Ethanol and acetate synthesis from waste gas using batch culture of Clostridium ljungdahlii

Single inorganic carbon source was used for production of chemicals and fuels via fermentation processes. Clostridium ljungdahlii, a strictly anaerobic autotrophic bacterium, was grown on synthesis gas to produce acetate and ethanol from gaseous substrates. C. ljungdahlii was grown on a various concentrations of carbon monoxide with synthesis gas total pressures of 0.8–1.8 atm with an interval of 0.2 atm. The cell and product yields were 0.015 g cell/g CO and 0.41 g acetate/g CO, respectively. Formation of acetate was steady and the production trend was about the same for all of the gases initial pressure and at constant cell density. The ethanol concentration was enhanced by the initial presence of hydrogen and carbon dioxide in the liquid phase. There was no substrate inhibition while C. ljungdahlii was grown in the batch fermentation, even at high system pressure of 1.6 and 1.8 atm. A desired product molar ratio of ethanol:acetate (5:1) was achieved with total gas pressure of 1.6 and 1.8 atm.     

Enhanced acetone/butanol/ethanol production by Clostridium beijerinckii IB4 using pH control strategy

PH is an essential factor for acetone/butanol/ethanol (ABE) production using Clostridium spp. In this study, batch fermentations by Clostridium beijerinckii IB4 at various pH values ranging from 4.9 to 6.0 were examined. At pH 5.5, the ABE production was dominant and maximum ABE concentration of 24.6 g/L (15.7 g/L of butanol, 8.63 g/L of acetone and 0.32 g/L of ethanol) was obtained with the consumption of 60 g/L of glucose within 36 h. However, in the control (without pH control), an ABE concentration of 14.1 g/L (11.0 g/L of butanol, 3.01 g/L of acetone and 0.16 g/L of ethanol) was achieved with the consumption of 41 g/L of glucose within 40 h. A considerable improvement in the productivity of up to 93.8% was recorded at controlled pH in comparison to the process without pH control. To better understand the influence of pH on butanol production, the reducing power capability and NADH-dependent butanol dehydrogenase activity were investigated, both of which were significantly improved at pH 5.5. Thus, the pH control technique is a convenient and efficient method for high-intensity ABE production.     

Process engineering of cellulosic n-butanol production from corn-based biomass using Clostridium cellulovorans

The cellulolytic Clostridium cellulovorans has been engineered to produce n-butanol from low-value lignocellulosic biomass by consolidated bioprocessing (CBP). The objective of this study was to establish a robust cellulosic biobutanol production process using a metabolically engineered C. cellulovorans. First, various methods for the pretreatment of four different corn-based residues, including corn cob, corn husk, corn fiber, and corn bran, were investigated. The results showed that better cell growth and a higher concentration of n-butanol were produced from corn cob that was pretreated with sodium hydroxide. Second, the effects of different carbon sources (glucose, cellulose and corn cob), basal media and culture pH values on butanol production were evaluated in the fermentations performed in 2-L bioreactors to identify the optimal CBP conditions. Finally, the engineered C. cellulovorans produced butanol with final concentration >3 g/L, yield >0.14 g/g, and selectivity >3 g/g from pretreated corn cob at pH 6.5 in CBP. This study showed that the fermentation process engineering of C. cellulovorans enabled a high butanol production directly from agricultural residues.     

Ethanol and acetate production by <Emphasis Type="Italic">Clostridium ljungdahlii</Emphasis> and <Emphasis Type="Italic">Clostridium autoethanogenum</Emphasis> using resting cells

Combined gasification and fermentation technologies can potentially produce biofuels from renewable biomass. Gasification generates synthesis gas consisting primarily of CO, CO₂, H₂, N₂, with smaller amounts of CH₄, NO_x, O₂, C₂ compounds, ash and tars. Several anaerobic bacteria species can ferment bottled mixtures of pure synthesis gas constituents. However, there are challenges to maintaining culture viability of synthesis gas exposed cells. This study was designed to enhance culture stability and improve ethanol-to-acetate ratios using resting (non-growing) cells in synthesis gas fermentation. Resting cell states were induced in autotrophic Clostridium ljungdahlii cultures with minimal ethanol and acetate production due to low metabolic activity compared to growing cell production levels of 5.2 and 40.1 mM of ethanol and acetate. Clostridium autoethanogenum cultures were not induced into true resting states but did show improvement in total ethanol production (from 5.1 mM in growing cultures to 9.4 in one nitrogen-limited medium) as well as increased shifts in ethanol-to-acetate production ratios.     

Metabolic engineering of Clostridium tyrobutyricum for enhanced butyric acid production from glucose and xylose

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8 g/L vs. 19.4 g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28 g/L·h vs. 0.16 g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53 g/L·h vs. 0.26 g/L·h) and yield (0.32 g/g vs. 0.28 g/g). When the initial total sugar concentration was ~120 g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4 g/L, yield of 0.43 g/g sugar consumed, productivity of 0.87 g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass.     

Clostridium difficile survives minimal temperature recommended for cooking ground meats

We quantified the thermal inhibitory effect of 71 °C (recommended for cooking ground meats), and re-heating at 85 °C, on food- and food-animal-derived Clostridium difficile spores. All C. difficile strains tested (n = 20) survived 71 °C for 2 h, but 90% died within 10 min when re-heated at 85 °C. Current cooking recommendations would need revision to include C. difficile.     

Acetone production with metabolically engineered strains of Acetobacterium woodii

Expected depletion of oil and fossil resources urges the development of new alternative routes for the production of bulk chemicals and fuels beyond petroleum resources. In this study, the clostridial acetone pathway was used for the formation of acetone in the acetogenic bacterium Acetobacterium woodii. The acetone production operon (APO) containing the genes thlA (encoding thiolase A), ctfA/ctfB (encoding CoA transferase), and adc (encoding acetoacetate decarboxylase) from Clostridium acetobutylicum were cloned under the control of the thlA promoter into four vectors having different replicons for Gram-positives (pIP404, pBP1, pCB102, and pCD6). Stable replication was observed for all constructs. A. woodii [pJIR_act_thlA] achieved the maximal acetone concentration under autotrophic conditions (15.2±3.4 mM). Promoter sequences of the genes ackA from A. woodii and pta-ack from C. ljungdahlii were determined by primer extension (PEX) and cloned upstream of the APO. The highest acetone production in recombinant A. woodii cells was achieved using the promoters P_thlA and P_pta-ack. Batch fermentations using A. woodii [pMTL84151_act_thlA] in a bioreactor revealed that acetate concentration had an effect on the acetone production, due to the high K_m value of the CoA transferase. In order to establish consistent acetate concentration within the bioreactor and to increase biomass, a continuous fermentation process for A. woodii was developed. Thus, acetone productivity of the strain A. woodii [pMTL84151_act_thlA] was increased from 1.2 mg L⁻¹ h⁻¹ in bottle fermentation to 26.4 mg L⁻¹ h⁻¹ in continuous gas fermentation.     

Heterologous expression and characterisation of a biosynthetic thiolase from Clostridium butyricum DSM 10702

Biosynthetic thiolases (EC 2.3.1.9) are key enzymes in the branched catabolism of diverse clostridia as their activity and regulation influence the production of organic acids and solvents. In Clostridium butyricum, they are also involved in the production of hydrogen as a sustainable and environmentally benign energy source. In this study, the gene coding for thiolase from C. butyricum DSM 10702 was cloned by genome walking. It was found to consist of 1179 bp coding for a protein with 393 amino acids and a deduced molecular weight of 41.4 kDa. The enzyme was fused to an N-terminal his-tag, expressed in Escherichia coli, purified to near homogeneity and characterised for biochemical and kinetic properties. Gel filtration chromatography revealed that the catalytically active enzyme consists of a homotetramer. The enzyme showed a K_M of ～32 μM towards acetoacetyl-CoA and of ～21 μM towards CoASH at 30 °C and pH 8.0. Claisen condensation of acetyl-CoA by thiolase was analysed in a coupled enzyme assay, where β-hydroxybutyryl-CoA dehydrogenase was applied catalysing the subsequent NADH-dependant reduction of the formed condensation product acetoacetyl-CoA. For this purpose the latter enzyme was cloned from C. butyricum DSM 10702 and recombinantly expressed in E. coli. The K_M of thiolase towards acetyl-CoA was ～674 μM at 30 °C and pH 7.5. Acetyl-CoA condensation was inhibited even at micromolar concentrations of CoASH indicating that CoASH has an important regulatory function in vivo.     

Engineering Clostridium acetobutylicum for production of kerosene and diesel blendstock precursors

Processes for the biotechnological production of kerosene and diesel blendstocks are often economically unattractive due to low yields and product titers. Recently, Clostridium acetobutylicum fermentation products acetone, butanol, and ethanol (ABE) were shown to serve as precursors for catalytic upgrading to higher chain-length molecules that can be used as fuel substitutes. To produce suitable kerosene and diesel blendstocks, the butanol:acetone ratio of fermentation products needs to be increased to 2–2.5:1, while ethanol production is minimized. Here we show that the overexpression of selected proteins changes the ratio of ABE products relative to the wild type ATCC 824 strain. Overexpression of the native alcohol/aldehyde dehydrogenase (AAD) has been reported to primarily increase ethanol formation in C. acetobutylicum. We found that overexpression of the AAD^D485G variant increased ethanol titers by 294%. Catalytic upgrading of the 824(aad^D485G) ABE products resulted in a blend with nearly 50 wt%≤C₉ products, which are unsuitable for diesel. To selectively increase butanol production, C. beijerinckii aldehyde dehydrogenase and C. ljungdhalii butanol dehydrogenase were co-expressed (strain designate 824(Cb ald-Cl bdh)), which increased butanol titers by 27% to 16.9 g L⁻¹ while acetone and ethanol titers remained essentially unaffected. The solvent ratio from 824(Cb ald-Cl bdh) resulted in more than 80 wt% of catalysis products having a carbon chain length≥C₁₁ which amounts to 9.8 g L⁻¹ of products suitable as kerosene or diesel blendstock based on fermentation volume. To further increase solvent production, we investigated expression of both native and heterologous chaperones in C. acetobutylicum. Expression of a heat shock protein (HSP33) from Bacillus psychrosaccharolyticus increased the total solvent titer by 22%. Co-expression of HSP33 and aldehyde/butanol dehydrogenases further increased ABE formation as well as acetone and butanol yields. HSP33 was identified as the first heterologous chaperone that significantly increases solvent titers above wild type C. acetobutylicum levels, which can be combined with metabolic engineering to further increase solvent production.     

Overflow metabolism at the thermodynamic limit of life: How carboxydotrophic acetogens mitigate carbon monoxide toxicity

Carboxydotrophic metabolism is gaining interest due to its applications in gas fermentation technology, enabling the conversion of carbon monoxide to fuels and commodities. Acetogenic carboxydotrophs play a central role in current gas fermentation processes. In contrast to other energy-rich microbial substrates, CO is highly toxic, which makes it a challenging substrate to utilize. Instantaneous scavenging of CO upon entering the cell is required to mitigate its toxicity. Experiments conducted with Clostridium autoethanogenum at different biomass-specific growth rates show that elevated ethanol production occurs at increasing growth rates. The increased allocation of electrons towards ethanol at higher growth rates strongly suggests that C. autoethanogenum employs a form of overflow metabolism to cope with high dissolved CO concentrations. We argue that this overflow branch enables acetogens to efficiently use CO at highly variable substrate influxes by increasing the conversion rate almost instantaneously when required to remove toxic substrate and promote growth. In this perspective, we will address the case study of C. autoethanogenum grown solely on CO and syngas mixtures to assess how it employs acetate reduction to ethanol as a form of overflow metabolism.     

Metabolic engineering of Clostridium acetobutylicum for butyric acid production with high butyric acid selectivity

A typical characteristic of the butyric acid-producing Clostridium is coproduction of both butyric and acetic acids. Increasing the butyric acid selectivity important for economical butyric acid production has been rather difficult in clostridia due to their complex metabolic pathways. In this work, Clostridium acetobutylicum was metabolically engineered for highly selective butyric acid production. For this purpose, the second butyrate kinase of C. acetobutylicum encoded by the bukII gene instead of butyrate kinase I encoded by the buk gene was employed. Furthermore, metabolic pathways were engineered to further enhance the NADH-driving force. Batch fermentation of the metabolically engineered C. acetobutylicum strain HCBEKW (pta⁻, buk⁻, ctfB⁻ and adhE1⁻) at pH 6.0 resulted in the production of 32.5 g/L of butyric acid with a butyric-to-acetic acid ratio (BA/AA ratio) of 31.3 g/g from 83.3 g/L of glucose. By further knocking out the hydA gene (encoding hydrogenase) in the HCBEKW strain, the butyric acid titer was not further improved in batch fermentation. However, the BA/AA ratio (28.5 g/g) obtained with the HYCBEKW strain (pta⁻, buk⁻, ctfB⁻, adhE1⁻ and hydA⁻) was 1.6 times higher than that (18.2 g/g) obtained with the HCBEKW strain at pH 5.0, while no improvement was observed at pH 6.0. These results suggested that the buk gene knockout was essential to get a high butyric acid selectivity to acetic acid in C. acetobutylicum.     

Fumaric acid fermentation with immobilised Rhizopus oryzae: Quantifying time-dependent variations in catabolic flux

A novel fermenter system utilising immobilised Rhizopus oryzae is presented. The impact of dissolved oxygen (20%, 60% and 80%) and pH (4 and 5) was investigated. All fermentations exhibited three distinct phases. Phase A, at the start, was associated with no fumarate production, minimal respiration and ethanol as the major product. Phase B was characterised by the onset of fumarate production and significant ethanol and respiration fluxes. Phase C was associated with zero ethanol flux. Inhibition of fumarate production was more severe at low pH. The DO 20% fermentation (pH 5) had a low respiration flux which resulted in excessive ethanol production. Higher DO levels resulted in less inhibition of fumarate production during phase C. Instantaneous fumarate yields on glucose were at a maximum at the start of phase C, with values in excess of 0.75 g g⁻¹ achieved for the DO 60% and 80% fermentations.     

Lactose-Inducible System for Metabolic Engineering of Clostridium ljungdahlii

The development of tools for genetic manipulation of Clostridium ljungdahlii has increased its attractiveness as a chassis for autotrophic production of organic commodities and biofuels from syngas and microbial electrosynthesis and established it as a model organism for the study of the basic physiology of acetogenesis. In an attempt to expand the genetic toolbox for C. ljungdahlii, the possibility of adapting a lactose-inducible system for gene expression, previously reported for Clostridium perfringens, was investigated. The plasmid pAH2, originally developed for C. perfringens with a gusA reporter gene, functioned as an effective lactose-inducible system in C. ljungdahlii. Lactose induction of C. ljungdahlii containing pB1, in which the gene for the aldehyde/alcohol dehydrogenase AdhE1 was downstream of the lactose-inducible promoter, increased expression of adhE1 30-fold over the wild-type level, increasing ethanol production 1.5-fold, with a corresponding decrease in acetate production. Lactose-inducible expression of adhE1 in a strain in which adhE1 and the adhE1 homolog adhE2 had been deleted from the chromosome restored ethanol production to levels comparable to those in the wild-type strain. Inducing expression of adhE2 similarly failed to restore ethanol production, suggesting that adhE1 is the homolog responsible for ethanol production. Lactose-inducible expression of the four heterologous genes necessary to convert acetyl coenzyme A (acetyl-CoA) to acetone diverted ca. 60% of carbon flow to acetone production during growth on fructose, and 25% of carbon flow went to acetone when carbon monoxide was the electron donor. These studies demonstrate that the lactose-inducible system described here will be useful for redirecting carbon and electron flow for the biosynthesis of products more valuable than acetate. Furthermore, this tool should aid in optimizing microbial electrosynthesis and for basic studies on the physiology of acetogenesis.     

Enhanced solvent production by metabolic engineering of a twin-clostridial consortium

The efficient fermentative production of solvents (acetone, n-butanol, and ethanol) from a lignocellulosic feedstock using a single process microorganism has yet to be demonstrated. Herein, we developed a consolidated bioprocessing (CBP) based on a twin-clostridial consortium composed of Clostridium cellulovorans and Clostridium beijerinckii capable of producing cellulosic butanol from alkali-extracted, deshelled corn cobs (AECC). To accomplish this a genetic system was developed for C. cellulovorans and used to knock out the genes encoding acetate kinase (Clocel_1892) and lactate dehydrogenase (Clocel_1533), and to overexpress the gene encoding butyrate kinase (Clocel_3674), thereby pulling carbon flux towards butyrate production. In parallel, to enhance ethanol production, the expression of a putative hydrogenase gene (Clocel_2243) was down-regulated using CRISPR interference (CRISPRi). Simultaneously, genes involved in organic acids reassimilation (ctfAB, cbei_3833/3834) and pentose utilization (xylR, cbei_2385 and xylT, cbei_0109) were engineered in C. beijerinckii to enhance solvent production. The engineered twin-clostridia consortium was shown to decompose 83.2 g/L of AECC and produce 22.1 g/L of solvents (4.25 g/L acetone, 11.5 g/L butanol and 6.37 g/L ethanol). This titer of acetone-butanol-ethanol (ABE) approximates to that achieved from a starchy feedstock. The developed twin-clostridial consortium serves as a promising platform for ABE fermentation from lignocellulose by CBP.     

Molecular characterization and molasses fermentation performance of a wild yeast strain operating in an extremely wide temperature range

Molasses fermentation performance by both a cryotolerant and a thermophilic yeast (strain AXAZ-1) isolated from grapes in Greece was evaluated in an extremely wide temperature range (3–40 °C). Sequence analysis of the 5.8S internal transcribed spacer and the D1/D2 ribosomal DNA (rDNA) regions assigned isolate to Saccharomyces cerevisiae. Restriction fragment length polymorphism of the mitochondrial DNA showed that strain AXAZ-1 is genetically divergent compared to other wild strains of Greek origin or commercial yeast starters. Yeast cells growing planktonically were capable of fermentation in a wide temperature spectrum, ranging from 3 °C to 38 °C. Immobilization of yeast on brewer’s spent grains (BSG) improved the thermo-tolerance of the strain and enabled fermentation at 40 °C. Time to complete fermentation with the immobilized yeast ranged from 20 days at 3 to 38 h at 40 °C. The daily ethanol productivity reached maximum (58.1 g/L) and minimum (2.5 g/L) levels at 30 and 3 °C, respectively. The aroma-related compounds’ profiles of immobilized cells at different fermentation temperatures were evaluated by using solid phase microextraction (SPME) gas chromatography–mass spectrometry (GC–MS). Molasses fermentation resulted in a high quality fermentation product due to the low concentrations of higher and amyl alcohols at all temperatures tested. Strain AXAZ-1 is very promising for the production of ethanol from low cost raw materials, as it was capable to perform fermentations of high ethanol concentration and productivities in both low and high temperatures.     

Estudios de la viabilidad y la vitalidad frente al congelado de la levadura probiótica Saccharomyces boulardii: efecto del preacondicionamiento fisiológico

The aim of this study was to evaluate the vitality and viability of the probiotic yeast Saccharomyces boulardii after freezing/thawing and the physiological preconditioning effect on these properties. The results indicate that the specific growth rate (0.3/h^?1) and biomass (2-3 × 10⁸ cells/ml) of S. boulardii obtained in flasks shaken at 28 °C and at 37 °C were similar. Batch cultures of the yeast in bioreactors using glucose or sugar-cane molasses as carbon sources, reached yields of 0.28 g biomass/g sugar consumed, after 10 h incubation at 28 °C; the same results were obtained in fed batch fermentations. On the other hand, in batch cultures, the vitality of cells recovered during the exponential growth phase was greater than the vitality of cells from the stationary phase of growth. Vitality of cells from fed-batch fermentations was similar to that of stationary growing cells from batch fermentations. Survival to freezing at –20 °C and subsequent thawing of cells from batch cultures was 0.31% for cells in exponential phase of growth and 11.5% for cells in stationary phase. Pre-treatment of this yeast in media with water activity (a_w) 0.98 increased the survival to freezing of S. boulardii cells stored at –20 °C for 2 months by 10 fold. Exposure of the yeast to media of reduced a_w and/or freezing/thawing process negatively affected cell vitality. It was concluded that stress conditions studied herein decrease vitality of S. boulardii. Besides, the yeast strain studied presented good tolerance to bile salts even at low pH values.     

Stability of phycocyanin extracted from Spirulina sp.: Influence of temperature,pH and preservatives

Temperature and pH play an important role in the stability of phycocyanin, a natural blue colorant. Systematic investigations showed the maximum stability of phycocyanin was in the pH range 5.5–6.0. Incubation at temperatures between 47 and 64 °C caused the concentration (C_R) and half-life of phycocyanin in solution to decrease rapidly. The C_R value remained at approximately 50% after incubating for 30 min at 59 °C. After heating at 60 °C for 15 min, the C_R value of phycocyanin at pH 7.0 was maintained at around 62–70% when 20–40% glucose or sucrose was added, and the half-life increased from 19 min to 30–44 min. 2.5% sodium chloride was found to be an effective preservative for phycocyanin at pH 7.0 as a C_R value of 76% was maintained and the half-life of 67 min was increased.     

α-Amylase from germinating soybean (Glycine max) seeds – Purification,characterization and sequential similarity of conserved and catalytic amino acid residues

Starch hydrolyzing amylase from germinated soybeans seeds (Glycine max) has been purified 400-fold to electrophoretic homogeneity with a final specific activity of 384 units/mg. SDS–PAGE of the final preparation revealed a single protein band of 100 kDa, whereas molecular mass was determined to be 84 kDa by MALDI–TOF and gel filtration on Superdex-200 (FPLC). The enzyme exhibited maximum activity at pH 5.5 and a pI value of 4.85. The energy of activation was determined to be 6.09 kcal/mol in the temperature range 25–85 °C. Apparent Michaelis constant (K_m(app)) for starch was 0.71 mg/mL and turnover number (k_cat) was 280 s^?1 in 50 mM sodium acetate buffer, pH 5.5. Thermal inactivation studies at 85 °C showed first-order kinetics with rate constant (k) equal to 0.0063 min^?1. Soybean α-amylase showed high specificity for its primary substrate starch. High similarity of soybean α-amylase with known amylases suggests that this α-amylase belongs to glycosyl hydrolase family 13. Cereal α-amylases have gained importance due to their compatibility for biotechnological applications. Wide availability and easy purification protocol make soybean as an attractive alternative for plant α-amylase. Soybean can be used as commercially viable source of α-amylase for various industrial applications.     

Cyanide hydratase from Aspergillus niger K10: Overproduction in Escherichia coli,purification, characterization and use in continuous cyanide degradation

A cyanide hydratase from Aspergillus niger K10 was expressed in Escherichia coli and purified. Apart from HCN, it transformed some nitriles, preferentially 2-cyanopyridine and fumaronitrile. V_max and K_m for HCN were ca. 6.8 mmol min⁻¹ mg⁻¹ protein and 109 mM, respectively. V_max for fumaronitrile and 2-cyanopyridine was two to three orders of magnitude lower than for HCN (ca. 18.8 and 10.3 μmol min⁻¹ mg⁻¹, respectively) but K_m was also lower (ca. 14.7 and 3.7 mM, respectively). Both cyanide hydratase and nitrilase activities were abolished in truncated enzyme variants missing 18–34 C-terminal aa residues. The enzyme exhibited the highest activity at 45 °C and pH 8–9; it was unstable at over 35 °C and at below pH 5.5. The operational stability of the whole-cell catalyst was examined in continuous stirred membrane reactors with 70-mL working volume. The catalyst exhibited a half-life of 5.6 h at 28 °C. A reactor loaded with an excess of the catalyst was used to degrade 25 mM KCN. A conversion rate of over 80% was maintained for 3 days.