Change in product selectivity during the production of glyceric acid from glycerol by Gluconobacter strains in the presence of methanol
© Sato et al.; licensee Springer. 2013
Received: 18 March 2013
Accepted: 20 March 2013
Published: 2 April 2013
To enhance the value-added use of methanol-containing raw glycerol derived from biodiesel fuel production, the effect of methanol supplementation on glyceric acid (GA) production by Gluconobacter spp. was investigated. We first conducted fed-batch fermentation with Gluconobacter frateurii NBRC103465 using raw glycerol as a feeding solution. GA productivity decreased with increasing dihydroxyacetone (DHA) formation when the raw glycerol contained methanol. The results of this experiment and comparative experiments using a synthetic solution modeled after the raw glycerol indicate that the presence of methanol caused a change in the concentrations of GA and DHA, two glycerol derivatives produced during fermentation. Other Gluconobacter spp. also decreased GA production in the presence of 1% (v/v) methanol. In addition, purified membrane-bound alcohol dehydrogenase (mADH) from Gluconobacter oxydans, which is a key enzyme in GA production, showed a decrease in dehydrogenase activity toward glycerol as the methanol concentration increased. These results strongly suggest that the observed decrease in GA production by Gluconobacter spp. resulted from the methanol-induced inhibition of mADH-mediated glycerol oxidation.
KeywordsAcetic acid bacteria Glyceric acid Methanol Membrane-bound alcohol dehydrogenase Raw glycerol
Biodiesel fuel (BDF), a class of renewable energy, is widely used to conserve fossil fuels and reduce carbon dioxide emissions. One method of BDF production involves transesterification between triacylglycerols, which are present in plant oils and animal fats, and methanol under alkaline conditions. This reaction forms glycerol as a byproduct at 10% of the initial amount of triacylglycerol. Because BDF production has rapidly increased in the US and in European and Asian countries (Rahmat et al. 2010; Glycerin market report, 2011), residual glycerol waste (raw glycerol) is now being used in chemical industries as an alternative feedstock. Therefore, many research groups have developed chemical and biological techniques for the conversion of glycerol into value-added chemicals such as epichlorohydrine (Kubicek et al. 2005), 1,3-propanediol (Rehman et al. 2008), 3-hydroxypropionic acid (Rathnasingh et al. 2009), and 2,3-dihydroxypropionic acid (glyceric acid, GA) (Habe et al. 2009a).
Raw glycerol derived from BDF production has diverse properties that depend on the initial raw materials (e.g., origin of triacylglycerol), reaction conditions, and manufacturing process. The transesterification of triacylglycerol with methanol requires excess methanol for efficient BDF production, resulting in an impure, methanol-containing raw glycerol. Although methanol recovery by evaporation during the BDF manufacturing process is relatively easy, it requires additional energy and is costly. Therefore, the use of raw glycerol is economically preferable, and so the technological utility of glycerol that contains impurities, such as methanol and alkali metals, should be developed. Indeed, raw glycerol after purification has relatively high purity and represents a useful raw material for chemical production, whereas impure raw glycerol is often wasted. Therefore, it is important to investigate the effects of impurities in raw glycerol, particularly methanol, on chemical production.
Our recent research has focused on microbial GA production from glycerol and the applications of GA because of its simple but chiral structure, which provides building blocks for various fine chemicals (Habe et al. 2009b). GA itself has been reported to have biological activity, such as accelerating the oxidation of ethanol (Eriksson et al. 2007) and enhancing the viability of ethanol-dosed gastric cells (Habe et al. 2011a). Applications of GA as a value-added material, including as an antitrypsin compound (Habe et al. 2011b), a bioplastic monomer (Fukuoka et al. 2011), and novel surfactants (Fukuoka et al. 2012), have also been investigated. With regard to the production of GA, a biological method that involves the enantioselective conversion of glycerol to D-GA by acetic acid bacterial fermentation has been developed (Habe et al. 2009c). Gluconobacter frateurii NBRC103465 showed the highest GA productivity (136 g/L), whereas Acetobacter tropicalis NBRC16470 produced D-GA with 99% ee (Habe et al. 2009a).
Concerning the effect of raw glycerol containing methanol on GA production by acetic acid bacteria, we demonstrated that Gluconobacter sp. NBRC3259 produced less GA when raw glycerol from which impurities had not been removed was applied (Habe et al. 2009d). It was also shown that this strain produced only a small amount of GA in the presence of 1% (v/v) methanol. In contrast, we developed a fed-batch fermentation method that uses glycerol in an alkaline solution for glycerol feeding and pH control (Habe et al. 2009a). Because raw glycerol usually contains alkaline metals such as sodium and potassium, it is of interest to investigate the feasibility of utilizing raw glycerol in fed-batch fermentation.
Materials and methods
Bacterial strains and culture conditions
Gluconobacter frateurii NBRC103465, G. frateurii THD32 (Toyama et al. 2005) and its ΔsldA mutant (Toyama et al. 2005; Soemphol et al. 2008), and Gluconobacter oxydans IFO12528 and its ΔadhA mutant (Habe et al. 2009a) were used for GA production. Seed cultures of the Gluconobacter strains were prepared in 5 mL of glucose medium composed of 5 g/L glucose, 5 g/L yeast extract, 5 g/L polypepton, and 1 g/L MgSO4 · 7H2O at 30°C and 200 rpm for 24 h. The seed cultures (1.5 mL) were transferred to 300-mL Erlenmeyer flaks containing 30 mL of glycerol medium composed of 170 g/L glycerol, 10 g/L polypepton, 1 g/L yeast extract, 1 g/L MgSO4 · 7H2O, 0.9 g/L KH2PO4, and 0.1 g/L K2HPO4. The cultures were incubated at 30°C and 200 rpm on a rotary shaker for 96 h. When needed, 50 mg/L kanamycin for the ΔadhA strain of G. oxydans and the ΔsldA strain of G. frateurii THD32 was added to the medium.
Jar fermentation experiment
Gluconobacter frateurii was cultured in a 5-L jar fermenter containing 2.5 L of glycerol medium (Habe et al. 2009a). The seed cultures (90 mL) were used for inoculation. Cultivation was done at 30°C, 500 rpm, and 0.5 vvm, and maintained at pH 6 using raw glycerol derived from BDF production or the model solution. The raw glycerol contained the following components: glycerol, 66.4% (w/v); methanol, 30.9% (w/v); and sodium salt, 0.54% (w/v); pH 12 (Habe et al. 2009d). In contrast, based on the raw glycerol composition, a synthetic solution modeled after the raw glycerol was prepared with the following pure reagents: glycerol, 66% (w/v); methanol, 30% (w/v); and sodium hydroxide, 1 M.
Analysis of the culture broth
The glycerol, GA, and DHA concentrations in the culture broth were determined by high-performance liquid chromatography (HPLC), as described previously (Habe et al. 2009a). In addition, the methanol concentration was determined by HPLC using the same method as that employed for the GA assay.
Bacterial growth was evaluated by OD measurements at 600 nm using a V-530 UV/VIS spectrophotometer (JASCO Corp., Tokyo, Japan).
Evaluation of the ability of G. oxydans and its ΔadhA mutant to assimilate methanol
Whole cells of G. oxydans IFO12528 and its ΔadhA strain were used to investigate methanol consumption. Cells were precultured in 30 mL of glucose medium in 300-mL Erlenmeyer flasks at 30°C and 200 rpm for 24 h. Cells collected from 60 mL of the culture by centrifugation were suspended in 30 mL of glycerol medium containing 0–10% (v/v) methanol. The initial OD600 was ~2.0. The flasks were shaken at 30°C and 200 rpm, and an aliquot of the broth was removed at regular intervals for HPLC.
Glycerol dehydrogenase activity in the presence of methanol was evaluated using purified, membrane-bound G. oxydans alcohol dehydrogenase (mADH) based on the method of Adachi et al. (1978) with modifications. Briefly, the reaction mixture contained 0.4 mL of McIlvaine buffer (pH 5.0), 10 mM potassium ferricyanide, 8 mM sodium azide, enzyme solution, 5-20% (w/v) glycerol, and/or 0-2% (w/v) methanol in a total volume of 1.0 mL. The reaction was carried out at 25°C for 5 min by adding ferricyanide solution, and stopped by adding 0.5 mL of ferric sulfate-Dupanol reagent (Wood et al. 1962). The resulting mixture was allowed to stand at 25°C for 20 min, and then the absorbance of the solution was measured at 660 nm to estimate the intensity of the Prussian blue color formed. The oxidation of 1 μmol of substrate was equal to 4.0 absorbance units. One unit of dehydrogenase activity was defined as the amount of enzyme that catalyzed the oxidation of 1 μmol of substrate in 1 min. After the determination of dehydrogenase activity toward 1.2 and 2% (w/v) methanol, that towards 20% (w/v) glycerol in the presence of various methanol concentrations was calculated by subtracting the value of the activity toward methanol from that toward glycerol in the presence of methanol.
The protein concentration of the purified enzyme was determined by the Lowry method using bovine serum albumin as the standard.
Fed-batch GA fermentation by G. frateurii NBRC103465 using raw glycerol derived from BDF production and its modeled solution
GA production by Gluconobacter spp. in the presence of methanol
Effect of methanol supplementation on GA and DHA production by Gluconobacter spp.
G. frateurii NBRC103465
G. frateurii THD32
G. oxydans IFO12528
Initial methanol (%, v/v)
28.2 ± 0.3
14.4 ± 0.7
23.0 ± 0.3
6.8 ± 0.3
18.8 ± 1.0
5.9 ± 0.4
15.9 ± 0.6
38.0 ± 1.7
25.1 ± 5.8
24.1 ± 1.4
33.7 ± 0.3
51.9 ± 2.1
Effect of methanol supplementation on the G. oxydans ΔadhA mutant and purified mADH
Our data indicate that GA production by G. frateurii NBRC103465 decreased when the microbe was cultured using raw glycerol (Figure 2) and a synthetic solution modeled after the raw glycerol, which contains 30% (w/v) methanol (Figure 3), for pH control. This phenomenon also occurred in flask cultures of other Gluconobacter spp. (Table 1). Thus, methanol was likely the cause of the decrease in GA production.
Previously, we showed that mADH is a key enzyme in the production of GA from glycerol, and that its deletion from G. oxydans (Δ adhA) resulted in a strain incapable of producing GA (Habe et al. 2009a). In addition, mADH exhibits higher dehydrogenase activity toward methanol than toward glycerol (Adachi et al. 1978). Therefore, we hypothesized that mADH catalyzed the oxidation of methanol more easily than the oxidation of glycerol, resulting in a decrease in the methanol consumption rate in the broth of the ΔadhA mutant. However, no differences in methanol consumption between the parental and ΔadhA strains of G. oxydans grown in glycerol containing up to 10% (v/v) methanol were detected (Figure 4). Next, the inhibitory effect of methanol on glycerol oxidation by mADH was evaluated using purified mADH. A comparison of mADH activity at high glycerol concentrations with or without methanol demonstrated that methanol inhibited glycerol dehydrogenase activity (Figure 5). This suggests that methanol decreased the rate of glycerol oxidation by mADH, resulting in reduced GA production. Activity of mADH toward various amount of glycerol (5, 10, 15, and 20%, w/v) in the presence of methanol (0.3%, w/v) was also measured. A gradual increase in dehydrogenase activity was observed as the glycerol concentration increased, although methanol inhibited dehydrogenase activity constantly by approximately 60% as compared to that in the absence of methanol (data not shown). This could suggest noncompetitive inhibition by methanol in mADH glycerol dehydrogenation; however, detailed kinetic analyses of mADH activity toward glycerol and/or methanol will be necessary to clarify the mechanism whereby methanol inhibits the oxidation of glycerol by mADH. In addition, fed-batch cultivation with a raw glycerol model solution (Figure 3) revealed that the methanol concentration in the broth reached 0.4 and 1.5% after 12 and 18 h of cultivation, respectively (data not shown). Considering the IC50 value for methanol in the oxidation of glycerol by mADH, GA production was probably inhibited even in the early stages of cultivation.
Because the ΔadhA strain of G. oxydans showed similar DHA production profiles in the presence of methanol as well as the parental strain (Figure 4), methanol was supposed to enhance DHA production regardless of GA production. In contrast, our preliminarily experiment showed that a membrane-bound glycerol dehydrogenase (SldAB)-defective mutant of G. frateurii THD32 (ΔsldA), which is incapable of producing DHA, showed a clear decrease in GA production in the presence of 1% methanol (data not shown), as well as the parental strain G. frateurii THD32. This suggests that methanol inhibited GA production regardless of DHA production. These complementary experiments imply that methanol would have an influence on activities of individual enzymes involved in each production. In contrast, DHA production by G. frateurii THD32 was not significantly changed in the presence of 1% methanol (Table 1). Hence, studies on cell responses at the transcriptomic and metabolomic levels in the presence of methanol will help elucidate the detailed mechanism of methanol-related DHA production and the difference among Gluconobacter strains in effect of methanol on DHA production.
Gluconobacter spp. tend to produce both GA and DHA at a high concentration (170 g/L) of glycerol (Table 1). In terms of DHA production, this is a problem; that is, a high concentration of glycerol during DHA fermentation results in increased byproduct (GA) formation (Figure 1). In addition, a higher initial concentration of glycerol decreased the rates of cell growth and DHA production (Claret et al. 1992). Therefore, attempts have been made to improve DHA production by process engineering (Hu et al. 2011) and strain development (Habe et al. 2010). However, our data show that G. oxydans, an industrial strain used for DHA production, produced a large quantity of DHA from 170 g/L glycerol with less GA production in the presence of 1% methanol (Table 1). This indicates that efficient DHA production by G. oxydans using a high concentration of glycerol can be achieved by adding a small amount of methanol to the culture. In this case, methanol seemed to act not only as an inhibitor of GA formation, but also as an enhancer of DHA formation. This suggests that BDF-derived raw glycerol containing methanol would be a good source material for efficient and economical DHA production with less byproduction of GA, although a clear mechanism for enhancing DHA production is unclear.
In summary, GA production in the presence of methanol decreased with the production of DHA by Gluconobacter spp. The dehydrogenase activity of G. oxydans mADH toward glycerol was inhibited by methanol, suggesting that the rate of glycerol oxidation catalyzed by mADH determines the product selectivity of Gluconobacter spp. between GA and DHA. Recombinant G. frateurii with an enhanced ability to assimilate methanol or mADHs with a lower affinity for methanol will be necessary for the efficient production of GA from raw glycerol.
This work was financially supported in part by the Japan-US Cooperation Project for Research and Standardization of Clean Energy Technologies from the Ministry of Economy, Trade, and Industry of Japan.
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