Effects of edd and pgi Disruptions on Inosine Accumulation in Escherichia coli

Using an inosine-producing mutant of Escherichia coli, the contributions of the central carbon metabolism for overproducing inosine were investigated. Sodium gluconate instead of glucose was tested as a carbon source to increase the supply of ribose-5-phosphate through the oxidative pentose phosphate pathway. The edd (6-phosphogluconate dehydrase gene)-disrupted mutant accumulated 2.5 g/l of inosine from 48 g/l of sodium gluconate, compared with 1.4 g/l of inosine in the edd wild strain. The rpe (ribulose phosphate 3-epimerase gene)-disrupted mutant resulted in low cell growth and low inosine production on glucose and on gluconate. The disruption of pgi (glucose-6-phosphate isomerase gene) was effective for increasing the accumulation of inosine from glucose but resulted in low cell growth. The pgi-disrupted mutant accumulated 3.7 g/l of inosine from 40 g/l of glucose when 8 g/l of yeast extract was added to the medium. Furthermore, to improve effective utilization of adenine, the yicP (adenine deaminase gene)-disrupted mutant was evaluated. It showed higher inosine accumulation, of 3.7 g/l, than that of 2.8 g/l in the yicP wild strain when 4 g/l of yeast extract was added to the medium.     

Nucleotide mutations in purA gene and pur operon promoter discovered in guanosine- and inosine-producing Bacillus subtilis strains

The promoter region of the pur operon, which contains 12 genes for inosine monophosphate biosynthesis from phosphoribosylpyrophosphate, and the purA gene, encoding the adenylosuccinate synthetase, were compared among wild-type and three purine-producing Bacillus subtilis strains. A single nucleotide deletion at position 55 (relative to translation start site) in purA gene was found in a high inosine-producing strain and in a high guanosine-producing strain, which correlates with the absence of adenylosuccinate synthetase activity in these strains. Within the pur operon promoter of high guanosine-producing strain, in addition to a single nucleotide deletion in PurBox1 and a single nucleotide substitution in PurBox2, there were 4 substitutions in the flanking region of the PurBoxes and 32 nucleotide mutations in the 5′ untranslated region. These mutations may explain the purine accumulation in purine-producing strains and be helpful to the rational design of high-yield recombinant strains.     

Production and Application of Syringomycin E as an Organic Fungicide Seed Protectant against Pythium Damping‐off

Syringomycin E (SRE) is a cyclic lipodepsinonapeptide with potent antifungal activity and is produced by certain strains of Pseudomonas syringae pv. syringae. In this study, its potential as an organic‐compatible agrofungicide and vegetable seed treatment against the soilborne pathogen Pythium ultimum var. ultimum was examined. A variant of P. syringae pv. syringae strain B301D with enhanced SRE‐producing capabilities was isolated and grown in a bioreactor with SRE yields averaging 50 mg/l in 40 h. SRE was extracted and purified through a large‐scale chromatography system using organic‐compatible processes and reagents. The minimum concentrations of the purified product required to inhibit 50 and 90% of P. ultimum oospore germination were determined as 31.3 and 250 μg/ml, respectively. Drench treatment of cucumber seeds in P. ultimum‐infested potting medium (500 oospores/g) with 50 μg/ml SRE or water with no SRE resulted in 90.2 ± 4.5% and 65.7 ± 4.6% germination rates, respectively. Seed coating with 0.03% (w/w) SRE allowed 65.7 ± 4.6% seedlings to germinate on naturally infested soil while 100.0 ± 0.0% of non‐coated seeds were unable to germinate due to Pythium infection. Organic‐compatible and scalably produced SRE is potentially a novel organic fungicide seed protectant.     

Metabolism of glucose and xylose as single and mixed feed in <Emphasis Type="Italic">Debaryomyces nepalensis</Emphasis> NCYC 3413: production of industrially important metabolites

Efficient conversion of hexose and pentose (glucose and xylose) by a single strain is a very important factor for the production of industrially important metabolites using lignocellulose as the substrate. The kinetics of growth and polyol production by Debaryomyces nepalensis NCYC 3413 was studied under single and mixed substrate conditions. In the presence of glucose, the strain produced ethanol (35.8 ± 2.3 g/l), glycerol (9.0 ± 0.2 g/l), and arabitol (6.3 ± 0.2 g/l). In the presence of xylose, the strain produced xylitol (38 ± 1.8 g/l) and glycerol (18 ± 1.0 g/l) as major metabolites. Diauxic growth was observed when the strain was grown with different combinations of glucose/xylose, and glucose was the preferred substrate. The presence of glucose enhanced the conversion of xylose to xylitol. By feeding a mixture of glucose at 100 g/l and xylose at 100 g/l, it was found that the strain produced a maximum of 72 ± 3 g/l of xylitol. A study of important enzymes involved in the synthesis of xylitol (xylose reductase (XR) and xylitol dehydrogenase (XDH)), glycerol (glycerol-3-phosphate dehydrogenase (G3PDH)) and ethanol (alcohol dehydrogenase (ADH)) in cells grown in the presence of glucose and xylose revealed high specific activity of G3PDH and ADH in cells grown in the presence of glucose, whereas high specific activity of XR, XDH, and G3PDH was observed in cells grown in the presence of xylose. To our knowledge, this is the first study to elaborate the glucose and xylose metabolic pathway in this yeast strain.     

Fermentation of corn fiber hydrolysate to lactic acid by the moderate thermophile <Emphasis Type="Italic">Bacillus coagulans</Emphasis>

A strain of Bacillus coagulans that converted mixed sugars of glucose, xylose, and arabinose to l-lactic acid with 85% yield at 50°C was isolated from composted dairy manure. The strain was tolerant to aldehyde growth inhibitors at 2.5 g furfural/l, 2.5 g 5-hydroxymethylfurfural/l, 2.5 g vanillin/l, and 1.2 g p-hydroxybenzaldehyde/l. In a simultaneous saccharification and fermentation process, the strain converted a dilute-acid hydrolysate of 100 g corn fiber/l to 39 g lactic acid/l in 72 h at 50°C. Because of its inhibitor tolerance and ability to fully utilize pentose sugars, this strain has potential to be developed as a biocatalyst for the conversion of agricultural residues into valuable chemicals.     

Multiple induced mutagenesis for improvement of ethanol production by <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis>

Kluyveromyces marxianus GX-15 was mutated multiple times by alternately treatment with UV irradiation and NTG for two cycles. Four mutant strains with improved ethanol yield were obtained. The maximum ethanol concentration, ethanol yield coefficient and theoretical ethanol yield of the best mutant strain, GX-UN120, was 69 g/l, 0.46 g/g and 91%, respectively, when fermenting 150 g glucose/l at 40°C. The corresponding values for GX-15 were 58 g/l, 0.39 g/g and 76%, respectively. GX-UN120 grew well in 11% (v/v) of ethanol, while GX-15 could not grow when ethanol was greater than 8% (v/v).     

Improvement of acetic acid tolerance and fermentation performance of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> by disruption of the <Emphasis Type="Italic">FPS1</Emphasis> aquaglyceroporin gene

The FPS1 gene coding for the Fps1p aquaglyceroporin protein of an industrial strain of Saccharomyces cerevisiae was disrupted by inserting CUP1 gene. Wild-type strain, CE25, could only grow on YPD medium containing less than 0.45% (v/v) acetic acid, while recombinant strain T12 with FPS1 disruption could grow on YPD medium with 0.6% (v/v) acetic acid. Under 0.4% (v/v) acetic acid stress (pH 4.26), ethanol production and cell growth rates of T12 were 1.7 ± 0.1 and 0.061 ± 0.003 g/l h, while those of CE25 were 1.2 ± 0.1 and 0.048 ± 0.003 g/l h, respectively. FPS1 gene disruption in an industrial ethanologenic yeast thus increases cell growth and ethanol yield under acetic acid stress, which suggests the potential utility of FPS1 gene disruption for bioethanol production from renewable resources such as lignocelluloses.     

Comparison of separate hydrolysis and fermentation and simultaneous saccharification and fermentation processes for ethanol production from wheat straw by recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> strain FBR5

Ethanol production by recombinant Escherichia coli strain FBR5 from dilute acid pretreated wheat straw (WS) by separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF) was studied. The yield of total sugars from dilute acid (0.5% H₂SO₄) pretreated (160 °C, 10 min) and enzymatically saccharified (pH 5.0, 45 °C, 72 h) WS (86 g/l) was 50.0 ± 1.4 g/l. The hydrolyzate contained 1,184 ± 19 mg furfural and 161 ± 1 mg hydroxymethyl furfural per liter. The recombinant E. coli FBR5 could not grow at all at pH controlled at 4.5 to 6.5 in the non-abated wheat straw hydrolyzate (WSH) at 35 °C. However, it produced 21.9 ± 0.3 g ethanol from non-abated WSH (total sugars, 44.1 ± 0.4 g/l) in 90 h including the lag time of 24 h at controlled pH 7.0 and 35 °C. The bioabatement of WS was performed by growing Coniochaeta ligniaria NRRL 30616 in the liquid portion of the pretreated WS aerobically at pH 6.5 and 30 °C for 15 h. The bacterium produced 21.6 ± 0.5 g ethanol per liter in 40 h from the bioabated enzymatically saccharified WSH (total sugars, 44.1 ± 0.4 g) at pH 6.0. It produced 24.9 ± 0.3 g ethanol in 96 h and 26.7 ± 0.0 g ethanol in 72 h per liter from bioabated WSH by batch SSF and fed-batch SSF, respectively. SSF offered a distinct advantage over SHF with respect to reducing total time required to produce ethanol from the bioabated WS. Also, fed-batch SSF performed better than the batch SSF with respect to shortening the time requirement and increase in ethanol yield.     

Display of α-amylase on the surface of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> cells by using NCgl1221 as the anchoring protein,and production of glutamate from starch

We developed a new cell surface display system in Corynebacterium glutamicum based on the C-terminally truncated NCgl1221 anchor protein to increase l-glutamate production from starch directly. The C-terminally truncated NCgl1221 protein is a mutant NCgl1221 and leads to the constitutive export of l-glutamate. The N terminus of α-amylase (AmyA) was fused to truncated NCgl1221, and the resulting fusion protein was expressed on the cell surface by IPTG induction. Localization of the fusion protein was confirmed by immunofluorescence microscopy and flow cytometric analysis. The results of l-glutamate fermentation showed that the soluble starch was utilized to grow and produce l-glutamate by the recombinant strain displaying AmyA. The amount of soluble starch was reduced from 30.0 ± 2.8 to 4.5 ± 0.7 g/l under non-inducing condition and from 50.0 ± 2.4 to 12.5 ± 1.1 g/l under biotin limitation in 36 h. The glutamate concentration in the medium was transiently increased in 14 h under no induction, while under biotin-limiting condition, glutamate production was continuously elevated during fermentation. The amount of glutamate reached 19.3 ± 2.1 g/l after 26 h of fermentation with biotin limitation, which was greater than that produced by the strain using PgsA, one of the poly-γ-glutamate synthetase complexes, as the anchor protein under the same condition. Therefore, the truncated NCgl1221 anchor protein has more advantages than the PgsA anchor protein in glutamate fermentation because truncated NCgl1221 leads to the constitutive export of l-glutamate without any treatments.     

Mutation-Screening in <Emphasis Type="SmallCaps">l</Emphasis>-(+)-Lactic Acid Producing Strains by Ion Implantation

In this paper, in order to obtain some industrial strains with high yield of l-(+)-lactic acid, the wild type strain Lactobacillus casei CICC6028 was mutated by nitrogen ions implantation. By study, it was found that the high positive mutation rate was obtained when the output power was 10 keV and the dose of N⁺ implantation was 50 × 2.6 × 10¹³ ions/cm². In addition, the initial screening methods were also studied, and it was found that the transparent halos method was unavailable, for some high yield strains of l-(+)-lactic acid were missed. Then a mutant strain which was named as N-2 was isolated, its optimum fermentation temperature was 40°C and the l-(+)-lactic acid yield was 136 g/l compared to the original strain whose optimum fermentation temperature was 34°C and l-(+)-lactic acid production was 98 g/l. Finally, High Performance Liquid Chromatography method was used to analyze the purity of l-(+)-lactic acid that was produced by the mutant N-2, and the result showed the main production of N-2 was l-(+)-lactic acid.     

Engineered disulfide bonds improve thermostability and activity of L‐isoleucine hydroxylase for efficient 4‐HIL production in Bacillus subtilis 168

4‐Hydroxyisoleucine, a promising drug, has mainly been applied in the clinical treatment of type 2 diabetes in the pharmaceutical industry. l ‐Isoleucine hydroxylase specifically converts l‐ Ile to 4‐hydroxyisoleucine. However, due to its poor thermostability, the industrial production of 4‐hydroxyisoleucine has been largely restricted. In the present study, the disulfide bond in l ‐isoleucine hydroxylase protein was rationally designed to improve its thermostability to facilitate industrial application. The half‐life of variant T181C was 4.03 h at 50°C, 10.27‐fold the half‐life of wild type (0.39 h). The specific enzyme activity of mutant T181C was 2.42 ± 0.08 U/mg, which was 3.56‐fold the specific enzyme activity of wild type 0.68 ± 0.06 U/mg. In addition, molecular dynamics simulation was performed to determine the reason for the improvement of thermostability. Based on five repeated batches of whole‐cell biotransformation, Bacillus subtilis 168/pMA5‐ido^T181C recombinant strain produced a cumulative yield of 856.91 mM (126.11 g/L) 4‐hydroxyisoleucine, which is the highest level of productivity reported based on a microbial process. The results could facilitate industrial scale production of 4‐hydroxyisoleucine. Rational design of disulfide bond improved l ‐isoleucine hydroxylase thermostability and may be suitable for protein engineering of other hydroxylases.     

Efficient chemical and enzymatic saccharification of the lignocellulosic residue from <Emphasis Type="Italic">Agave tequilana</Emphasis> bagasse to produce ethanol by <Emphasis Type="Italic">Pichia caribbica</Emphasis>

Bagasse of Agave tequilana (BAT) is the residual lignocellulosic waste that remains from tequila production. In this study we characterized the chemical composition of BAT, which was further saccharified and fermented to produce ethanol. BAT was constituted by cellulose (42%), hemicellulose (20%), lignin (15%), and other (23%). Saccharification of BAT was carried out at 147°C with 2% sulfuric acid for 15 min, yielding 25.8 g/l of fermentable sugars, corresponding to 36.1% of saccharificable material (cellulose and hemicellulose contents, w/w). The remaining lignocellulosic material was further hydrolyzed by commercial enzymes, ~8.2% of BAT load was incubated for 72 h at 40°C rendering 41 g/l of fermentable sugars corresponding to 73.6% of the saccharificable material (w/w). Mathematic surface response analysis of the acid and enzymatic BAT hydrolysis was used for process optimization. The results showed a satisfactory correlation (R ² = 0.90) between the obtained and predicted responses. The native yeast Pichia caribbica UM-5 was used to ferment sugar liquors from both acid and enzymatic hydrolysis to ethanol yielding 50 and 87%, respectively. The final optimized process generated 8.99 g ethanol/50 g of BAT, corresponding to an overall 56.75% of theoretical ethanol (w/w). Thus, BAT may be employed as a lignocellulosic raw material for bioethanol production and can contribute to BAT residue elimination from environment.     

Optimization of ethanol,citric acid,and α-amylase production from date wastes by strains of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>, <Emphasis Type="Italic">Aspergillus niger</Emphasis>, and <Emphasis Type="Italic">Candida guilliermondii</Emphasis>

The present study deals with submerged ethanol, citric acid, and α-amylase fermentation by Saccharomyces cerevisiae SDB, Aspergillus niger ANSS-B5, and Candida guilliermondii CGL-A10, using date wastes as the basal fermentation medium. The physical and chemical parameters influencing the production of these metabolites were optimized. As for the ethanol production, the optimum yield obtained was 136.00 ± 0.66 g/l under optimum conditions of an incubation period of 72 h, inoculum content of 4% (w/v), sugars concentration of 180.0 g/l, and ammonium phosphate concentration of 1.0 g/l. Concerning citric acid production, the cumulative effect of temperature (30°C), sugars concentration of 150.0 g/l, methanol concentration of 3.0%, initial pH of 3.5, ammonium nitrate concentration of 2.5 g/l, and potassium phosphate concentration of 2.5 g/l during the fermentation process of date wastes syrup did increase the citric acid production to 98.42 ± 1.41 g/l. For the production of α-amylase, the obtained result shows that the presence of starch strongly induces the production of α-amylase with a maximum at 5.0 g/l. Among the various nitrogen sources tested, urea at 5.0 g/l gave the maximum biomass and α-amylase estimated at 5.76 ± 0.56 g/l and 2,304.19 ± 31.08 μmol/l/min, respectively after 72 h incubation at 30°C, with an initial pH of 6.0 and potassium phosphate concentration of 6.0 g/l.     

Effect of prebiotics on bacteriocin production and cholesterol lowering activity of <Emphasis Type="Italic">Pediococcus acidilactici</Emphasis> LAB 5

The in vitro influence of three prebiotics viz. mannitol, maltodextrin and sorbitol was evaluated on probiotic aspects like bile salt tolerance, cholesterol lowering efficiency and bacteriocin production of the strain, Pediococcus acidilactici LAB 5 which was isolated from vacuum packed fermented meat product. Optimum temperature for bacteriocin production in MRS medium was 37°C. The strain deconjugated bile salt (sodium taurocholate) to 607.66 ± 10.894 μg/ml from initial bile salt concentration 3 mg/ml. In vitro cholesterol removal capability of the strain P. acidilactici LAB 5 was 62 ± 2.742 μg/ml. Prebiotic sorbitol had a positive influence on the probiotic parameters like better cell growth, bacteriocin production and cholesterol removal capability. Anaerobic condition had influenced largely on bile salt deconjugation, cholesterol removal and bacteriocin production. Synbiotic treatment of P. acidilactici LAB 5 with sorbitol for 1 month lowered the plasma cholesterol level to 176.34 ± 12.66 μg/ml in comparison to untreated one (208.76 ± 20.27 μg/ml) in Swiss albino mice. Intestinal adherence of P. acidilactici LAB 5 was also more in synbiotic condition than only in probiotic and control treatments.     

Improvement of robustness and ethanol production of ethanologenic Saccharomyces cerevisiae under co-stress of heat and inhibitors

Bioethanol is an attractive alternative to fossil fuels. Saccharomyces cerevisiae is the most important ethanol producer. However, yeast cells are challenged by various environmental stresses during the industrial process of ethanol production. The robustness under heat, acetic acid, and furfural stresses was improved for ethanologenic S. cerevisiae in this work using genome shuffling. Recombinant yeast strain R32 could grow at 45°C, and resist 0.55% (v/v) acetic acid and 0.3% (v/v) furfural at 40°C. When ethanol fermentation was conducted at temperatures ranging from 30 to 42°C, recombinant strain R32 always gave high ethanol production. After 42 h of fermentation at 42°C, 187.6 ± 1.4 g/l glucose was utilized by recombinant strain R32 to produce 81.4 ± 2.7 g/l ethanol, which were respectively 3.4 and 4.1 times those of CE25. After 36 h of fermentation at 40°C with 0.5% (v/v) acetic acid, 194.4 ± 1.2 g/l glucose in the medium was utilized by recombinant strain R32 to produce 84.2 ± 4.6 g/l of ethanol. The extent of glucose utilization and ethanol concentration of recombinant strain R32 were 6.3 and 7.9 times those of strain CE25. The ethanol concentration produced by recombinant strain R32 was 8.9 times that of strain CE25 after fermentation for 48 h under 0.2% (v/v) furfural stress at 40°C. The strong physiological robustness and fitness of yeast strain R32 support its potential application for industrial production of bioethanol from renewable resources such as lignocelluloses.     

Strain improvement of <Emphasis Type="Italic">Lactobacillus lactis</Emphasis> for <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid production

Three mutants, isolated by repeated UV mutagenesis of Lactobacillus lactis NCIM 2368, produced increased d-lactic acid concentrations. These mutants were compared with the wild type using 100 g hydrolyzed cane sugar/l in the fermentation medium. One mutant, RM2-24, produced 81 g lactic acid/l which was over three times that of the wild type. The highest d-lactic acid (110 g/l) in batch fermentation was obtained with 150 g cane sugar/l with a 73% lactic acid yield. The mutant utilizes cellobiose efficiently, converting it into d-lactic acid suggesting the presence of cellobiase. Thus, this strain could be used to obtain d-lactic acid from cellulosic materials that are pre-hydrolyzed with cellulase.     

Fatty acid profiles of Trachinus radiatus Cuvier, 1829 (Perciformes‐Trachinoidei,Trachinidae)

The goal of this study was to analyse the fatty acid (FA) profiles of the streaked (starry) weever (Trachinus radiatus), a prized food fish in the countries of its distribution. Fish (N = 20) were sampled in July 2011. Location: 42.761019°N, 17.765090°W; Adriatic Sea, Elaphite Islands near Dubrovnik, Croatia, at 5–10 m depth using longline hooks; body length ranges: 24.1–47.2 cm, weight ranges: 120–960 g. Morphological species determination was genetically confirmed (Folmer region of COI gene). Biochemical analysis of T. radiatus muscular tissue (filet) revealed average ± SD dry matter of 252.3 ± 14.8 g/kg w.w.; moisture of 747.7 ± 14.8 g/kg w.w., and ash of 28.0 ± 6.9 g/kg w.w. Intramuscular crude protein content exceeded the total lipid (TL = 11.9 ± 4.0 g/kg w.w.) content approximately 17.7 fold. Unsaturated FA (UFA) was higher than saturated FA (SFA), with a predominance of polyunsaturated FA (PUFA). The ω3:ω6 ratio was 4.9:1, respectively. Among individually determined fatty acids, the PUFA 22:6n3 (DHA) was highly present (29.99 ± 2.75% TL) followed by a relatively high 20:5n3 (EPA) content. There was 25 fold higher EPA content than of substrate αLNA, and a 15.5 fold higher DHA content to DPAn3. Such ratios indicate that besides trophic ingestion, FA bioconversion elongase/desaturase synthesis pathways toward ω3 PUFA in Weevers could be highly efficient.     

Effect of chemical and microbial vitamin B<Subscript>12</Subscript> analogues on production of vitamin B<Subscript>12</Subscript>

Strain improvement by genetic manipulation or optimization of fermentation conditions for overproduction of vitamin B₁₂ has a drawback due to feed back inhibition. To resist the feed back inhibition by analogues of vitamin B₁₂ in Propionibacterium freudenrechii subsps. shermanii (OLP-5), we have tested with microbially separated B₁₂ analogues from three different strains. Microbial analogues were differentiated from commercially available vitamin B₁₂ by high pressure liquid chromatography and spectrophotometric method. An analogue isolated from NRRL-B-4327 was shown to increase vitamin B₁₂ concentration from 18.53 ± 0.15 to 31.67 ± 0.58 mg/l in OLP-5 strain. The presence of chemical analogue (ICH₂ Co(DH)₂ (H₂Py)₄) increased vitamin B₁₂ production from 16.13 ± 0.15 to 18.53 ± 0.15 mg/l in OLP-5. These findings revealed that addition of B₁₂ analogues in fermentation media have developed strain resistance to feed back inhibition by vitamin B₁₂.     

A study of the efficiency of edible oils degraded in alkaline conditions by <Emphasis Type="Italic">Pseudomonas aeruginosa</Emphasis> SS-219 and <Emphasis Type="Italic">Acinetobacter</Emphasis> sp. SS-192 bacteria isolated from Japanese soil

High lipid concentration contained in wastewater inhibits the activity of microorganisms in biological wastewater treatment systems such as activated sludge and methane fermentation. To reduce the inhibitory effects, microorganisms capable of efficiently degrading edible oils were screened from various environmental sources. From Japanese soil, we isolated 2 bacteria strains with high degradation abilities at an alkaline pH without consumption of biological oxygen demand (BOD) constituents. Acinetobacter sp. strain SS-192 and Pseudomonas aeruginosa strain SS-219 degraded 77.5 ± 0.6% and 89.5 ± 1.5%, respectively, of 3,000 ppm of mixed oil consisting of salad oil/lard/beef tallow (1/1/1, w/w/w) at 37°C and pH 9.0 in 24 h. Efficient degradation by the two strains occurred at pH 8–9 and 25–40°C. Strain SS-219 degraded lipids even at pH 3. The degradation rate of 3,000 ppm of salad oil, lard, and beef tallow by strain SS-192 was 79.9 ± 2.6%, 63.6 ± 1.9%, and 70.1 ± 1.2%, respectively, during a 24-h cultivation. The degradation rate of 3,000 ppm of salad oil, lard, and beef tallow by strain SS-219 was 82.3 ± 2.1%, 71.9 ± 2.2%, and 71.0 ± 1.1%, respectively, during a 24-h cultivation. After mixed oil degradation by both strains, the BOD value of the cell culture increased from 2,100 ppm to 3,200–4,000 ppm. The fact that neither strain utilizes BOD ingredients will be beneficial to pretreatment of methane fermentation systems such as upflow anaerobic sludge blanket reactors. In addition, the growth of usual heterotrophic microorganisms utilizing soluble BOD can be suppressed under alkaline pH.