Abstract

The effect of trace metal ions (Co2+, Cu2+, Fe2+, Mn2+, Mo6+, Ni2+, Zn2+, SeO4   and WO4  ) on growth and ethanol production by an ethanologenic acetogen, Clostridium ragsdalei was investigated in CO:CO2-grown cells. A standard acetogen medium (ATCC medium no. 1754) was manipulated by varying the concentrations of trace metals in the media. Increasing the individual concentrations of Ni2+, Zn2+, SeO4   and WO4   from 0.84, 6.96, 1.06, and 0.68 μM in the standard trace metals solution to 8.4, 34.8, 5.3, and 6.8 μM, respectively, increased ethanol production from 35.73 mM under standard metals concentration to 176.5, 187.8, 54.4, and 72.3 mM, respectively. Nickel was necessary for growth of C. ragsdalei. Growth rate (μ) of C. ragsdalei improved from 0.34 to 0.49 (day−1), and carbon monoxide dehydrogenase (CODH) and hydrogenase (H2ase)-specific activities improved from 38.45 and 0.35 to 48.5 and 1.66 U/mg protein, respectively, at optimum concentration of Ni2+. At optimum concentrations of WO4   and SeO4  , formate dehydrogenase (FDH) activity improved from 32.3 to 42.6 and 45.4 U/mg protein, respectively. Ethanol production and the activity of FDH reduced from 35 mM and 32.3 U/mg protein to 1.14 mM and 8.79 U/mg protein, respectively, upon elimination of WO4   from the medium. Although increased concentration of Zn2+ enhanced growth and ethanol production, the activities of CODH, FDH, H2ase and alcohol dehydrogenase (ADH) were not affected by varying the Zn2+ concentration. Omitting Fe2+ from the medium decreased ethanol production from 35.7 to 6.30 mM and decreased activities of CODH, FDH, H2ase and ADH from 38.5, 32.3, 0.35, and 0.68 U/mg protein to 9.07, 7.01, 0.10, and 0.24 U/mg protein, respectively. Ethanol production improved from 35 to 54 mM when Cu2+ was removed from the medium. The optimization of trace metals concentration in the fermentation medium improved enzyme activities (CODH, FDH, and H2ase), growth and ethanol production by C. ragsdalei.

Introduction

The environmental concerns over the use of petroleum-based fuels and their limited supplies have generated a great interest in producing ethanol as an alternative fuel. The use of bioethanol (ethanol from biomass) reduces the dependence on imported oil, supports agriculture, and limits greenhouse gas emissions. In the United States, bioethanol is primarily produced from the fermentation of corn starch, which is presently facing critical issues such as potential diversion of food and fodder-grade feedstocks towards biofuel production, its indirect effects on land-use change, and its limited supply [24]. Hence, to make the bioethanol production processes sustainable, rigorous criteria must be considered and best practices in terms of choice of feedstocks and its direct and indirect environmental and socio-economic effects should be utilized [11]. Bioethanol produced from lignocellulosic biomass grown on agriculturally marginal lands (e.g., switchgrass) and waste biomass (e.g., agricultural and forestry wastes) could compete with present supplies [21] and provide significant environmental and economic benefits over corn starch-based ethanol [11].

Lignocellulosic biomass can be converted to ethanol by direct fermentation of sugars obtained by acidic/enzymatic hydrolysis of the biomass (cellulosic ethanol) [19]. Although this process has tremendous potential, and over the past several years great advances have been made in this area [17], there are several disadvantages associated with this technology, such as the difficulties in handling and converting diverse sources of biomass to ethanol, and the lignin component of biomass is left unutilized. A promising approach for conversion of biomass to ethanol is the stepwise process of gasification and microbial fermentation [30]. In gasification, all biomass components including lignin are gasified to synthesis gas (syngas: a mixture of primarily CO, CO2, and H2) [30]. Syngas is fermented to several commodity chemicals, including ethanol by a group of obligatory anaerobic bacteria known as acetogens [30]. As a feed-stock flexible process, syngas fermentation can utilize a wide variety of biomass sources that are combustible and non-food based, such as municipal solid waste, tires, and residual agricultural biomass [30].

Acetogens utilize the acetyl-CoA/Wood-Ljungdahl pathway for production of acetyl-CoA, a precursor of cellular biomass, acetate, and ethanol. Key enzymes of this pathway include formate dehydrogenase (FDH), bifunctional carbon monoxide dehydrogenase/acetyl CoA synthase (CODH/ACS), and hydrogenase (H2ase), all of which are metalloenzymes [9]. In addition, solvent-producing clostridia also have iron- and zinc-containing alcohol dehydrogenase (ADH) [15, 26] that plays a key role by catalyzing the reduction of acetyl CoA to ethanol [6].

Considering the key role of metalloenzymes in the metabolism of acetogens, a study was undertaken to investigate the effect of trace metals (Co2+, Cu2+, Fe2+, Mn2+, Mo6+, Ni2+, Zn2+, SeO4  , and WO4  ) on growth, production of ethanol, production of acetate and enzyme activities (CODH, FDH, H2ase, and ADH) by a recently isolated ethanologenic acetogen, Clostridium ragsdalei using syngas components. C. ragsdalei was isolated from duck pond sediment, and produces ethanol and acetate from syngas components [12] (US Pat. No. US 2008/0057554 A1). It was hypothesized that the optimization of trace metal concentrations in the culture medium might enhance the activity of metalloenzymes, thus improving growth and ethanol production by C. ragsdalei.

Materials and methods

Bacterial strain, media, and growth conditions

The bacterium used in this study was Clostridium ragsdalei (ATCC PTA 7826), which was isolated in our laboratory from duck pond sediment in Brandt Park, Norman, OK, USA. The standard acetogen medium (ATCC medium no. 1754) for cultivation of C. ragsdalei was prepared using strict anaerobic techniques [2] under an atmosphere of N2:CO2 (80:20). The medium (per liter) contained: mineral solution, 25 ml [29]; trace metal solution, 10 ml [29]; vitamin solution, 10 ml [29]; 2-(N-morpholino)ethanesulfonic acid (MES), 20 g; yeast extract (Difco, Becton Dickinson, Sparks, M.D.), 0.5 g; 0.1% resazurin, 0.1 ml and cysteine-sulfide reducing agent, 2.5 ml [29]. The pH of the medium was adjusted to 6.1 using NaOH. The trace metal solution (per liter) contained MnSO4·H2O (1.0 g), Fe(NH4)2(SO4)2·6H2O (0.8 g), CoCl2·6H2O (0.2 g), ZnSO4·7H2O (0.2 g), CuCl2·2H2O (0.02 g), NiCl2·6H2O (0.02 g), Na2MoO4·2H2O (0.02 g), Na2SeO4 (0.02 g), and Na2WO4 (0.02 g). The concentrations of individual trace metals in the media are presented in Table 1. Metals present in the yeast extract were removed as metal ion phosphates using a procedure derived from dephosphorylating media components [20].

Concentration of trace metals in standard growth medium, ATCC 1754 (1X)

Trace metal(μM)
Co8.40
Cu1.17
Fe20.40
Mn59.17
Mo0.83
Ni0.84
Se1.06
W0.68
Zn6.96
Trace metal(μM)
Co8.40
Cu1.17
Fe20.40
Mn59.17
Mo0.83
Ni0.84
Se1.06
W0.68
Zn6.96

Concentration of trace metals in standard growth medium, ATCC 1754 (1X)

Trace metal(μM)
Co8.40
Cu1.17
Fe20.40
Mn59.17
Mo0.83
Ni0.84
Se1.06
W0.68
Zn6.96
Trace metal(μM)
Co8.40
Cu1.17
Fe20.40
Mn59.17
Mo0.83
Ni0.84
Se1.06
W0.68
Zn6.96

Clostridium ragsdalei was grown in anaerobic culture tubes (Bellco Glass, Inc., Vineland, NJ, USA) containing 5 ml of medium and a gas mixture of CO:N2:CO2 (70:24:6 pressurized to 230 kPa gauge) in the head space. Since CO is sparingly soluble in water, the tubes were incubated on their sides at 36°C on a rotary shaker (100–120 rpm) to maximize gas–liquid mixing.

Fermentation experiment

Batch fermentation experiments were conducted to examine the effect of trace metals (Co2+, Cu2+, Fe2+, Mn2+, Mo6+, Ni2+, Zn2+, SeO4  , and WO4  ) on growth and ethanol production by C. ragsdalei. The concentration of trace metals in standard trace metals solution (Table 1) is denoted as 1X throughout the study. The concentrations of each trace metal was either increased ten-fold (10X) with respect to standard metal concentration (1X) (Table 1) or eliminated (0X) from the media. Once effective metals for growth and ethanol production were identified, different concentrations (1X, 5X, 10X, and 20X) of each metal were titrated to find their optimal concentrations for enhanced ethanol production. Fermentation experiments were performed in triplicate in 160-ml Wheaton serum vials containing 10 ml of medium. C. ragsdalei cells were transferred three times in the media with each trace metal concentrations to minimize the metal ion carry over via inoculum into the experimental media. A 1% inoculum was used in all experiments. The bottles were fed with CO (440-kPa gauge) and incubated at 36°C on a rotary shaker. Once the cells were grown, the headspace gases were exchanged with CO (440-kPa gauge) every 24 h for 10 days. At the end of the experiments, final pH and growth were recorded and the samples were analyzed for acetate and ethanol.

A time course experiment was conducted on the optimized concentrations metals and to study their effects on growth and fermentation products formed over a period of 10 days. The time course experiment was conducted in 500-ml Wheaton serum bottles with 50 ml of medium. Experiments were conducted according to the procedure described above, except that samples (1.5 ml) were collected every 24 h for 10 days. The samples were analyzed for pH, growth, and fermentation products.

Analytical methods

Growth was monitored by measuring optical density (OD) at 600 nm with a Beckman Coulter DU 640 spectrophotometer (Bausch and Lomb, Rochester, NY). Growth rate (μ) was derived from OD data as described elsewhere [4]. The fermentation products (i.e., acetate and ethanol) were analyzed quantitatively using a Shimadzu GC-8A gas chromatograph (Shimadzu, Maryland, USA) equipped with a flame ionization detector (FID) and helium was used as the carrier gas. The column and the injector/detector temperatures were maintained at 155 and 200°C, respectively. The glass column (2.6 m) was packed with Carbopack BDA (80/120 mesh) and 4% Carbowax 20 M resin (Supelco Inc., Bellefonte, PA). Data were analyzed with a Shimadzu C-R8A integrator.

Enzyme assays

Enzyme activities (FDH, CODH, H2ase, and ADH) were determined spectrophotometrically as the substrate-dependent reduction of methyl viologen (MV) in 2-ml cuvettes as described previously [18]. The cultures in the enzyme assays were grown in 500-ml Wheaton serum bottles with 50 ml of media as stated above. The exponential phase cultures were used for enzyme assays. Protein concentrations were estimated using bicinchoninic acid method [28] with bovine serum albumin as a standard.

Results

Screening of trace metals for their effect on ethanol production

The effect of different trace metals on growth rate and production of ethanol and acetate by C. ragsdalei is presented in Table 2. C. ragsdalei produced 35 mM of ethanol and 9 mM of acetate under the standard medium (1X) condition. At higher concentrations (10X) of Ni2+, Zn2+, SeO4   and WO4   ethanol production increased to 176, 190, 75, and 55 mM, respectively. Ethanol production decreased to 27.01, 6.30, 22.02, and 1.55 mM when Co2+, Fe2+, Mo2+ and WO4   were eliminated (0X) from the media, indicating that these metals were required for ethanol production. An increase in ethanol production to 54 mM was noticed when Cu2+ was removed (0X) from the media. Ethanol production did not change considerably at higher concentration (10X) of Cu2+, Co2+, Fe2+, and Mn2+, and also when Mn2+, Zn2+, and SeO4   were omitted (0X) from the media. A decrease in ethanol production to 23.64 mM was observed at higher concentration (10X) of Mo2+.

Effect of trace metals on growth rate (μ), final pH (pHf), production of ethanol, and production of acetate by C. ragsdalei after 10 days of growth

Trace metalsGrowth rate (day−1)pHfEthanol (mM)Acetate (mM)
1Xa0.34 ± 0.0065.935.73 ± 2.058.87 ± 0.31
Ni
 0XNo growth6.1No growthNo growth
 10X0.49 ± 0.0025.8176.52 ± 5.6214.96 ± 2.78
Zn
 0X0.34 ± 0.0185.933.48 ± 1.4211.20 ± 3.24
 10X0.48 ± 0.0025.6187.80 ± 8.5618.56 ± 2.36
Se
 0X0.30 ± 0.0125.938.32 ± 2.129.56 ± 1.34
 10X0.30 ± 0.0125.954.35 ± 3.238.64 ± 0.96
W
 0X0.30 ± 0.0155.91.14 ± 0.0418.56 ± 0.75
 10X0.44 ± 0.0035.972.29 ± 1.8010.87 ± 0.82
Cu
 0X0.30 ± 0.0025.954.09 ± 2.6211.83 ± 1.49
 10X0.30 ± 0.0085.936.63 ± 1.579.17 ± 1.27
Fe
 0X0.33 ± 0.0045.96.30 ± 0.9215.34 ± 0.30
 10X0.34 ± 0.0075.935.87 ± 1.728.50 ± 1.15
Co
 0X0.31 ± 0.0015.927.01 ± 1.317.02 ± 0.85
 10X0.34 ± 0.0015.937.34 ± 0.696.70 ± 1.03
Mo
 0X0.31 ± 0.0045.922.02 ± 0.907.38 ± 0.65
 10X0.31 ± 0.0015.923.64 ± 1.428.06 ± 0.34
Mn
 0X0.31 ± 0.0015.933.11 ± 1.468.75 ± 0.35
 10X0.31 ± 0.0015.936.78 ± 0.249.11 ± 0.04
Trace metalsGrowth rate (day−1)pHfEthanol (mM)Acetate (mM)
1Xa0.34 ± 0.0065.935.73 ± 2.058.87 ± 0.31
Ni
 0XNo growth6.1No growthNo growth
 10X0.49 ± 0.0025.8176.52 ± 5.6214.96 ± 2.78
Zn
 0X0.34 ± 0.0185.933.48 ± 1.4211.20 ± 3.24
 10X0.48 ± 0.0025.6187.80 ± 8.5618.56 ± 2.36
Se
 0X0.30 ± 0.0125.938.32 ± 2.129.56 ± 1.34
 10X0.30 ± 0.0125.954.35 ± 3.238.64 ± 0.96
W
 0X0.30 ± 0.0155.91.14 ± 0.0418.56 ± 0.75
 10X0.44 ± 0.0035.972.29 ± 1.8010.87 ± 0.82
Cu
 0X0.30 ± 0.0025.954.09 ± 2.6211.83 ± 1.49
 10X0.30 ± 0.0085.936.63 ± 1.579.17 ± 1.27
Fe
 0X0.33 ± 0.0045.96.30 ± 0.9215.34 ± 0.30
 10X0.34 ± 0.0075.935.87 ± 1.728.50 ± 1.15
Co
 0X0.31 ± 0.0015.927.01 ± 1.317.02 ± 0.85
 10X0.34 ± 0.0015.937.34 ± 0.696.70 ± 1.03
Mo
 0X0.31 ± 0.0045.922.02 ± 0.907.38 ± 0.65
 10X0.31 ± 0.0015.923.64 ± 1.428.06 ± 0.34
Mn
 0X0.31 ± 0.0015.933.11 ± 1.468.75 ± 0.35
 10X0.31 ± 0.0015.936.78 ± 0.249.11 ± 0.04

a  1X standard concentrations of all the trace metals, 0X elimination of trace metal, 10X tenfold higher metal concentration than 1X

Effect of trace metals on growth rate (μ), final pH (pHf), production of ethanol, and production of acetate by C. ragsdalei after 10 days of growth

Trace metalsGrowth rate (day−1)pHfEthanol (mM)Acetate (mM)
1Xa0.34 ± 0.0065.935.73 ± 2.058.87 ± 0.31
Ni
 0XNo growth6.1No growthNo growth
 10X0.49 ± 0.0025.8176.52 ± 5.6214.96 ± 2.78
Zn
 0X0.34 ± 0.0185.933.48 ± 1.4211.20 ± 3.24
 10X0.48 ± 0.0025.6187.80 ± 8.5618.56 ± 2.36
Se
 0X0.30 ± 0.0125.938.32 ± 2.129.56 ± 1.34
 10X0.30 ± 0.0125.954.35 ± 3.238.64 ± 0.96
W
 0X0.30 ± 0.0155.91.14 ± 0.0418.56 ± 0.75
 10X0.44 ± 0.0035.972.29 ± 1.8010.87 ± 0.82
Cu
 0X0.30 ± 0.0025.954.09 ± 2.6211.83 ± 1.49
 10X0.30 ± 0.0085.936.63 ± 1.579.17 ± 1.27
Fe
 0X0.33 ± 0.0045.96.30 ± 0.9215.34 ± 0.30
 10X0.34 ± 0.0075.935.87 ± 1.728.50 ± 1.15
Co
 0X0.31 ± 0.0015.927.01 ± 1.317.02 ± 0.85
 10X0.34 ± 0.0015.937.34 ± 0.696.70 ± 1.03
Mo
 0X0.31 ± 0.0045.922.02 ± 0.907.38 ± 0.65
 10X0.31 ± 0.0015.923.64 ± 1.428.06 ± 0.34
Mn
 0X0.31 ± 0.0015.933.11 ± 1.468.75 ± 0.35
 10X0.31 ± 0.0015.936.78 ± 0.249.11 ± 0.04
Trace metalsGrowth rate (day−1)pHfEthanol (mM)Acetate (mM)
1Xa0.34 ± 0.0065.935.73 ± 2.058.87 ± 0.31
Ni
 0XNo growth6.1No growthNo growth
 10X0.49 ± 0.0025.8176.52 ± 5.6214.96 ± 2.78
Zn
 0X0.34 ± 0.0185.933.48 ± 1.4211.20 ± 3.24
 10X0.48 ± 0.0025.6187.80 ± 8.5618.56 ± 2.36
Se
 0X0.30 ± 0.0125.938.32 ± 2.129.56 ± 1.34
 10X0.30 ± 0.0125.954.35 ± 3.238.64 ± 0.96
W
 0X0.30 ± 0.0155.91.14 ± 0.0418.56 ± 0.75
 10X0.44 ± 0.0035.972.29 ± 1.8010.87 ± 0.82
Cu
 0X0.30 ± 0.0025.954.09 ± 2.6211.83 ± 1.49
 10X0.30 ± 0.0085.936.63 ± 1.579.17 ± 1.27
Fe
 0X0.33 ± 0.0045.96.30 ± 0.9215.34 ± 0.30
 10X0.34 ± 0.0075.935.87 ± 1.728.50 ± 1.15
Co
 0X0.31 ± 0.0015.927.01 ± 1.317.02 ± 0.85
 10X0.34 ± 0.0015.937.34 ± 0.696.70 ± 1.03
Mo
 0X0.31 ± 0.0045.922.02 ± 0.907.38 ± 0.65
 10X0.31 ± 0.0015.923.64 ± 1.428.06 ± 0.34
Mn
 0X0.31 ± 0.0015.933.11 ± 1.468.75 ± 0.35
 10X0.31 ± 0.0015.936.78 ± 0.249.11 ± 0.04

a  1X standard concentrations of all the trace metals, 0X elimination of trace metal, 10X tenfold higher metal concentration than 1X

Acetate production increased to 15 and 18.6 mM at increased concentrations (10X) of Ni2+ and Zn2+, respectively. An increase in acetate production to 15.34 and 18.64 mM was also observed when Fe2+ and WO4   were eliminated (0X) from the media. There were no appreciable changes in acetate production at greater concentration (10X) of Co2+, Cu2+, Fe2+, Mn2+, Mo6+, SeO4  , and WO4  , and also when Co2+, Cu2+, Mn2+, Mo6+, Zn2+, and SeO4   were omitted (0X) from the media.

The growth rate of C. ragsdalei improved at increased concentrations (10X) of Ni2+, Zn2+, and WO4  2−. Nickel was necessary for growth of C. ragsdalei. The growth rate of C. ragsdalei for remaining metals (Co2+, Cu2+, Fe2+, Mn2+, Mo6+, and SeO4  ) was similar to that with standard metals (1X) in growth medium. The final pH of the media was similar under the various metal concentrations.

Effect of optimized concentrations of Ni2+, Zn2+, WO4  , and SeO4   on growth rate, ethanol production, and acetate production

The optimal concentrations of Ni2+, Zn2+, SeO4  , and WO4   for ethanol production were 8.5, 35, 5, and 7 μM and the concentrations of ethanol produced at these concentrations were 180, 200, 60, and 90 mM, respectively (Fig. 1). Ethanol production at the standard metal concentrations (1X) was 35 mM. The optimum concentrations of Ni2+, Zn2+, SeO4  , and WO4   increased cell growth, which became more pronounced by the addition of Ni2+ and Zn2+. Acetate production at optimum concentrations of Ni2+, Zn2+, and SeO4   was similar to that produced under control conditions.
Effect of different concentrations of nickel (Ni), zinc (Zn), selenite (Se), and tungstate (W), on growth rate (/day), production of ethanol, and production of acetate by C. ragsdalei
Fig. 1

Effect of different concentrations of nickel (Ni), zinc (Zn), selenite (Se), and tungstate (W), on growth rate (/day), production of ethanol, and production of acetate by C. ragsdalei

Time course experiment

Cultures of C. ragsdalei demonstrated improved growth under optimized concentration of Ni2+ and Zn2+ compared to the control (1X) (Fig. 2) and remained in stationary phase of growth for 7–8 days before cell lysis was observed. However, cells lysed in the standard medium (1X) after 3–4 days of growth, which was also observed for optimum concentrations of WO4   and SeO4   (Fig. 3). When Ni+, Zn+, SeO4  , and WO4   were used at their optimum concentrations, and Cu2+ was eliminated from the trace metals solution (CuNiZnSeW), a significant increase in growth was observed, and cells remained in the stationary phase until the end of the experiment (10 days). An increase in ethanol production was observed once the cultures entered into the exponential phase, which continued to increase until the stationary phase (Figs. 2, 3). An increase in acetate production was observed during the exponential phase of growth in all metals concentrations tested, which started decreasing once C. ragsdalei cells entered into the stationary phase of growth. The transient reduction in acetate concentration was associated with an increase in ethanol concentration (Figs. 2, 3).
Effect of optimal concentrations of nickel (Ni) and zinc (Zn) on final pH, growth rate (/day), production of ethanol, and production of acetate by C. ragsdalei
Fig. 2

Effect of optimal concentrations of nickel (Ni) and zinc (Zn) on final pH, growth rate (/day), production of ethanol, and production of acetate by C. ragsdalei

 
Effect of optimal concentrations of selenate (Se), tungstate (W), and optimal concentrations of copper-nickel-zinc-selenite-tungstate combined together (CuNiZnSeW) on final pH, growth rate (/day), production of ethanol, and production of acetate by C. ragsdalei
Fig. 3

Effect of optimal concentrations of selenate (Se), tungstate (W), and optimal concentrations of copper-nickel-zinc-selenite-tungstate combined together (CuNiZnSeW) on final pH, growth rate (/day), production of ethanol, and production of acetate by C. ragsdalei

Effect of Ni2+, Zn2+, SeO4  , and WO4   on enzyme activities in Clostridium ragsdalei

The optimum concentration of Ni2+ stimulated the activities of CODH and H2ase; whereas, the activity of FDH was enhanced at optimum concentrations of SeO4   and WO4   (Table 3). Inclusion of optimum concentrations of SeO4   and WO4   together in the medium had the same effect on FDH activity as the individual additions of SeO4   and WO4   (Table 3). Enzyme activity of CODH, FDH, H2ase, and ADH were reduced when Fe2+ was removed from the medium, whereas at increased concentration of Fe2+ (10X), there was no change in enzyme activities as compared to those under the standard metal concentration (1X) (Table 3). Although the optimum concentration of Zn2+ increased the growth and ethanol production (Fig. 1), enzyme activities were not affected by the concentration of Zn2+ (Table 3).

Effect of trace metals on activities (U/mg protein) of carbon monoxide dehydrogenase (CODH), formate dehydrogenase (FDH), hydrogenase (H2ase), and alcohol dehydrogenase (ADH) by C. ragsdalei

Growth conditionsaFDHCODHH2aseADH
1X32.25 ± 1.4138.45 ± 1.680.35 ± 0.010.68 ± 0.01
Ni
 0XNo growthNo growthNo growthNo growth
 10X34.6 ± 1.1348.46 ± 1.571.66 ± 0.060.65 ± 0.12
Se
 0X31.97 ± 0.9238.01 ± 0.490.32 ± 0.030.83 ± 0.06
 5X42.62 ± 0.7337.07 ± 3.350.28 ± 0.010.61 ± 0.03
W
 0X8.79 ± 0.1636.24 ± 0.290.33 ± 0.030.77 ± 0.01
 10X45.44 ± 0.2133.57 ± 0.790.41 ± 0.080.68 ± 0.05
Se (5X) + W (10X)35.46 ± 0.3436.25 ± 0.410.31 ± 0.020.71 ± 0.13
Zn
 0X31.96 ± 1.2135.64 ± 2.500.32 ± 0.030.65 ± 0.03
 5X34.02 ± 0.0836.81 ± 2.390.44 ± 0.040.75 ± 0.03
Fe
 0X7.01 ± 0.629.07 ± 0.040.10 ± 0.040.24 ± 0.02
 10X35.65 ± 0.3337.51 ± 0.500.39 ± 0.050.63 ± 0.01
Growth conditionsaFDHCODHH2aseADH
1X32.25 ± 1.4138.45 ± 1.680.35 ± 0.010.68 ± 0.01
Ni
 0XNo growthNo growthNo growthNo growth
 10X34.6 ± 1.1348.46 ± 1.571.66 ± 0.060.65 ± 0.12
Se
 0X31.97 ± 0.9238.01 ± 0.490.32 ± 0.030.83 ± 0.06
 5X42.62 ± 0.7337.07 ± 3.350.28 ± 0.010.61 ± 0.03
W
 0X8.79 ± 0.1636.24 ± 0.290.33 ± 0.030.77 ± 0.01
 10X45.44 ± 0.2133.57 ± 0.790.41 ± 0.080.68 ± 0.05
Se (5X) + W (10X)35.46 ± 0.3436.25 ± 0.410.31 ± 0.020.71 ± 0.13
Zn
 0X31.96 ± 1.2135.64 ± 2.500.32 ± 0.030.65 ± 0.03
 5X34.02 ± 0.0836.81 ± 2.390.44 ± 0.040.75 ± 0.03
Fe
 0X7.01 ± 0.629.07 ± 0.040.10 ± 0.040.24 ± 0.02
 10X35.65 ± 0.3337.51 ± 0.500.39 ± 0.050.63 ± 0.01

Specific activity = 1 μmol of substrate reduced.min−1 mg−1 of protein

a  1X standard concentrations of all the trace metals, 0X elimination of trace metals, 5X fivefold higher concentration than 1X, 10X tenfold higher concentration than 1X

Effect of trace metals on activities (U/mg protein) of carbon monoxide dehydrogenase (CODH), formate dehydrogenase (FDH), hydrogenase (H2ase), and alcohol dehydrogenase (ADH) by C. ragsdalei

Growth conditionsaFDHCODHH2aseADH
1X32.25 ± 1.4138.45 ± 1.680.35 ± 0.010.68 ± 0.01
Ni
 0XNo growthNo growthNo growthNo growth
 10X34.6 ± 1.1348.46 ± 1.571.66 ± 0.060.65 ± 0.12
Se
 0X31.97 ± 0.9238.01 ± 0.490.32 ± 0.030.83 ± 0.06
 5X42.62 ± 0.7337.07 ± 3.350.28 ± 0.010.61 ± 0.03
W
 0X8.79 ± 0.1636.24 ± 0.290.33 ± 0.030.77 ± 0.01
 10X45.44 ± 0.2133.57 ± 0.790.41 ± 0.080.68 ± 0.05
Se (5X) + W (10X)35.46 ± 0.3436.25 ± 0.410.31 ± 0.020.71 ± 0.13
Zn
 0X31.96 ± 1.2135.64 ± 2.500.32 ± 0.030.65 ± 0.03
 5X34.02 ± 0.0836.81 ± 2.390.44 ± 0.040.75 ± 0.03
Fe
 0X7.01 ± 0.629.07 ± 0.040.10 ± 0.040.24 ± 0.02
 10X35.65 ± 0.3337.51 ± 0.500.39 ± 0.050.63 ± 0.01
Growth conditionsaFDHCODHH2aseADH
1X32.25 ± 1.4138.45 ± 1.680.35 ± 0.010.68 ± 0.01
Ni
 0XNo growthNo growthNo growthNo growth
 10X34.6 ± 1.1348.46 ± 1.571.66 ± 0.060.65 ± 0.12
Se
 0X31.97 ± 0.9238.01 ± 0.490.32 ± 0.030.83 ± 0.06
 5X42.62 ± 0.7337.07 ± 3.350.28 ± 0.010.61 ± 0.03
W
 0X8.79 ± 0.1636.24 ± 0.290.33 ± 0.030.77 ± 0.01
 10X45.44 ± 0.2133.57 ± 0.790.41 ± 0.080.68 ± 0.05
Se (5X) + W (10X)35.46 ± 0.3436.25 ± 0.410.31 ± 0.020.71 ± 0.13
Zn
 0X31.96 ± 1.2135.64 ± 2.500.32 ± 0.030.65 ± 0.03
 5X34.02 ± 0.0836.81 ± 2.390.44 ± 0.040.75 ± 0.03
Fe
 0X7.01 ± 0.629.07 ± 0.040.10 ± 0.040.24 ± 0.02
 10X35.65 ± 0.3337.51 ± 0.500.39 ± 0.050.63 ± 0.01

Specific activity = 1 μmol of substrate reduced.min−1 mg−1 of protein

a  1X standard concentrations of all the trace metals, 0X elimination of trace metals, 5X fivefold higher concentration than 1X, 10X tenfold higher concentration than 1X

Discussion

Acetogens utilize the acetyl-CoA/Wood-Ljungdahl pathway for production of acetyl-CoA, a precursor of cell biomass, acetate, and ethanol [9]. Hence, to improve the growth and fermentation products, it is necessary to improve the carbon flow to acetyl-CoA, which requires upstream manipulations in this pathway. In this study, the activities of the key metalloenzymes of this pathway were enhanced by optimizing the concentrations of trace metals in the growth medium, which improved growth and ethanol production by C. ragsdalei.

The ethanol production and enzyme activities (CODH, FDH, H2ase, and ADH) of C. ragsdalei were reduced when Fe2+ was removed (0X) from the medium. All the key metalloenzymes of acetyl-CoA pathway (CODH, FDH, and H2ase) are iron-sulfur proteins [5, 10, 32]. Hence, a reduction in enzyme activities (CODH, FDH, H2ase, and ADH) and ethanol production by C. ragsdalei upon elimination of Fe2+ from the growth media was anticipated. However, increasing Fe2+ concentration (10X) had no effect on the growth, production of ethanol, or production of acetate, which indicates that Fe2+ concentration in the growth medium became saturating at a concentration exceeding 20.4 μM (1X) for the growth and metabolism of C. ragsdalei.

FDH catalyzes the first reaction on the methyl branch of the acetyl Co-A pathway, where it reduces CO2 to formate [9]. The metal co-factors of FDH in clostridia are reported to be variable, where iron, tungsten, selenium, and/or molybdenum have been shown to be the components of FDH [16, 31, 32]. FDH in acetogens contain selenium and tungsten [14, 31, 32]; whereas, in non-acetogenic clostridia such C. formicoaceticum, molybdenum-containing FDH is present [16]. In acetate-producing acetogens, the presence of tungsten and selenium in FDH has been suggested to function as cofactors, promoting the FDH-mediated reduction of CO2 [32]. C. ragsdalei produced acetate and ethanol as the fermentation products when grown on CO:CO2. Whole-cell FDH activity of C. ragsdalei was enhanced at the optimum concentration of tungstate and selenite, and reduced upon elimination of tungstate and iron, suggesting that FDH of C. ragsdalei may be a tungsten-selenium-iron protein.

At the optimum concentration of Ni2+, an increase in ethanol production by C. ragsdalei was observed that was associated with increased CODH activity. CODH in acetogenic bacteria such as M. thermoacetica occurs as a bifunctional CODH/ACS enzyme where CODH generates CO from CO2, and the ACS combines the CO with CoA and a methyl group to form acetyl-CoA [10]. Both CODH and ACS contain iron-nickel-sulfur metal clusters (CODH: Fe-[NiFe3S4] and ACS: [Fe4S4]-Cys-Gly-Cys-Ni-Cys-Gly-Cys-Ni) at their active sites [10]. Therefore, CODH/ACS and the associated metals (Fe and Ni) play a key role in the metabolism of acetogens.

In addition to Fe2+ and Ni2+, Cu2+ also regulates the activity of ACS in acetogens, where Cu2+ has a negative effect on ACS activity [3, 10, 27]. The metal cluster of ACS contains binuclear metal sites: a proximal metal site (Mp) and a distal metal site (Md), both of which contain Ni2+ under the condition where no Cu2+ is present in the growth medium. However, in the presence of Cu2+, the proximal metal site in the A-cluster can undergo a metal substitution resulting in a binuclear site composition of Cu–Ni and Ni–Ni [10, 27]. The Ni–Ni form of ACS is active whereas Cu-Ni form of enzyme is inactive, which eliminates ACS activity (measured by ability to generate the NiFeC EPR signal) [27]. Although ACS activity in the present study was not measured, an increase in ethanol production was observed upon removing Cu2+ from the growth medium, which could be due to inhibition of ACS activity by Cu2+. Increasing the concentration of Cu2+ had no change on growth and product formation, suggesting Cu2+ concentration in standard trace metals solution (1X) was enough to cause ACS inhibition, probably due to the fact that the cells of acetogenic bacteria can concentrate Cu2+ over 85-fold and Ni2+ at least tenfold from the growth medium [27].

Hydrogenases catalyze the reversible oxidation of molecular hydrogen, and are of two types in bacteria: NiFe and Fe-only H2ase [5]. The NiFe-H2ase is typically involved in oxidation of hydrogen; whereas Fe-only H2ase catalyzes the reduction of protons as terminal electron acceptors to yield hydrogen [5]. Hydrogenase plays a key role in the metabolism of acetogens, most of which can grow autotrophically, as well as heterotrophically [9]. During autotrophic growth on H2 and CO2, H2ase-mediated oxidation of H2 provides reducing equivalents for fixation of CO2 into acetate and cell biomass [9]. In contrast, H2ase in acetogens growing on carbohydrates dispose off the excess reducing equivalents by reducing protons into H2 [1]. In addition, existence of multiple H2ases that account for different roles under different growth conditions have also been reported in acetogens [9]. H2ase of C. pasteurianum, a Fe-only H2ase has been most extensively studied both biochemically and spectroscopically [22]. H2ase purified from fructose grown cells of Acetobacterium woodii also does not contain nickel, and exhibits spectroscopic properties similar to that of Fe-only H2ase of C. pasteurianum [22, 25]. To our knowledge, all purification and spectroscopic studies of H2ase in acetogens have been done from heterotrophically grown acetogens, which has decreased the probability of isolating Fe–Ni hydrogenase, and have ruled out the presence of nickel in the enzyme. However, a genome sequence analysis of M. thermoacetica has revealed a gene cluster homologue of genes that make up an operon required for maturation of the Ni–Fe H2ase [23]. In the present study, H2ase activity was stimulated by increased concentrations of Ni2+, and reduced by the elimination of Fe2+ from the media. Thus, H2ases present in CO:CO2-grown C. ragsdalei may be Fe-only and/or NiFe H2ases. Since, CO:CO2 was used as growth substrate in present study, low H2ase activities obtained were probably due to inhibition of H2ase by CO [25].

In solventogenic clostridia, ADH catalyzes the reduction of acetyl CoA to ethanol [6]. The biochemical and genetic studies on ADH from different clostridia [6, 13] have indicated the role of ADH in solvent production. Clostridial ADHs have been shown to contain zinc [15] and iron [26]. A reduction in ADH activity of C. ragsdalei was observed when iron was removed from the media, suggesting that ADH of C. ragsdalei may be an iron-containing enzyme. Furthermore, supplementing the growth medium of C. ragsdalei with optimized levels of Zn2+ resulted in increased ethanol production and improved cell growth; however, no changes in enzyme activities (CODH, FDH, H2ase, and ADH) were observed upon varying Zn2+ concentration. These results indicate that both types of ADH may be present in C. ragsdalei.

The effects of trace metals on growth, homoacetogenesis, and activities of enzymes of the acetyl-CoA pathway (CODH, FDH, and H2ase) [8, 14] have been mostly studied in heterotrophically grown acetogens. However, the effects of trace metals on product formation under chemolithotrophic growth conditions have not been measured. The activities of key enzymes of Wood-Ljungdahl pathway (CODH, FDH, and H2ase) may vary under heterotrophic and chemolithotrophic growth conditions [7, 18] with higher enzyme activities obtained when cultures were grown on CO:CO2 and/or H2:CO2 than when grown on sugars [7, 18]. In the present study, the effects of trace metals on growth, enzyme activities, and ethanol production by an acetogen (C. ragsdalei) grown on CO:CO2 was studied, which can provide further insights about medium manipulation for increased ethanol production by solventogenic acetogens via syngas fermentation.

Conclusions

Bioethanol production from fermentation of lignocellulosic biomass-derived syngas is a promising alternative for biofuel production. This process offers advantages such as the utilization of whole biomass, including lignin, irrespective of the biomass source and the elimination of the extensive pretreatment steps to obtain fermentable sugars. One of the major limitations of syngas fermentation is the low ethanol yield of biocatalysts. In the present study, ethanol production by C. ragsdalei was improved four-fold by optimizing the trace metal concentrations in the growth medium, emphasizing the importance of medium optimization for improving the ethanol fermentation from syngas. The increase in ethanol production by C. ragsdalei was also substantiated by increased cell growth and metalloenzyme activities of the acetyl-CoA pathway. The presence of Cu2+ in the medium negatively affected the ethanol production by C. ragsdalei. The optimum medium concentrations of Cu2+, Ni2+, Zn2+, SeO4  , and WO4   for ethanol production were 0, 8.5, 35, 7, and 5 μM, respectively. Evaluation of other media components (minerals and vitamins) is warranted for further improvement of the growth and ethanol production by C. ragsdalei from syngas.

Acknowledgments

This research was supported in part by USDA-CSREES Special Grant awards 2005-34447-15711 and 2006-34447-16939. We would like to thank Dr. James A. Zahn for his constructive suggestions in this manuscript.

References

1.

Adams
MWW
,
Mortenson
LE
,
Chen
J-S
Hydrogenase
 
Biochem Biophys Acta
 
1981
 
594
 
105
 
176

2.

Balch
WE
,
Wolfe
RS
New approach to the cultivation of methanogenic bacteria: 2-mercaptoethanesulfonic acid (HS-CoM)-dependent growth of Methanobacterium ruminantium in a pressurized atmosphere
 
Appl Environ Microbiol
 
1976
 
32
 
781
 
791

3.

Bramlett
MR
,
Tan
X
,
Lindahl
PA
Inactivation of acetyl CoA synthase/carbon monoxide dehydrogenase by copper
 
J Am Chem Soc
 
2003
 
125
 
9316
 
9317
 

4.

Burdette
DS
,
Jung
S-H
,
Shen
G-J
,
Hollingsworth
RI
,
Zeikus
JG
Physiological function of alcohol dehydrogenase and long-chain (C30) fatty acids in alcohol tolerance of Thermoanaerobacter ethanolicus
 
Appl Environ Microbiol
 
2002
 
68
 
1914
 
1918
 

5.

Cammack
R
Hydrogenase sophistication
 
Nature
 
1999
 
397
 
214
 
215
 

6.

Chen
JS
Alcohol dehydrogenase: multiplicity and relatedness in the solvent-producing clostridia
 
FEMS Microbiol Rev
 
1995
 
17
 
263
 
273
 

7.

Clark
JE
,
Ragsdale
SW
,
Ljungdahl
LG
,
Wiegel
J
Levels of enzymes involved in the synthesis of acetate from carbon dioxide in Clostridium thermoautotrophicum
 
J Bacteriol
 
1982
 
151
 
507
 
509

8.

Diekert
GB
,
Thauer
RK
The effect of nickel on carbon monoxide dehydrogenase formation in Clostridium thermoaceticum and Clostridium formicoaceticum
 
FEMS Microbiol Lett
 
1980
 
7
 
187
 
189
 

9.

Drake
HL
,
Kusel
K
,
Matthies
C
Dworkin
M
,
Falkow
S
,
Rosenberg
E
,
Schleifer
K-H
,
Stackebrandt
E
Acetogenic prokaryotes
 
The prokaryotes
 
2006
 3  
Berlin Heidelberg New York
 
Springer
 
354
 
420

10.

Drennan
CL
,
Doukov
TI
,
Ragsdale
SW
The metalloclusters of carbon monoxidedehydrogenase/acetyl-CoA synthase: a story in pictures
 
J Biol Inorg Chem
 
2004
 
9
 
511
 
515
 

11.

Hill
J
,
Nelson
E
,
Tilman
D
,
Polasky
S
,
Tiffany
D
Environmental, economic, and energetic costs and benefits of biodiesel and ethanol biofuels
 
Proc Natl Acad Sci
 
2006
 
103
 
11206
 
11210
 

12.

Huhnke R, Lewis R, Tanner RS (2008) Isolation and characterization of novel clostridial species. US patent application. Publication no. US 2008/0057554 A1

13.

Ismaiel
AA
,
Zhu
CX
,
Colby
GD
,
Chen
JS
Purification and characterization of a primary-secondary alcohol dehydrogenase from two strains of Clostridium beijerinckii
 
J Bacteriol
 
1993
 
175
 
5097
 
5105

14.

Koesnandar
NN
,
Nagai
S
Effects of trace metal ions on the growth, homoacetogenesis and corronoid production by Clostridium aceticum
 
J Fermen Bioengg
 
1991
 
71
 
181
 
185
 

15.

Korkhin
Y
,
Kalb (Gilboa)
AJ
,
Peretz
M
,
Bogin
O
,
Burstein
Y
,
Frolow
F
NADP-dependent bacterial alcohol dehydrogenases: crystal structure, cofactor-binding and cofactor specificity of the ADHs of Clostridium beijerinckii and Thermoanaerobacter brockii
 
J Mol Biol
 
1998
 
278
 
967
 
981
 

16.

Liu
C-L
,
Mortenson
LE
Formate dehydrogenase of Clostridium pasteurianum
 
J Bacteriol
 
1984
 
159
 
375
 
380

17.

Margeot
A
,
Hahn-Hagerdal
B
,
Edlund
M
,
Slade
R
,
Monot
F
New improvements for lignocellulosic ethanol
 
Curr Opin Biotechnol
 
2009
 
20
 
372
 
380
 

18.

Mehta MD, Saxena J, Tanner RS (2004) Enzyme activities in clostridia producing ethanol from carbon monoxide. Abstr 104th Annu Meet Am Soc Microbiol, O-81, p 474

19.

Mielenz
JR
Ethanol production from biomass: technology and commercialization status
 
Curr Opin Microbiol
 
2001
 
4
 
324
 
329
 

20.

Peckman KR (1976) Investigation of the phylogenetic relationship of Sporomusa ureae to members of the Bacillaceae using primary structural characterization of 16S ribosomal ribonucleic acids. PhD thesis. University of Illinois, Urbana

21.

Perlack RD, Wright LL, Turhollow AF, Graham RL, Stokes BJ, Erbach DC (2005) Biomass as feedstock for a bioenergy and bioproducts industry: the technical feasibility of a billion-ton annual supply. DOE/GO-102005-2135, Oak Ridge National Laboratory, Oak Ridge. http://:www.osti.gov/bridge

22.

Peters
JW
,
Lanzilotta
WN
,
Lemon
BJ
,
Seefeldt
LC
X-ray crystal structure of the Fe-only hydrogenase (CpI) from Clostridium pasteurianum to 1.8 angstrom resolution
 
Science
 
1998
 
5395
 
1853
 
1858
 

23.

Pierce
E
,
Xie
G
,
Barabote
RD
,
Saunders
E
,
Han
CS
,
Detter
JC
,
Richardson
P
,
Brettin
TS
,
Das
A
,
Ljungdahl
LG
,
Ragsdale
SW
The complete genome sequence of Moorella thermoacetica (f. Clostridium thermoaceticum)
 
Appl Environ Microbiol
 
2008
 
10
 
2550
 
2573

24.

Pimentel
D
Ethanol fuels: energy balance, economics, and environment impacts are negative
 
Nat Resour Res
 
2003
 
12
 
127
 
134
 

25.

Ragsdale
SW
,
Ljungdahl
LG
Hydrogenase from Acetobacterium woodii
 
Arch Microbiol
 
1984
 
139
 
361
 
365
 

26.

Scopes
RK
An iron-activated alcohol dehydrogenase
 
FEBS Lett
 
1983
 
156
 
303
 
306
 

27.

Seravalli
J
,
Xiao
Y
,
Gu
W
,
Cramer
SP
,
Antholine
WE
,
Krymov
V
,
Gerfen
GJ
,
Ragsdale
SW
Evidence that NiNi acetyl-CoA synthase is active and that the CuNi enzyme is not
 
Biochem
 
2004
 
43
 
3944
 
3955
 

28.

Smith
PK
,
Krohn
RI
,
Hermanson
GT
,
Mallia
AK
,
Garter
FH
,
Provenzano
MD
,
Fujimoto
EK
,
Goeke
MN
,
Olson
BJ
,
Klenk
DC
Measurement of protein using bicinchoninic acid
 
Anal Biochem
 
1985
 
150
 
76
 
85
 

29.

Tanner
RS
Hurst
CJ
,
Crawford
RL
,
Mills
AL
,
Garland
JL
,
Stetzenbach
LD
,
Lipson
DA
Cultivation of bacteria and fungi
 
Manual of environmental microbiology
 
2007
 3  
Washington, DC
 
ASM Press
 
69
 
78

30.

Tanner
RS
Wall
J
,
Harwood
CJ
,
Demain
AL
Production of ethanol from synthesis gas
 
Bioenergy
 
2008
 
Washington, DC
 
ASM Press
 
147
 
151

31.

Wagner
R
,
Andreesen
JR
Accumulation and incorporation of 185W-tungsten into proteins of Clostridium acidiurici and Clostridium cylindrosporum
 
Arch Microbiol
 
1987
 
147
 
295
 
299
 

32.

Yamamoto
I
,
Saiki
T
,
Liu
SM
,
Ljungdahl
LG
Purification and properties of NADP-dependent formate dehydrogenase from Clostridium thermoaceticum, a tungsten-selenium-iron protein
 
J Biol Chem
 
1983
 
258
 
1826
 
1832

This article is published and distributed under the terms of the Oxford University Press, Standard Journals Publication Model (https://dbpia.nl.go.kr/journals/pages/open_access/funder_policies/chorus/standard_publication_model)