Top and bottom yeasts together accelerate ethanol production in molasses fermentation

Summary Alcohol producing top and bottom yeasts were employed individually and together to assess their role in enhancing the rate of ethanol production, in cane molasses fermentation, at 30°C. The combination of top yeastS.cerevisiae NCIM 3281, and bottom yeastS.uvarum NCIM 3509, improved the enthanol production rate by 32.6% in batch fermentation and 25.2% in recycling yeasts cell fermentation as compared to their mean value of individual ethanol production activity.     

Butanol production from cellulosic substrates by sequential co-culture ofClostridium thermocellum andC.acetobutylicum

A sequential co-culture approach was investigated for the conversion of lignocellulosic substrates to fuels and chemicals. Growth ofClostridium acetobutylicum on solka floc (or a mixture of solka floc and aspenwood xylan), in co-culture withC.thermocellum, resulted in the efficient utilization of all the hydrolysis products derived from the lignocellulosic substrates. This co-culture approach resulted in a 1.7–2.6 fold increase in the total fermentation products formed. The majority of the fermentation products were acids and not solvents, however the solventogenesis step could be induced by the addition of butyric acid to the fermentation medium.     

Conversion of sugar-beet particles to ethanol by the bacteriumZymomonas mobilis in solid-state fermentation

Summary The possibility of usingZymomonas mobilis as the microorganism, in solid-state fermentation of sugar-beet particles was investigated. The major factors affecting the process were investigated and related to ethanol yield and productivity. Ethanol yield of 0.48 g/g sugar, volumetric productivity of 12 g/L h, and final ethanol concentration of 130 g/L show the good performance ofZ.mobilis in a solid-state fermentation.     

Regulation of alpha-amylase production inBacillus licheniformis M27 by enzyme end-products in submerged fermentation and its overcoming in solid state fermentation system

Summary Alpha-amylase production byBacillus licheniformis M27 in submerged fermentation was reduced from 480 to 30 units/ml when soluble starch concentration in medium was increased from 0.2 to 1.0%. In contrast, the enzyme production increased by 29 times even with 42 fold increase in the concentration of soluble starch and other starchy substrates in solid state fermentation system. The data establish regulation of the enzyme formation by enzyme end-product in submerged fermentation and ability of solid state fermentation to minimize it significantly. These features were not known earlier.     

Bdellovibrio in methylotrophic bacteria

Summary During the production of single cell protein ofMethylomonas sp. using methanol as the sole carbon source in the pilot plant scale, we isolated aBdellovibrio strain from an abnormal fermentation broth. The abnormality of fermentation caused byBdellovibrio was much like phage infection. However, the plaques formed byBdellovibrio enlarged progressively when plated with host.     

Production of xylanases byChaetomium cellulolyticum during growth on lignocelluloses

Summary Chaetomium cellulolyticum was able to produce xylanases on all the three lignocelluloses: wheat straw, corn stover and aspen wood. Wheat straw was the best. Solid state fermentation of lignocelluloses gave higher yields of xylanases than liquid state fermentation, but it took longer time of incubation.     

Use ofClostridium acetobutylicum P262 for production of solvents from whey permeate

Summary The production of solvents from whey permeate in batch fermentation usingClostridium acetobutylicum P262 was examined. An overall reactor productivity of 0.24 g/l.h was observed, representing a marked improvement over reports using other strains of clostridia. Using a semi-synthetic medium galactose was shown to be as effective a substrate as glucose. When whey permeate was used in which the lactose was hydrolysed prior to fermentation, preferential uptake of glucose over galactose was observed, and such hydrolysis provided no advantage to the fermentation process.     

Production of microbial lipases in a solid state fermentation system

Summary Several filamentous fungi were grown on solid state fermentation systems and selected for their highest yield in lipolytic activity, low protease levels and dairy flavor generation.P. candidum,M. miehei andP. camembertii were the selected ones. A comparison between kinetics in solid and submerged fermentation was performed usingP. candidum, with the solid system giving the highest titers and a stable production.     

Development of a fermentation procedure to produce a tempe-related food using common beans as substrate

Summary A basic procedure was developed to produce a tempe-like product using the mouldRhizopus oligosporus and black common beans (Phaseolus vulgaris) as substrate. The initial pH of the substrate was 5.8, and fermentation was conducted at 37°C with a relative humidity of 70% for 72 hrs. Levels of soluble solids and soluble protein increased dramatically as a result of fermentation. Some changes were as well observed in fatty acid contents of fermented samples. It was concluded that the common bean used was an acceptable substrate for preparing this product.     

Ethanol fermentation of hexose and pentose wood sugars produced by hydrogen-fluoride solvolysis of aspen chips

Summary Hexose and pentose sugars, produced by hydrogen-fluoride solvolysis of aspen wood chips, were totally consumed in a coculture fermentation by Zymomonas mobilis and a mutant of Clostridium saccharolyticum. Z. mobilis converted the glucose to ethanol, while the mutant, which was improved in both ethanol production and tolerance, converted the xylose component to ethanol. A high conversion efficiency of wood sugars to ethanol was obtained, and the cells after the fermentation were successfully used for cell recycle.NRCC no. 23211     

The inhibitory effect of ethanol on ethanol production by Zymomonas mobilis

Summary In an effort to establish the reasons for the limitations in the final ethanol concentration of Zymomonas mobilis fermentation, the effects of CO₂ and ethanol on the fermentation were investigated using continuous and fed-batch cultivation systems. The nucleation and stripping out of CO₂ from the fermenter using diatomaceous earth or nitrogen gas or both exhibited a profound effect on the glucose uptake rate during the early stages of fed-batch fermentation, but did not improve final ethanol yields. The addition of ethanol together with above mentioned experiments confirmed conclusively that ethanol inhibition is responsible for the final ethanol concentration obtainable during Zymomonas mobilis fermentation. The final concentration lies between 90 and 110 gl⁻¹ or approximately 12–15% (v/v) ethanol.     

A simple method for xylanase preparation used for the hydrolysis and fermentation of hemicellulose to butanediol

Summary When culture filtrates ofTrichoderma harzianum E58 were concentrated by passage through an ultrafiltration membrane with a molecular weight exclusion limit of 10,000 Daltons, 80% of the original xylanase activity was recovered in the ultrafiltrates. Culture filtrates and ultrafiltrates which were concentrated by rotary evaporation contained inhibitors which restricted the fermentation of the hemicellulose-derived sugars to 2,3-butanediol. A simple solvent-exchange treatment of the ultrafiltrates could effectively concentrate the xylanases as well as remove the fermentation inhibitors.     

Fed-batch fermentation of glucose to acetate by an improved strain ofClostridium thermoaceticum

The fed-batch approach to the production of acetate from glucose by an improved strain ofClostridium thermoaceticum resulted in better performance than the batch fermentation, especially in media containing an excess (3X) of nutrients and trace salts. At pH 6.6, 46 g/l acetic acid was produced in 192 hours with 93% substrate utilization. In contrast, batch fermentation under similar conditions resulted in a maximum of 35 g/l acetic acid with less than 82% substrate utilization.     

A continuous thermophilic cellulose fermentation in an upflow reactor by aClostridium thermocellum-containing mixed culture

Summary A continuous thermophilic cellulose fermentation by aCl. thermocellum-containing mixed culture was carried out in an upflow reactor for a period of 100 days. The cellulose conversion rate was finally 0.35 g.1^–1.h^–1. Evidence that the fermentation process was influenced by both pH and dilution rate was given by the changes of concentration of the main fermentation products, acetic acid and ethanol. The role of cellodextrins and glucose as reactive intermediates in the process of cellulose breakdown was established.     

Production of ethanol at high temperatures in the fermentation of Jerusalem artichoke juice and a simple medium byKluyveromyces marxianus

Summary Temperatures as high as 36°C and 40°C did not negatively affect the ethanol productivity of Jerusalem artichoke (J.a.) juice batch fermentation and the final concentrations of ethanol were close to those produced at lower temperatures. At higher process temperatures (36–40°C), ethanol toxicity inKluyveromyces marxianus was less important during the fermentation of J.a. juice as compared with a simple medium. In simple medium, the heat-sticking of fermentation was observed and the percentage of unfermented sugars steeply increased from 28°C up to 40°C.     

Use of chemostat for selection ofStreptomyces hygroscopicus mutants altered in regulation of maltose utilization

Summary Streptomyces hygroscopicus mutants showing altered fermentation kinetics were isolated using a selection procedure in a chemostat. Several mutants were obtained which differed in their capacity to produce the macrolide antibiotic turimycin.     

By-products formed during direct conversion of sugar beets to ethanol byZymomonas mobilis in conventional submerged and solid-state fermentations

Summary The nature and amounts of by-products formed during conversion of sugar beets to ethanol byZ. mobilis in Conventional Submerged Fermentation (CSF) and Solid-State Fermentation (SSF) were investigated. It was found that the bacterium produced fewer by-products in SSF than CSF, and that by-products profile was different. The influence of fermentation temperature on synthesis of by-products in SSF was also studied. High fermentation temperature favoured sorbitol synthesis and low fermentation temperature the synthesis of levan. The best results were obtained at 35°C. An ethanol yield of up to 95% of the theoretical value with final ethanol concentration of 142 g/L were obtained.     

Simultaneous saccharification and fermentation by mixed cultures ofBrettanomyces clausenii andPichia spipitis R of SO2-prehydrolysed wood

Summary Using pilot scale Wenger and Stake II reactors for prehydrolysing aspen and coniferous wood chips in the presence of SO₂ catalyst, highly digestible lignocellulosic substrates were generated from which about 90% yields of hemicellulose mostly in monomeric form could be recovered. Simultaneous saccharification and fermentation (SSF) of these SO₂ feedstocks by a mixed culture ofBrettanomyces clausenii andPichia stipitis R resulted in rapid and efficient fermentation giving a final yield of 369 and 360 L ethanol/tonne of the prehydrolysed woods, respectively. BecauseB. clausenii is an excellent cellobiose fermenter, no -glucosidase was needed during SSF.     

An indirect method for studying the fine control of citric acid formation byAspergillus niger

Summary During the main period of citric acid fermentation byAspernillus niger product formation is easily determinable from oxygen uptake and carbon dioxide output rates. This was applied in a study on the response of citrate formation to shifts of some environmental parameters of known importance during fermentation.     

Selection of preculture conditions for solid state fermentation of sugar beet pulp

Summary For the protein upgrading of sugar-beet pulp in solid state fermentation byTrichoderma reesei andFusarium oxysporum, serveral conditions were studied to prepare an economical preculture for large scale process. The best performance was shown by a preculture obtained in 24 h from 1.5 % molasses solution at pH 4.5–5.0 with 1.0 % milled beet pulp.