Comparative study of d-xylose conversion to ethanol by immobilized growing or non-growing cells of the yeast Pachysolen tannophilus

Summary The direct conversion of d-xylose to ethanol was investigated using immobilized growing and non-growing cells of the yeast Pachysolen tannophilus. Both preparations produced ethanol from d-xylose, however the d-xylose conversion to ethanol was much better with immobilized growing cells. Ethanol concentration up to 22.9 g/l and ethanol yield of 0.351 g/g of d-xylose were obtained in batch fermentation by immobilized growing cells whereas only 17.0 g/l and 0.308 g/g of d-xylose were obtained by immobilized non-growing cells. With continuous systems, immobilized growing cells were necessary for the long-term operation, since a steady state ethanol concentration of 17.7 g/l was maintained for only one week by immobilized non-growing cell reactor. With simultaneous control of aeration rate and concentrations of nitrogen sources in feed medium, immobilized growing cells of P. tannophilus showed excellent performance. At a residence time of 25 h, the immobilized cell reactor produced 26.9 g/l of ethanol from 65 g/l of d-xylose in feed medium.     

Contributions of immobilized and free cells of salt-tolerantZygosaccharomyces rouxii andCandida versatilis to the production of ethanol and 4-ethylguaiacol

Summary The contribution of immobilized cells and free cells released from gel beads to ethanol production by the salt-tolerant yeastsZygosaccharomyces rouxii andCandida versatilis, and 4-ethylguaiacol (4-EG) production byC. versatilis were investigated using an airlift reactor. The amounts of ethanol produced by free cells were about 65% and about 90% of total ethanol in the reactor forZ. rouxii andC. versatilis, respectively. It was found that immobilized cells gave a much lower specific productivity of ethanol (ethanol production per hour per cell) than free cells of both yeasts, especially ofC. versatilis. 4-EG was produced mainly by immobilized cells ofC. versatilis; the amount of 4-EG produced by free cells was about 20% of the total 4-EG, in contrast to the results of ethanol production. However, the specific productivity of 4-EG (4-EG production per hour per cell) by immobilized and free cells was fairly similar.     

Process and technoeconomics of ethanol production by immobilized cells

Summary A two-stage fermentation process has been developed for continuous ethanol production by immobilized cells of Zymomonas mobilis. About 90–92 kg/m³ ethanol was produced after 4 h of residence time. Entrapped cells of Zymomonas mobilis have a capability to convert glucose to ethanol at 93% of the theoretical yield. The immobilized cell system has functioned for several weeks, and experience indicates that the carrageenan gel apparently facilitates easy diffusion of glucose and ethanol.The simplicity and the high productivity of the plug-flow reactor employing immobilized cells makes it economically attrative. An evaluation of process economics of an immobilized cell system indicates that at least 4 c/l of ethanol can be saved using the immobilized cell system rather than the conventional batch system. The high productivity achieved in the immobilized cell reactor results in the requirement for only small reactor vessels indicating low capital cost. Consequently, by switching from batch to immobilized processing, the fixed capital investment is substantially reduced, thus increasing the profitability of ethanol production by fermentation.     

Ethanol fermentation of mahula (<Emphasis Type="Italic">Madhuca latifolia</Emphasis>) flowers using free and immobilized bacteria <Emphasis Type="Italic">Zymomonas mobilis</Emphasis> MTCC 92

Mahula (Madhuca latifolia L.) is a deciduous tree commonly found in the tropical rain forests of Asian and Australian continent. Corolla, the edible part of its flowers, is rich in fermentable sugar (37 ± 0.23%; on dry weight basis). Batch fermentation of mahula flowers was carried out using Zymomonas mobilis MTCC 92 free cells and cells immobilized in calcium alginate matrix. The ethanol productions were 122.9 ± 0.972 and 134.6 ± 0.104 g/kg flowers on dry weight basis using free and immobilized cells, respectively, after 96 h of fermentation, which showed that cells entrapped in calcium alginate matrix yielded 8.7% more ethanol than free cells. Further, the immobilized cells were physiologically active up to three more cycles of fermentation producing 132.7 ± 0.095, 130.5 ± 0.09 and 128.7 ± 0.056 g ethanol per kg flower in first, second and third cycle, respectively.     

Critical factors affecting ethanol production by immobilized Pichia stipitis using corn cob hemicellulosic hydrolysate

Fermentation of xylose from hydrolysate of acid-treated corn cob by Pichia stipitis is inhibited by acetic acid and lignin derivatives. In the present study, we have designed and implemented an immobilized cell culture for xylose to ethanol conversion from acid-treated corn cob hydrolysate without the removal of fermentation inhibitors. In this study, cultivations of suspended and immobilized Pichia were compared in terms of ethanol yield and productivity to investigate whether the cell immobilization could improve resistance to inhibitors. Cell immobilization clearly favored the fermentative metabolism in nondetoxified corn cob hydrolysate leading to an improvement of twofold ethanol productivity as compared to that achieved with suspension culture. Calcium alginate as an immobilization matrix was selected to immobilize Pichia cells. Concentrations of sodium alginate, calcium chloride, and fermentor agitation speed were optimized for ethanol production using statistical method. Statistical analysis showed that agitation speed had maximum influence on ethanol production by immobilized Pichia cells. In comparison to suspension culture, immobilization had a positive impact on the fermentative metabolism of Pichia, improving the ethanol yield from 0.40 to 0.43?g/g and productivity from 0.31 to 0.51?g/L/h for acid-treated corn cob hydrolysate.     

Ethanol production from concentrated food waste hydrolysates with yeast cells immobilized on corn stalk

The aim of the present study was to examine ethanol production from concentrated food waste hydrolysates using whole cells of S. cerevisiae immobilized on corn stalks. In order to improve cell immobilization efficiency, biological modification of the carrier was carried out by cellulase hydrolysis. The results show that proper modification of the carrier with cellulase hydrolysis was suitable for cell immobilization. The mechanism proposed, cellulase hydrolysis, not only increased the immobilized cell concentration, but also disrupted the sleek surface to become rough and porous, which enhanced ethanol production. In batch fermentation with an initial reducing sugar concentration of 202.64 ± 1.86 g/l, an optimal ethanol concentration of 87.91 ± 1.98 g/l was obtained using a modified corn stalk-immobilized cell system. The ethanol concentration produced by the immobilized cells was 6.9% higher than that produced by the free cells. Ethanol production in the 14th cycle repeated batch fermentation demonstrated the enhanced stability of the immobilized yeast cells. Under continuous fermentation in an immobilized cell reactor, the maximum ethanol concentration of 84.85 g/l, and the highest ethanol yield of 0.43 g/g (of reducing sugar) were achieved at hydraulic retention time (HRT) of 3.10 h, whereas the maximum volumetric ethanol productivity of 43.54 g/l/h was observed at a HRT of 1.55 h.     

Repeated batch production of ethanol from Jerusalem artichoke tubers using recycled immobilized cells of Kluyveromyces fragilis

Summary Recycled immobilized cells of Kluyveromyces fragilis ATCC 28244 were used for repeated batch production of ethanol from the inulin sugars derived from Jerusalem artichoke tubers. Using 10% initial sugar concentration, a maximum ethanol concentration of 48 g/l was achieved in 7 h when the immobilized cell concentration in the Ca alginate beads was 72 g dry wt. immobilized cell/l bead volume. The maximum ethanol production rate was 13.5 g ethanol/l bioreactor volume/h. The same Ca alginate beads containing the cells were used repeatedly for 11 batch runs starting with fresh medium at the beginning of each run. The ethanol yield was found to be almost constant at 96% of the theoretical for all 11 batch runs, while the maximum ethanol production rate during the last batch run was found to be 70% of the original ethanol rate obtained in the first batch run.     

The production of ethanol by immobilized yeast cells

Saccharomyces cerevisiae cells were immobilized in calcium alginate beads for use in the continuous production of ethanol. Yeasts were grown in medium supplemented with ethanol to selectively screen for a culture which showed the greatest tolerance to ethanol inhibition. Yeast beads were produced from a yeast slurry containing 1.5% alginate (w/v) which was added as drops to 0.05M CaCl₂ solution. To determine their optimum fermentation parameters, ethanol production using glucose as a substrate was monitored in batch systems at varying physiological conditions (temperature, pH, ethanol concentration), cell densities, and gel concentration. The data obtained were compared to optimum free cell ethanol fermentation parameters. The immobilized yeast cells examined in a packed-bed reactor system operated under optimized parameters derived from batch-immobilized yeast cell experiments. Ethanol production rates, as well as residual sugar concentration were monitored at different feedstock flow rates.     

Ethanol production by immobilized whole cells ofZymomonas mobilis in a continuous flow expanded bed bioreactor and a continuous flow stirred tank bioreactor

Continuous ethanol fermentation by immobilized whole cells ofZymomonas mobilis was investigated in an expanded bed bioreactor and in a continuous stirred tank reactor at glucose concentrations of 100, 150 and 200 g L^–1. The effect of different dilution rates on ethanol production by immobilized whole cells ofZymomonas mobilis was studied in both reactors. The maximum ethanol productivity attained was 21 g L^–1 h^–1 at a dilution rate of 0.36 h^–1 with 150 g glucose L^–1 in the continuous expanded bed bioreactor. The conversion of glucose to ethanol was independent of the glucose concentration in both reactors.     

High alcohol production by repeated batch fermentation using an immobilized osmotolerant Saccharomyces cerevisiae

A repeated batch fermentation system was used to produce ethanol using an osmotolerant Saccharomyces cerevisiae (VS₃) immobilized in calcium alginate beads. For comparison free cells were also used to produce ethanol by repeated batch fermentation. Fermentation was carried for six cycles with 125, 250 or 500 beads using 150, 200 or 250 g glucose L⁻¹ at 30°C. The maximum amount of ethanol produced by immobilized VS₃ using 150 g L⁻¹ glucose was only 44 g L⁻¹ after 48 h, while the amount of ethanol produced by free cells in the first cycle was 72 g L⁻¹. However in subsequent fed batch cultures more ethanol was produced by immobilized cells compared to free cells. The amount of ethanol produced by free cells decreased from 72 g L⁻¹ to 25 g L⁻¹ after the fourth cycle, while that of immobilized cells increased from 44 to 72 g L⁻¹. The maximum amount of ethanol produced by immobilized VS₃ cells using 150, 200 and 250 g glucose L⁻¹ was 72.5, 93 and 87 g ethanol L⁻¹ at 30°C. Journal of Industrial Microbiology & Biotechnology (2000) 24, 222–226. Received 16 September 1999/ Accepted in revised form 22 December 1999     

Comparison of suspended and immobilized yeast metabolism using 31P nuclear magnetic resonance spectroscopy

Summary ³¹P nuclear magnetic resonance has been employed to monitor noninvasively Saccharomyces cerevisiae anaerobic glucose metabolism in suspended and immobilized cells. Results show that cell entrapment in Ca-alginate beads alters cell metabolism compared to that in suspended cells. Assuming similar intracellular ionic strength, differences in intracellular phosphate chemical shift indicate that the internal pH of the immobilized cells is lower than the suspended cell internal pH. This result is consistent with higher ethanol production rates exhibited by immobilized yeast.     

Ethanol production from sulphuric acid wood hydrolysate ofPinus radiata using free and immobilized cells ofPichia stipitis

Summary Ethanol was produced by a strain ofPichia stipitis adapted to an inhibitory acid wood hydrolysate ofPinus radiata. The best ethanol productivity for batch cultures was 0.21 g/l h at 0.7% ethanol. Varying culture conditions increased ethanol concentration to 0.76%, however the productivity decreased to 0.18 g/l h. A decrease in ethanol concentration in the culture fluid was noted late in the batch which suggested ethanol catabolism. Values of kinetic parameters (K _m,K _s, _max, andV _max) were evaluated for this system. The use of calcium alginate immobilized cells in a continuous-flow stirred tank reactor lead to enhanced fermentative performance, namely a maximum productivity of 0.27 g/l h and 1.13% ethanol yield. The immobilized cells in continuous flow reactors represent an attractive option for fermenting sugars released by sulphuric acid hydrolysis ofP. radiata wood.     

Immobilization and characterization of Saccharomyces cerevisiae in crosslinked,prepolymerized polyacrylamide-hydrazide

Summary Baker's yeast (Saccharomyces cerevisiae) was immobilized in gels made of prepolymerized, linear, water soluble polyacrylamide, partially substituted with acylhydrazide groups. Gelation was effected by the addition of controlled amounts of dialdehydes (e.g. glyoxal). The immobilized yeasts retained full glycolytic activity. Moreover, the entrapped cells were able to grow inside the chemically corsslinked gel during continuous alcohol production. Glyoxal was found to be the most favourable crosslinking agent for this system. the system employed allowed for the free exchange of substrate and products. The gel surrounding the entrapped cells had no effect on temperature stability profile. On the other hand, substantial enhancement in survival of cells in presence of high ethanol concentrations was recorded for the entrapped yeast. The capability of the immobilized yeast to carry out continuous conversion of glucose to ethanol was demonstrated.     

Alcoholic fermentation of D-xylose by immobilizedPichia stipitis yeast

Summary Pichia stipitis NRRL Y-7124 yeast cells were for the first time immobilized both in agar gel beads and on fine nylon net for ethanol fermentation on D-xylose, in order to investigate the possibility of using the biocatalyst for improved utilization of the biomass pentose fraction. With free cells the initial xylose level affected little ethanol production, with a maximum of 22 g/l ethanol obtained in 5 days on 5% and of 40 g/l in 8 days on 10% xylose, and an average volumetric productivity of about 0.22 g/lh. The maximum ethanol concentration of 19.5% on 5% xylose with the nylon net attached cells in a continuous packed-bed column reactor was obtained with 35 h residence time. The volumetric productivities of 0.56 g/lh at 19.5 g/l ethanol and 1.0 g/lh at 15.0 g/l ethanol were markedly higher than those obtained with free cells. The stability of the immobilized biocatalyst was excellent. The same reactor could be used for at least 80 days without significant activity loss.     

Kinetics of ethanol production by immobilized Kluyveromyces marxianus cells at varying sugar concentrations of Jerusalem artichoke juice

Summary Kinetics of ethanol fermentation at varying sugar concentrations of Jerusalem artichoke tuber extract has been studied using Kluyveromyces marxianus cells immobilized in calcium alginate gel beads. A maximum ethanol concentration of 111 g/l was achieved at an initial sugar concentration of 260 g/l in 20 hours, when the immobilized cell concentration in the calcium alginate beads was 53.3 g dry wt./l bead volume. Ethanol yield remained almost unaffected by initial sugar concentration up to 250 g/l and was found to be about 88% of the theoretical. Maximum rate of ethanol production decreased from 22.5 g ethanol/l/h to 10.5 g ethanol/l/h while the maximum rate of total sugars utilization decreased from 74.9 g sugars/l/h to 28.5 g sugars/l/h as the initial substrate concentration was increased from 100 to 300 g/l. The concentration of free cells in the fermentation broth was low.     

High solids fermentation of hydrolysates of wheat starch B in a continuous dynamic immobilized biocatalyst bioreactor

Summary A simple and efficient method of conversion of wheat starch B to ethanol was investigated. Employing a two-stage enzymatic saccharification process, 95% of the wheat starch was converted to fermentable sugars in 40 h. From 140 g/l total sugars in the feed solution, 63.6 g/l ethanol was produced continuously with a residence time of 3.3 h in a continuous dynamic immobilized biocatalyst bioreactor by immobilized cells ofSaccharomyces cerevisiae. The advantages and the application of this bioreactor to continuous alcoholic fermentation of industrial substrates are presented.     

Glycerol production by immobilized cells of Saccharomyces cerevisiae

Summary Cells of Saccharomyces cerevisiae were immobilized in K-Carrageenan. Addition of sodium sulfite to the fermentation medium up to four percent led to glycerol yields of 25 to 27 g/l at temperatures below 31°C.These results demonstrate that it is possible to direct the metabolism of immobilized cells from ethanol fermentation to glycerol fermentation by sulfite.     

The production of ethanol from lactose in a tubular reactor by immobilized cells of Kluyveromyces fragilis

Summary An immobilized-cell tubular reactor for the continuous fermentation of lactose by Kluyveromyces fragilis was developed. Two types of supporting media were successfully tested; beechwood cubes and activated charcoal pellets. Ethanol productivity of 17.2 g/l/h was achieved from a 15% whey-lactose solution using K. fragilis immobilized on charcoal pellets, with a final ethanol concentration of 18 g/l. The use of two reactors in series demonstrated that it is possible to obtain up to 50 g/l of ethanol in the final product. No decrease in biological activity of the immobilized yeast cells occurred over a period of up to 31 days of continuous operation.     

Continuous production of ethanol using yeast cells immobilized in preformed cellulose beads

 Saccharomyces cerevisiae cells were immobilized on preformed cellulose beads by adsorption. The fermentation capacity of the immobilized yeast cells was found to be practically independent of the hydrogen ion concentration between pH 3.1 and 6.25. The fermentation capacity was maximal at 30 °C. The immobilized yeast cells were used for continuous production of ethanol in a fluidized-bead reactor. The average values characteristic for the process were an ethanol concentration of 41.9±0.1 g l^-1, a fermentation efficiency of 82.9±2.1% and a volumetric productivity of 3.94±0.52 g l^-1 h^-1. Received: 9 October 1995/Accepted: 22 April 1996     

A comparison between the fermentative activities of free and Ca-alginate-entrapped cells of saccharomyces cerevisiae

The continuous ethanol production by free and Ca-alginate-entrapped cells of the yeast Saccharomyces cer. IBT H 191 was investigated in a membrane reactor and in a CSTR, respectively. An empiric productivity model for free-cell fermentation was found to be valid for immobilized cells if no external diffusion resistance existed within the reactor. In such a case the fermentative power of the immobilized cells was identical with this one of the free cells. A change of the ethanol-tolerance behaviour of the cells as a result of the cell-immobilization did not occur.