Vertical Rotating Immobilized Cell Reactor of the bacteriumZymomonas mobilis for stable long-term continuous ethanol production

Summary Vertical Rotating Immobilized Cell Reactor was designed and built for glucose conversion into ethanol. Immobilized biomass units withZ. mobilis cells attached into polyurethane foam discs were fixed along a rotating shaft inside the bioreactor. The effect of rotation speed on the concentration of immobilized biomass was studied. Stability of the bioreactor over long-term operation was dependent on the concentration of the immobilized biomass. With fermentation carried out at 6 rpm a constant active immobilized cell concentration of only 34.5 g/l was maintained and used to convert up to 140 g glucose/l into more than 70 g ethanol/l with a volumetric ethanol productivity of 63 g/l/h.     

Kinetic studies on alac-containing strain ofZymomonas mobilis

Summary Batch and continuous culture studies have been carried out on a strain ofZ.mobilis (ZM6306) which can convert lactose directly to ethanol. Previous strain development has established that thelac operon encoded on the transposon Tn951 can be expressed inZ.mobilis. Using a medium containing 80 g/l glucose and 40 g/l lactose, it was found that strain ZM6306 could convert about 13 g/l lactose to 4 g/l ethanol and 6 g/l galactose in continuous culture. Further lactose conversion is likely with increased cell concentration using a cell recycle system.     

High productivity continuous ethanol fermentation with a flocculating mutant strain of Zymomonas mobilis

High fermenter (volumetric) ethanol productivities (80 g/lh^–1) were attained in a simple single-stage continuous-stirred-tank-reactor (CSTR) employing a flocculent mutant of Zymomonas mobilis with a feed containing 100g/l glucose. Under these conditions a final ethanol concentration of 47.6 g/l was obtained, representing a maximum conversion efficiency of 97% of theoretical.Nomenclature SR = Medium glucose concentration (g/l)X Biomass concentration (g/l) - P Ethanol concentration (g/l) - VP Volumetric productivity (g ethanol/l/h) - Yp/s Product yield coefficient (g ethanol/g glucose consumed) - Qp Specific rate of ethanol formation (g ethanol/g cells/h) - D Dilution rate (h^–1) - Dmax Maximum dilution rate: ie., highest dilution rate at which the effluent glucose concentration 4g/l (h^–1)     

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 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.     

High productivity ethanol fermentations with Zymomonas mobilis using continuous cell recycle

Summary Cell recycle studies have been carried out with a strain of Zymomonas mobilis selected for its improved ethanol tolerance and faster rates of glucose uptake and ethanol production. As part of the investigation a capilliary cross-flow microfiltration unit with polyamide membranes has been evaluated in view of its potential advantages (low cost and ability to withstand repeated cleaning with caustic soda). The results demonstrate that ethanol concentrations of 60–65g/l can be sustained at productivities ranging from 120–200g/l/h.     

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.     

Resistance of bacterial film to contamination during use as inoculum in repeated batch fermentation

Summary AnEscherichia coli strain constitutive for -galactosidase was immobilized onto cotton cloth. The resultingE.coli film was used as a resident inoculum in repeated batch fermentations for 30 days in the presence ofBrevibacterium ammoniagenes added as a contaminant. Analysis of -galactosidase production shows that contamination did not decrease the capacity of the film to generateE.coli cells, or decrease theE.coli population on the film.     

Isolation and immobilization ofSclerotium rolfsii protoplasts

Summary Protoplasts fromSclerotium rolfsii were prepared usingTrichoderma harzianum lytic enzymes and immobilized in Ca alginate gels. The immobilized protoplasts when incubated with 1% carboxymethylcellulose in osmotically stabilized induction medium, could secrete endoglucanase and -glucosidase. On repeated use the immobilized preparation retained 36% endoglucanase and 26% -glucosidase activity after 5 cycles.NCL Communication No. 3798     

Effect of acid or enzymatic hydrolysis on ethanol production by Zymomonas mobilis growing on Jerusalem artichoke juice

Summary Ethanol production from the inulin of Jerusalem artichoke byZ. mobilis was studied in batch and continuous fermentations. Both acid or enzymatic hydrolysis were used. In continuous cultures enzymatic hydrolysis showed better results. Ethanol productivities of 17.7 and 29.0 g/l.h were obtained at output concentrationsca 35 g/l (% of conversion 99 and 83; ethanol yield 0.45 g/g). The hydrolysed juice could be used without any nutrient addition.     

Glucose production using immobilized mycelial-associated β-glucosidase of Trichoderma E58

Summary The immobilization of the mycelial-associated -glucosidase of Trichoderma E-58 has been carried out by encapsulating, in calcium alginate beads, the fungal mycelium obtained durinq liquid culture. The activity of this immobilized -glucosidase was found to vary with culture age and to be more thermally stable than the extracellular -glucosidase produced by this organism. The activity of the immobilized enzyme was successfully demonstrated in both static and shake-flask batch reaction mixtures at 50°C using both cellobiose and salicin as substrates.     

Alcoholic fermentation by Zymomonas mobilis: Effect of initial substrate on physiological parameters

Summary The influence of initial substrate concentration on fermentation kinetics of Zymomonas mobilis on glucose has been studied in batch cultures over the range 50–190 gl^-1 glucose. With increasing glucose, parameters relative to growth ( and R_GX) are more rapidly and more noticeably affected than those connected with ethanol production (p and R_GP). The water content of the cells is also affected.     

Kinetic studies on a flocculent strain of Zymomonas mobilis

Summary A flocculent mutant of Zymomonas mobilis has been isolated and kinetic studies carried out in batch and continuous culture. By comparison with the parent strain the specific rates of glucose uptake and ethanol production were decreased by 20%. Cell recycle and semibatch cultures with the flocculent strain resulted in relatively high productivities (viz. 50 g/l/h). However semibatch culture had the additional advantages of an increased ethanol concentration (viz. 82 g/l) and a more stable and controlled environment for cell separation.     

Immobilization studies of whole microbial cells on transition metal activated inorganic supports

Summary Whole cells of Saccharomyces bayanus, Saccharomyces cerevisiae and Zymomonas mobilis were immobilized by chelation/metal-link processes onto porous inorganic carriers. The immobilized yeast cells displayed much higher sucrose hydrolyzing activities (90–517 U/g) than the bacterial, Z. mobilis, cells (0.76–1.65 U/g). The yeast cells chelated on hydrous metal oxide derivative of pumice stone presented higher initial -d-fructofuranosidase (invertase, EC 3.2.1.26) activity (161–517 U/g) than on other derivatives (90–201 U/g). The introduction of an organic bridge between the cells and the metal activator led to a decrease of the initial activity of the immobilized cells, however S. cerevisiae cells immobilized on the carbonyl derivative of titanium (IV) activated pumice stone, by covalent linkage, displayed a very stable behaviour, which in continuous operation at 30° C show only a slightly decrease on invertase activity for a two month period (half-life=470 days). The continuous hydrolysis of a 2% w/v sucrose solution at 30° C in an immobilized S. cerevisiae packed bed reactor was described by a simple kinetic model developed by the authors (Cabral et al., 1984a), which can also be used to predict the enzyme activity of the immobilized cells from conversion degree data.     

Vacuum fermentation for ethanol production using strains of Zymomonas mobilis

Summary Using strains of Z.mobilis, a vacuum fermentation system has been evaluated. The system was designed with the fermentor at atmospheric pressure and an external vacuum vessel (50 mm Hg). Sequential operation of the vacuum vessel was under microprocessor control. The use of Z.mobilis together with the two-stage design of the vacuum system has been found to overcome the problems of oxygen addition and the possibility of contamination reported previously for vacuum fermentations with yeasts. The productivity of 85 g/1/h found in the continuous cell recycle experiments was similar to that reported previously for a strain of S.cerevisiae.     

Diacetyl production by co-immobilized citrate-positiveLactococcus lactis subsp.lactis 3022 and homogenized bovin liver in alginate fibers with double gel layers

Summary Diacetyl production by (Citr⁺)Lactococcus lactis subsp.lactis 3022 cells immobilized in Ca-alginate fine fibers with single layer in the presence of catalase was three times higher than that in the absence of catalase. A co-immobilized culture system of the lactic acid bacterial cells (outer) and the homogenized bovine liver (inner layer) in Ca-alginate fibers with double gel layers was developed. The culture system gave high diacetyl productivity (30 mg/l) for ten repeated batch cultures.     

Growth ofZymomonas on lactose: Gene cloning in combination with mutagenesis

Summary Wild-type strains ofZymomonas mobilis have a limited substrate range of glucose, fructose and sucrose. In order to expand this substrate range, transconjugants ofZ. mobilis containing Lac⁺ plasmids have been constructed. Although -galactosidase is expressed in such strains, they lack the ability to grow on lactose. We now report the development ofZ. mobilis strains capable of growth on lactose. This was achieved in two stages. First, a broad host range plasmid was constructed (pRUT102) which contained the lactose operon under the control of aZ. mobilis promoter plus genes for galactose utilization.Z. mobilis CP4.45 containing pRUT102 was then subjected to mutagenesis combined with continued selection pressure for growth on lactose. One strain,Z. mobilis SB6, produced a turbid culture that yielded 0.25% ethanol from 5% lactose (plus 2% yeast extract) in 15 days.     

Bioconversion of gitoxigenin by immobilized plant cells in a column bioreactor

Summary Daucus carota cells immobilized in a Ca-alginate performed the bioconversion of gitoxigenin to 5-hydroxygitoxigenin in a column bioreactor. The smooth spherical shape of the alginate beads was preserved for more than three weeks. The bioreactor was functional for more than thirty days as detected by the bioconversion activity. The rate of bioconversion was influenced by means of aeration.Issued as National Research Council of Canada Publication Number 19556     

Growth of selected fungi on leaf-protein supernatant

Summary Some 19 strains ofAspergillus niger,A. oryzae, andPaccilomyces spp. are tested for their ability to grow on the supernatant remaining after the expressed juice from sugar beet tops and meadow grass has been heat-treated to precipitate crude leaf protein, and supplemented as required by glucose or ammonium sulphate. With effective strains ofA. niger,A. oryzae,P. elegans orP. variotii and an optimized carbohydrate/nitrogen ratio, over 70% of the organic content of the supernatant is rapidly converted into mycelial biomass of high protein content.     

An airlift-recycle fermenter for microbial desulfurization of coal

Summary An airlift-external recycle fermenter has been constructed and used for the removal of pyritic sulfur from coal samples (4% initial total sulfur) by the thermophilic, sulfur oxidizing organism Sulfolobus acidocaldarius. The airlift fermenter behaved as a well mixed reactor. Approximately, 30% of initial pyritic sulfur has been removed from a 5% coal slurry of ~125 particle size, at a maximum rate of 1.8 mg S/l.h.