one case, cells were entrapped in borosilicate glass fiber pads, while in the other, cells were immobilized via flocculation. The reactors were operated in both the fixed-bed and expanded-bed manner. Ethanol productivities as high as 132 g/l·h were achieved. Data obtained from studies employing 5.0 and 10.0% glucose concentrations are presented. Problems encountered during the operation of the continuous, immobilized cell reactors are discussed.Operated by Union Carbide Corporation under contract W-7405-eng-26 with the U.S. Department of Energy.     

Ethanol production by Zymomonas mobilis in fed-batch fermentations

The production of ethanol by Zymomonas mobilis NRRL B-4286 was studied in fed-batch cultures. Initial percent (w/v) glucose, rate of feed, and quantity of 50%; (w/v) glucose feed were varied. Glucose inhibition of growth rate occurred at concentrations greater than 8% (w/) Feed was begun after 4 h incubation. Feed volume was ca. 36%; of starting batch volume to get ca. 10%; (w/v) ethanol at harvest. The range of feed rates studied varied from 16%; batch volume/h (glucose concentration increased to an inhibitory level) to 4%; batch volume/h (glucose concentration dropped rapidly to zero and was limiting). Increasing feed volume to 46%; of starting volume at the best feed rate (ca. 10%; feed volume/h) increased final ethanol concentration to 11.3%; (w/v). However, the resultant increase in fermentation time from ca. 21 to 29 h decreased ethanol volumetric productivity from 5.2 to 4.6 g/L h.     

Ethanol production by Zymomonas mobilis CP4 from sugar cane chips

Summary The fermentation of large sugar cane chips (1.0–1.5 in) to ethanol by Zymomonas mobilis CP4 (Z. mobilis) was studied in two glass fermentors operating with culture circulation for agitation (the EX-FERM type): a. A laboratory scale(2.5 liter) cylindrical vessel; b. A bench scale (8 liter) wide vessel. Z. mobilis cultures consumed 89–96% of the cane sucrose, converting it to ethanol by 90–97% of the theoretical yield in the laboratory scale fermentor and by 83–90% in the bench scale fermentor culture. Comparative Saccharomyces spp. cultures in laboratory fermentor consumed 96–98% of the cane sucrose, with ethanol conversion of only 75–79% of the theoretical yield.These preliminary results indicated that sucrose in agricultural size sugar cane chips was ethanol fermentable as compared to small size sugar cane chips or to sugar cane juice. Z. mobilis CP4 cultures converted sucrose more efficiently to ethanol than Saccharomyces spp. as shown in the laboratory scale fermentor studies.The ethanol yields in a wide bench scale fermentor cultures were slightly lower than in a laboratory fermentor.     

Ethanol production by Zymomonas mobilis entrapped in alumina pellets

Summary Zymomonas mobilis cells were immobilized on pellets of alumina (Al₂O₃) by entrapment based on electrostatic forces. Entrapped cells produced 52 g/l^-1 ethanol every 24 h for many successive fermentation batches, when inoculated in batch synthetic media containing 12% glucose. It was shown that the rate of growth, ethanol production and glucose utilization increased when Al₂O₃ was added in the growth medium. This increase was dependent upon the concentration of Al₂O₃. The optimum conditions for immobilization of Z. mobilis on Al₂O₃ were established. Reduction in productivity and yield was not observed for up to 15 successive fermentation batches using the same entrapped cells.     

Behaviour of Endomycopsis fibuligera glucoamylase towards raw starch

An extracellular glucoamylase [exo-1,4-α-d-glucosidase, 1,4-α-d-glucan glucohydrolase, EC 3.2.1.3] of Endomycopsis fibuligera has been purified and some of its properties studied. It had a very high debranching activity (0.63). The enzyme was completely adsorbed onto raw starch at all the pH values tested (pH 2.0–7.6). Amylase inhibitor from Streptomyces sp. did not prevent the adsorption of glucoamylase onto raw starch although the enzyme did not digest raw starch in the presence of amylase inhibitor. Sodium borate (0.1 m) eluted only 35% of the adsorbed enzyme from raw starch. The optimum pH for raw starch digestion was 4.5 whereas that of boiled soluble starch hydrolysis was 5.5. Waxy starches were more easily digested than non-waxy starches, and root starches were slowly digested by this enzyme.     

Ethanol production from wood hydrolysate using genetically engineered Zymomonas mobilis

An ethanologenic microorganism capable of fermenting all of the sugars released from lignocellulosic biomass through a saccharification process is essential for secondary bioethanol production. We therefore genetically engineered the ethanologenic bacterium Zymomonas mobilis such that it efficiently produced bioethanol from the hydrolysate of wood biomass containing glucose, mannose, and xylose as major sugar components. This was accomplished by introducing genes encoding mannose and xylose catabolic enzymes from Escherichia coli. Integration of E. coli manA into Z. mobilis chromosomal DNA conferred the ability to co-ferment mannose and glucose, producing 91 % of the theoretical yield of ethanol within 36 h. Then, by introducing a recombinant plasmid harboring the genes encoding E. coli xylA, xylB, tal, and tktA, we broadened the range of fermentable sugar substrates for Z. mobilis to include mannose and xylose as well as glucose. The resultant strain was able to ferment a mixture of 20 g/l glucose, 20 g/l mannose, and 20 g/l xylose as major sugar components of wood hydrolysate within 72 h, producing 89.8 % of the theoretical yield. The recombinant Z. mobilis also efficiently fermented actual acid hydrolysate prepared from cellulosic feedstock containing glucose, mannose, and xylose. Moreover, a reactor packed with the strain continuously produced ethanol from acid hydrolysate of wood biomass from coniferous trees for 10 days without accumulation of residual sugars. Ethanol productivity was at 10.27 g/l h at a dilution rate of 0.25 h(-1).     

Ethanol production from starch by a coimmobilized mixed culture system of Aspergillus awamori and Saccharomyces cerevisiae

The development of a coimmobilized mixed culture sys tem of aerobic and facultative anaerobic microorganisms in Ca-alginate gel beads and the production of useful metabolites by the system were investigated. A coimmobilized mixed culture system of Aspergillus awamori (obligate aerobe) and Saccharomyces cerevisiae (facultative anaerobe) in Ca-alginate gel beads was used as a model system, and ethanol production from starch by the system was used as a model production. Mold Asp. awamori is an amylolytic microorganism while yeast S. cerevisiae is an ethanol producer. The two microorganisms grew competitively in the oxygen-rich surface area of the gel beads because they had similar oxygen demands in aerobic culture conditions. Neither microorganism exhibited "habitat segregation" in the gel beads and leaked yeast cells grew aerobically without ethanol production in the broth. Ethanol productivity was low under these conditions.A more desirable coimmobilized mixed culture system of Asp. awamori and S. cerevisiae was established by adding Vantocil IB (a biocidal compound) to the production medium. The antimicrobial activity of Vantocil IB was more effective with S. cerevisiae than with Asp. awamori, so that a dense mycelial layer of Asp. awamori formed in the surface of the gel beads While S. cerevisiae grew densely in the more inner areas of the gel beads. Also, yeast cell leakace was repressed and ethanol productivity was improved. The system with Vantocil IB produced ethanol of 4.5 and 12.3 g/L from 16 and 40 g/L starch, respectively. A continuous culture using this system with Vantocil IB was also carried out, and a stable steady state could be maintained for six days without leakage of yeast cells and contamination. The selection of a factor suitable for producing "habitat segregation" enabled the development of a coimmobilized mixed culture system of an aerobe and a facultative anaerobe. In this study, total habitat segregation was used to denote a tendency to exhibit denser growth in different parts of one gel bead.     

Continuous ethanol production from sago starch using immobilized amyloglucosidase and Zymomonas mobilis

To produce ethanol more economically than in a conventional process, it is necessary to attain high productivity and low production cost. To this end, a continuous ethanol production from sago starch using immobilized amylogucosidase (AMG) and Zymomonas mobilis cells was studied. Chitin was used for immobilization of AMG and Z. mobilis cells were immobilized in the form of sodium alginate beads. Ethanol was produced continuously in an simultaneous saccharification and ethanol fermentation (SSF) mode in a pacekd bed reactor. The maximum ethanol productivity based on the void volume, V_v, was 37 g/l/h with ethanol yield, Y_p/s, 0.43 g/g (84% of the theoretical ethanol yield) in this system. The steady-state concentration of ethanol (46 g/l could be maintained in a stable manner over two weeks at the dilution rate of 0.46 h⁻.     

Sorbitol production by Zymomonas mobilis

Summary High resolution ¹³C Nuclear Magnetic Resonance (NMR) spectroscopy has been employed to determine the chemical composition of the unknown major products in a sucrose or fructose plus glucose fermentation to ethanol by the bacterium Zymmonas mobilis. When grown on these sugars Z.mobilis was found to produce significant amounts of sorbitol, up to 43 g·l^-1 for strain ZM31 when grown on 250 g·l^-1 sucrose.The production of sorbitol and decrease of glucose, fructose, or sucrose was followed throughout batch fermentations by NMR and HPLC. Sorbitol was shown to be derived only from fructose by [¹⁴C]-feeding experiments. Additionally ³¹P NMR spectroscopy was utilized to determine the concentrations of both glucose 6-phosphate and fructose 6-phosphate relative to their respective concentrations in Z.mobilis cells fermenting glucose or fructose alone.It is suggested that free glucose inside the cell inhibits fructokinase. Free intracellular fructose may then be reduced to sorbitol via a dehydrogenase type enzyme. Attempts to grow Z.mobilis on sorbitol were unsuccessful, as were experiments to induce growth via mutagenesis.This work was supported in part by the National Energy Research, Development and Demonstration Council of Australia     

Ethanol production by immobilized Saccharomyces cerevisiae, Saccharomyces uvarum, and Zymomonas mobilis

Saccharomyces cerevisiae NRRL Y-2034, S, uvarum NRRL Y-1347, and Zymomonas mobilis NRRL B-806 each were separately immobilized in a Ca-alginate matrix and incubated in the presence of a free-flowing and continuous 1, 3, 5, 10, or 20% (w/w) glucose solution. In general, the yeast cells, converted 100percnt; of the 1, 3, and 5% glucose to alcohol within 48 h and maintained such a conversion rate for at least two weeks. The bacterium converted ca. 90% (w/w) of the 1, 3, and 5% glucose to alcohol continuously for one week. However, both the yeast and bacterium were inhibited in the highest glucose (20% w/w) solution. All of the immobilized cultures produced some alcohol for at least 14 days. Immobilized S. cerevisiae was the best alcohol producer of all of the glucose concentrations; the yeast yielded 4.7 g ethanol/100 g solution within 72 h in the 10% glucose solution. After 7-8 days in the 10% solution, S. cerevisiae produced ethanol at 100% of theoretical yield (5.0 g ethanol/100 g solution), with a gradual decrease in alcohol production by 14 days. Immobillized S. uvarum produced a maximum of 4.0 g ethanol/100 g solution within 2 days and then declined to ca. 1.0 g ethanol/100 g solution after 7 days continuous fermentation in the 10% glucose solution. Zymomonas mobilis reached its maximum ethanol production at 4 days (4.7 g/100 g solution), and then diminished similarly to S. uvarum. The development of a multiple disk shaft eliminated the problem both of uneven distribution of alginate-encapsulated cells and of glucose channeling within the continuous-flow fermentor column. This invention improved alcohol production about threefold for the yeast cells.     

Hydrogen peroxide production by Zymomonas mobilis

Summary The anaerobic aerotolerant bacterium Zymomonas mobilis 113 produced superoxide (O ₂ ^- ) and hydrogen peroxide (H₂O₂) under aerobic conditions. The main generators of H₂O₂ were glucose oxidase and superoxide dismutase (SOD). The O ₂ ^- generation was probably related to minor alternative reduced nicotinamide adenine zinucleotide (NADH)-oxidation reactions in the electron transport chain. An increase in medium pO₂ was observed during growth of Z. mobilis 113 in a batch culture. The maximum pO₂ increase correlated with glucose oxidase and SOD activities. An decrease in medium pO₂ value coincided with an increase in catalase activity in batch culture. Medium deoxygenation reduced the pO₂ effect, yet the culture still responded with a pO₂ increase after inoculation and addition of the feeding medium. We conclude that the apparent pO₂ effects are related to changes in H₂O₂ concentration in the culture liquid.