The response by microorganisms to steady-state growth in controlled concentrations of oxygen and glucose. II. Saccharomyces carlsbergensis

The growth of Saccharomyces carlsbergensis in continuous culture has been studied when dissolved oxygen and glucose concentrations were held constant at a series of steady-state levels. Both oxygen and glucose controlled the degree of aerobic metabolism and of ethanolic fermentation. When the glucose uptake rate was low (between 1.2 and 2.8 mmoles per hour per gram of yeast) the relative distribution of glucose between ethanolic and aerobic fermentation was sensitive to oxygen: when dissolved oxygen was near to saturation, glucose metabolism was 0.98 aerobic; when dissolved oxygen was 0.01 saturated, 0.8 of intake glucose metabolism was by ethanolic fermentation. On the other hand when glucose intake was high (between 7.6 and 18.2 mmoles) metabolism was predominately by ethanolic fermentation even when dissolved oxygen concentration was at saturation. The extent, to which catabolism proceeded by an anaerobic or aerobic pathway, as judged by ethanol production, was controlled more by the uptake of glucose than of oxygen.     

Continuous fermentation of high-strength glucose feeds to ethanol

Summary Aqueous feeds of 413 and 495 g/L glucose were fermented to ethanol at 90–95% conversion in a continuous flow extractive fermentation system with cell recycle. Compared to the continuous conventional fermentation of a 195 g/L glucose medium, the volumetric productivity was more than doubled in extractive mode, with no deleterious effects on cell viability, specific glucose consumption rate or ethanol yield. The use of an effective, biocompatible and stable in situ extractant with flash vaporization can also produce a concentrated ethanol vapour stream, reducing distillation costs of the product.     

An artificial intelligence tool for bioprocess monitoring: application to continuous production of gluconic acid by immobilized Aspergillus niger

Experimental data on continuous fermentation of sucrose and glucose solution at low pH to gluconic acid by Asprgillus niger immobilized on cellulose fabric show complex dynamic behaviour including a decline in yield. The data have been analyzed using an artificial intelligence based symbolic regression technique to provide a mathematical model for predicting values of conversion 5, 10 and 15 h ahead values of conversion. These predictions can be used during continuous operations to monitor the bioprocess and adjust the residence time of fermentation to get complete and more efficient conversion of sucrose or glucose to gluconic acid.     

Application of multistage continuous fermentation for production of fuel alcohol by very-high-gravity fermentation technology

A fermentation system to test the merging of very-high-gravity (VHG) and multistage continuous culture fermentation (MCCF) technologies was constructed and evaluated for fuel ethanol production. Simulated mashes ranging from 15% to 32% w/v glucose were fermented by Saccharomyces cerevisiae and the dilution rates were adjusted for each glucose concentration to provide an effluent containing less than 0.3% w/v glucose (greater than 99% consumption of glucose). The MCCF can be operated with glucose concentrations up to 32% w/v, which indicates that the system can successfully operate under VHG conditions. With 32% w/v glucose in the medium reservoir, a maximum of 16.73% v/v ethanol was produced in the MCCF. The introduction of VHG fermentation into continuous culture technology allows an improvement in ethanol productivity while producing ethanol continuously. In comparing the viability of yeast by methylene blue and plate count procedures, the results in this work indicate that the methylene blue procedure may overestimate the proportion of dead cells in the population. Ethanol productivity (Yps) increased from the first to the last fermentor in the sequence at all glucose concentrations used. This indicated that ethanol is more effectively produced in later fermentors in the MCCF, and that the notion of a constant Yps is not a valid assumption for use in mathematical modeling of MCCFs. Journal of Industrial Microbiology & Biotechnology (2001) 27, 87–93. Received 20 January 2001/ Accepted in revised form 28 April 2001     

Ethanol fermentation coupled with complete cell recycle pervaporation system: Dependence of glucose concentration

Summary A membrane bioreactor system comprised of a fermenter and a flat pervaporation module was developed for continuous ethanol fermentation by Saccharomyces cerevisiae. In order to obtain the guidelines for high sugar concentration fermentation, the dependence of glucose concentration on the coupled system was investigated. Fed by 158 and 290g glucose/l, the improvement in productivity was obtained with 1. 58 and 1. 86 times, and the ethanol yield was 0. 45 and 0. 395, respectively. With the fermentation proceeding, the permeate flux decreased but the selectivity kept unaltered.     

Kinetics of polysaccharide B-1459 fermentation

Polysaccharide gum was made by fermentation with Xanthomonas campestris NRRL B-1459 in a medium of glucose, minerals, and distillers' solubles. The effect of distillers' solubles on growth rate can be described by the familiar saturation equation. Although a quasistoichiometric relationship was observed between nitrogen utilization and growth, total nitrogen supply was not growth limiting, nor was polymer formation growth associated. Cell growth primarily took place in the early part of the fermentation; polysaccharide biosynthesis occurred throughout the fermentation. Glucose was converted to polysaccharide at a fairly constant yield, which was 70–80% of glucose consumed, under optimum conditions. The kinetic patterns observed indicate that multistage continuous fermentation will be suitable for polysaccharide production.     

Effect of temperature and long-term operation on passively immobilizedZymomonas mobilis for continuous ethanol production

Summary A fibrous support was used forZ. mobilis immobilization. The system showed a broad optimum temperature range (25–35°C) for highest ethanol productivity, ethanol yield and glucose conversion during continuous fermentation of a 100 g/L glucose medium. Ethanol production and glucose conversion kept steady during two months of continuous operation at D=1h^–1.     

Propionic acid fermentation by Propionibacterium acidipropionici: effect of growth substrate

Summary Batch propionic acid fermentations by Propionibacterium acidipropionici with lactose, glucose, and lactate as the carbon source were studied. In addition to propionic acid, acetic acid, succinic acid and CO₂ were also formed from lactose or glucose. However, succinic acid was not produced in a significant amount when lactate was the growth substrate. Compared to fermentations with lactose or glucose at the same pH, lactate gave a higher propionic acid yield, lower cell yield, and lower specific growth rate. The specific fermentation or propionic acid production rate from lactate was, however, higher than that from lactose. Since about equimolar acid products would be formed from lactate, the reactor pH remained relatively unchanged throughout the fermentation and would be easier to control when lactate was the growth substrate. Therefore, lactate would be a preferred substrate over lactose and glucose for propionic acid production using continuous, immobilized cell bioreactors. Correspondence to: S. T. Yang     

An automated flow injection analysis system for on-line monitoring of glucose and L-lactate during lactic acid fermentation in a recycle bioreactor

The study concerns on-line sequential analysis of glucose and L-lactate during lactic acid fermentation using a flow injection analysis (FIA) system. Enzyme electrodes containing immobilized glucose oxidase and L-lactate oxidase were used with an amperometric detection system. A 12-bit data acquisition card with 16 analog input channels and 8 digital output channels was used. The software for data acquisition was developed using Visual C++, and was devised for sampling every hour for sequential analyses of lactate and glucose. The detection range was found to be 2–100 g l^–1 for glucose and 1–60 g l^–1 for L-lactate using the biosensors. This FIA system was used for monitoring glucose utilization and L-lactate production by immobilized cells of Lactobacillus casei subsp. rhamnosus during a lactic acid fermentation process in a recycle batch reactor. After 13 h of fermentation, complete sugar utilization and maximal L-lactate production was observed. A good agreement was observed between analysis data obtained using the biosensors and data from standard analyses of reducing sugar and L-lactate. The biosensors exhibited excellent stability during continuous operation for at least 45 days.     

Studies on Erythorbic Acid Production by Fermentation

Screening was carried out for erythorbic acid (EA)-producing strains from about 5,000 newly isolated fungi and bacteria. Penicillium notatum FY 115 was screened out as most powerful EA producer. Only Penicillium, but no other genera, was obtained as EA producers from our screening program. Monospore selections and mutagenic treatments succeeded to elevate the yield of EA over 40% to glucose supplied. Various cultural conditions were studied, and pH change during fermentation process was proved to be most important for favorable EA production. Over 80% yield could be obtained when washed mycelium was used in dilute glucose solution.

Abundant accumulation of EA by the strain FY 115, Penicillium sp., in fermentation broth was studied, and EA, both free and Na-salt, was obtained as crystal in the yield of about 45% to glucose supplied, in the media of 8% glucose by jar fermentor, in considering the inhibitory effect of some metal ion.

Extraction processes were improved to elevate the yield and was developed the continuous multi-bed extraction system of anion-exchange resin, which resulted in the yield of 90.9% of EA from fermentation broth in sum total.     

Evaluation of cell recycling in continuous fermentation of enzymatic hydrolysates of spruce with Saccharomyces cerevisiae and on-line monitoring of glucose and ethanol

The maximum growth rate of Saccharomyces cerevisiae ATCC 96581, adapted to fermentation of spent sulphite liquor (SSL), was 7 times higher in SSL of hardwood than the maximum growth rate of bakers' yeast. ATCC 96581 was studied in the continuous fermentation of spruce hydrolysate without and with cell recycling. Ethanol productivity by ATCC 96581 in continuous fermentation of an enzymatic hydrolysate of spruce was increased 4.6 times by employing cell recycling. On-line analysis of CO₂, glucose and ethanol (using a microdialysis probe) was used to investigate the effect of fermentation pH on cell growth and ethanol production, and to set the dilution rate. Cell growth in the spruce hydrolysates was strongly influenced by fermentation pH. The fermentation was operated in continuous mode for 210 h and a theoretical ethanol yield on fermentable sugars was obtained. Received: 25 May 1998 / Received revision: 11 August 1998 / Accepted: 12 August 1998     

Rapid ethanol fermentations using vacuum and cell recycle

Cell recycle and vacuum fermentation systems were developed for continuous ethanol production. Cell recycle was employed in both atmospheric pressure and vacuum fermentations to achieve high cell densities and rapid ethanol fermentation rates. Studies were conducted with Saccharomyces cerevisiae (ATCC No. 4126) at a fermentation temperature of 35°C. Employing a 10% glucose feed, a cell density of 50 g dry wt/liter was obtained in atmospheric-cell recycle fermentations which produced a fermentor ethanol productivity of 29.0 g/liter-hr. The vacuum fermentor eliminated ethanol inhibition by boiling away ethanol from the fermenting beer as it was formed. This permitted the rapid and complete fermentation of concentrated sugar solutions. At a total pressure of 50 mmHg and using a 33.4% glucose feed, ethanol productivities of 82 and 40 g/liter-hr were achieved with the vacuum system with and without cell recycle, respectively. Fermentor ethanol productivities were thus increased as much as twelvefold over conventional continuous fermentations. In order to maintain a viable yeast culture in the vacuum fermentor, a bleed of fermented broth had to be continuously withdrawn to remove nonvolatile compounds. It was also necessary to sparge the vacuum fermentor with pure oxygen to satisfy the trace oxygen requirement of the fermenting yeast.     

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.     

Whey disposal by deproteinization and fermentation

The non-pollutant plant support material of the dwarf duckweed Wolffia arrhiza (Fam. Lemnaceae) was used for the entrapment of living yeast cells (Kluyveromyces fragilis) which hydrolyse lactose with the subsequent fermentation of glucose and galactose at high cell densities (up to 7.0 × 10⁸/ml support). The stabile yeast-plant cell immobilizates are able to produce ethanol from lactose-containing media (e.g. whey) by batch fermentation (on a rotary shaker) or continuous fermentation (in a turbulence reactor) for several days (at a pH below 4.2 and a temperature of 30°C). The removal of whey proteins by a preceding heat denaturation of whey, high dilution rates, C_So values of 50 to 60 g lactose per litre whey and the preferential use of the K. fragilis strain DSM 7238 were determined as the prerequisites for an optimum continuous fermentation. Economically interesting productivities (P_max ? 15 g ethanol/1 · h, D = 0.72 h^?1) with an actual lactose turnover of 90% were obtained by using these parameters.     

Dilution rates influence ammonia-assimilating enzyme activities and cell parameters of Selenomonas ruminantium strain D in continuous (glucose-limited) culture

Aims: The objective of this study was to examine the effect of dilution rates (Ds, varying from 0·05 to 0·42 h^?1) in glucose‐limited continuous culture on cell yield, cell composition, fermentation pattern and ammonia assimilation enzymes of Selenomonas ruminantium strain D. Methods and Results: All glucose‐limited continuous culture experiments were conducted under anaerobic conditions. Except for protein, all cell constituents including carbohydrates, RNA and DNA yielded significant cubic responses to Ds with the highest values at Ds of either 0·10 or 0·20 h^?1. At Ds higher than 0·2 h^?1, fermentation acid pattern shifted primarily from propionate and acetate to lactate production. Succinate also accumulated at the higher Ds (0·30 and 0·42 h^?1). Glucose was most efficiently utilized by S. ruminantium D at 0·20 h^?1 after which decreases in glucose and ATP yields were observed. Under energy limiting conditions, glutamine synthetase (GS) and glutamate dehydrogenase (GDH) appeared to be the major enzymes involved in nitrogen assimilation suggesting that other potential ammonia incorporating enzymes were of little importance in ammonia assimilation in S. ruminantium D. GS exhibited lower activities than GDH at all Ds, which indicates that the bacterial growth rate is not a primary regulator of their activities. Conclusions: Studied dilution rates influenced cell composition, fermentation pattern and nitrogen assimilation of S. ruminantium strain D grown in glucose‐limited continuous culture. Significance and Impact of the Study: Selenomonas ruminantium D is an ecologically and evolutionary important bacterium in ruminants and is present under most rumen dietary conditions. Characterizing the growth physiology and ammonia assimilation enzymes of S. ruminantium D during glucose limitation at Ds, which simulate the liquid turnover rates in rumen, will provide a better understanding of how this micro‐organism responds to differing growth conditions.     

Fermentation of mannitol by Clostridium butyricum: role of acetate as an external hydrogen acceptor

Summary The continuous fermentation of mannitol (pH 6, dilution rate (D)=0.087 h^-1) by Clostridium butyricum LMG 1213t1 was investigated under several conditions. Mannitol was readily fermented when glucose or acetate were added in the in-flow medium as co-substrate. Butyrate, CO₂ and H₂ were the major fermentation products. In mannitol-glucose mixtures (ratios 4 or 8) the amount of mannitol fermented depended upon the amount of glucose in the in-flow medium. In mannitol-acetate mixtures, 1 mol of acetate was needed for the fermentation of approximately 5.5 mol mannitol. We detected d-mannitol-1-phosphate dehydrogenase activity, responsible for the generation of supplementary reduced nicotine adenine dinucleotide (NADH) as a source for extra H₂ gas. Fermentation of mannitol-acetate in the presence of [¹⁴C]-labelled acetate revealed butyrate as the only labelled fermentation end-product.     

Enzymes limiting butanol and acetone formation in continuous and batch cultures of Clostridium acetobutylicum

Summary The formation of butanol in continuous cultures of Clostridium acetobutylicum is regulated at the genetic level via expression of butyraldehyde dehydrogenase since increased in vitro activities of this key enzyme are associated with increased in vivo butanol formation rates in both acidogenic and solventogenic fermentations. Addition of glucose, butyric acid and carbon monoxide results in induction of butyraldehyde dehydrogenase. The production of acetone in continuous fermentation is also controlled at the genetic level through expression of coenzyme A (CoA)-transferase; this enzyme is induced by glucose. Carbon monoxide inactivates acetoacetate decarboxylase. In controlled-pH batch fermentation solventogenesis does not correlate with in vitro activities of butyraldehyde dehydrogenase. Instead, initiation of alcohol formation is accompanied by increased activities of both reduced nicotine adenine dinucleotide (NADH)- and reduced nicotine adenine dinucleotide phosphate (NADPH)-specific alcohol dehydrogenases. The production of acetone in batch fermentation is regulated at the genetic level through combined induction of both CoA-transferase and acetoacetate decarboxylase. These two enzymes are not detected in either batch or continuous culture at or above pH 6.0. This finding explains the inability of the cells to produce acetone at elevated culture pH.     

Extractive fermentation-integrated reaction and product recovery

Summary Refinements have been made to a prototype process for the production of ethanol by extractive fermentation. The process is characterized by thein situ extraction of ethanol from a 7 L continuous stirred tank fermenter and the thermal recovery of ethanol from the extracting solvent, which is circulated in a closed loop through the process. Data are provided to show the efficacy and stability of the process under various operating conditions, and the near complete (>96%) continuous conversion of a 300 g/L glucose feed.     

Growth of Saccharomyces cerevisiae in a chemostat under high glucose conditions

Saccharomyces cerevisiae was grown in a chemostat under high glucose conditions (up to 300 g l^–1). The results support the view that higher glucose feed favors higher ethanol production regardless of the existence of osmotic stress. A low glucose utilization and yield coefficient provides an opportunity to improve continuous fermentation performance in the fuel alcohol industry. The possibility exists of reusing yeast cells and subsequently lower operating costs, and by using an optimal glucose feeding concentration between 100 and 200 g l^–1.