Acidic Conditions Are Not Obligatory for Onset of Butanol Formation by Clostridium beijerinckii (Synonym, C. butylicum)

Factors that may initiate the metabolic transition for butanol production were investigated in batch cultures of Clostridium beijerinckii (synonym, Clostridium butylicum) VPI 13436. Cultures maintained at pH 6.8 produced nearly as much butanol as those incubated without pH control, indicating that neither a change in the culture pH nor acid conditions per se are always required to initiate solvent formation. Acetate and butyrate levels at the onset of butanol production were dependent on the pH at which the cultures were maintained. Cultures maintained at pH 6.8 could be accelerated into solvent production by artificially lowering the pH to 5.0 or by the addition of acetate plus butyrate without a pH change (but neither acid alone was effective). Solvent production was associated with slower rates of growth and general metabolism, and it did not show a requirement for mature spore formation. We speculate that a slowdown in metabolism, which may be brought about by several conditions, is mechanistically related to the onset of butanol production. Extracts of solvent-producing cells contained acetoacetate decarboxylase activity as well as higher NADP⁺-linked butanol dehydrogenase and lower hydrogenase activities than extracts of acid-producing cells. Solvent production did not appear to involve an enhanced ability to catalyze H₂ oxidation.     

Acetone-butanol-isopropanol production byClostridium beijerinckii (synonym,Clostridium butylicum)

Isopropanol is a product of the organism formerly known as Clostridium butylicum, which is now included in the speciesClostridium beijerinckii. We tested 52 strains ofC.beijerinckii for their ability to produce acetone,n-butanol, and isopropanol. The 32 butanol-producing strains may be divided into two groups based on whether isopropanol was produced. Isopropanol-producing cultures accumulated acetone only transiently.     

丙酮丁醇发酵菌的分子遗传改造

丙酮丁醇梭菌及拜氏梭菌是重要的ABE（丙酮、丁醇和乙醇）工业生产菌株,其发酵产物中的丙酮和丁醇均为重要的化工原料,汽车发动机试验证明丁醇还是一种性能优于乙醇的极具潜力的生物燃料和燃料添加剂。随着新生物技术的不断发展及工业生产的需求,遗传工程改造不断应用于丙酮丁醇生产菌株。在前人研究及工业实践的基础上,对丙酮丁醇生产菌株的遗传特性及其分子遗传改造取得的进展进行了详细概述。     

Acetone and Butanol Production by Clostridium acetobutylicum in a Synthetic Medium

The effect of the component concentrations of a synthetic medium on acetone and butanol fermentation by Clostridium acetobutylicum ATCC 824 was investigated. Cell growth was dependent on the presence of Mg, Fe, and K in the medium. Mg and Mn had deleterious effects when in excess. Ammonium acetate in excess caused acid fermentation. The metabolism was composed of two phases: an acid phase and a solvent one. Low concentrations of glucose allowed the first phase only. The theoretical ratio of the conversion of glucose to solvents, which was 28 to 33%, was obtained with the following medium: MgSO₄, 50 to 200 mg/liter; MnSO₄, 0 to 20 mg/liter; KCl, 0.015 to 8 g/liter (an equivalent concentration of K⁺ was supplied in the form of KH₂PO₄ and K₂HPO₄); FeSO₄, 1 to 50 mg/liter; ammonium acetate, 1.1 to 2.2 g/liter; para-aminobenzoic acid, 1 mg/liter; biotin, 0.01 mg/liter; glucose, 20 to 60 g/liter.     

拜氏梭菌Clostridium beijerinckii NCIMB 8052发酵玉米皮生产丁醇

玉米皮作为玉米淀粉加工的副产物,是一种可用于生产液体燃料的潜在廉价优质的生物质资源。本文以玉米皮为原料,对拜氏梭菌发酵生产丁醇进行了研究。实验结果表明,玉米皮首先在最优的预处理温度140℃下使用0.5%硫酸水溶液以固液比1∶8处理20 min,再添加200 IU/g底物糖化酶、1.0 IU/g底物木聚糖酶进行酶解,可以使原料中的淀粉和半纤维素转化为可发酵糖,此时水解液中的总糖浓度为50.46 g/L。然后使用1.0%的活性炭对水解液进行脱毒处理以去除发酵抑制物,再进行丁醇发酵,丁醇产量为9.72 g/L,总溶剂产量可达14.09 g/L,糖醇转化率为35.1%。上述研究结果证明玉米皮作为一种粮食加工废弃物用于液体燃料丁醇的生产在技术上是完全可行的。     

Production of Acetone and Butanol Using Immobilized Growing-cells of Clostridium acetobutylicum

The biosynthetic route for chloromonilicin, an antifungal substance from cherry rot fungus, was investigated using deuterium-labeled precursors. The incorporation of synthetic deuterium-labeled moniliphenone into chloromonilicin and into its xanthone precursor, 4-chloropinselin, was confirmed by ’H-NMR spectrometry.     

Butanol production by Clostridium beijerinckii ATCC 55025 from wheat bran

Wheat bran, a by-product of the wheat milling industry, consists mainly of hemicellulose, starch and protein. In this study, the hydrolysate of wheat bran pretreated with dilute sulfuric acid was used as a substrate to produce ABE (acetone, butanol and ethanol) using Clostridium beijerinckii ATCC 55025. The wheat bran hydrolysate contained 53.1 g/l total reducing sugars, including 21.3 g/l of glucose, 17.4 g/l of xylose and 10.6 g/l of arabinose. C. beijerinckii ATCC 55025 can utilize hexose and pentose simultaneously in the hydrolysate to produce ABE. After 72 h of fermentation, the total ABE in the system was 11.8 g/l, of which acetone, butanol and ethanol were 2.2, 8.8 and 0.8 g/l, respectively. The fermentation resulted in an ABE yield of 0.32 and productivity of 0.16 g l⁻¹ h⁻¹. This study suggests that wheat bran can be a potential renewable resource for ABE fermentation.     

Expression of Solvent-Forming Enzymes and Onset of Solvent Production in Batch Cultures of Clostridium beijerinckii ("Clostridium butylicum")

Clostridium beijerinckii ("Clostridium butylicum") NRRL B592 and NRRL B593 were grown in batch cultures without pH control. The use of more sensitive and accurate procedures for the determination of solvents in cultures led to the recognition of the onset of solvent production about 2 h earlier than the previously assigned point and at a higher culture pH for both strains. Reliable assays for solvent-forming enzyme activities in cell extracts have also been developed. The results showed that activities of solvent-forming enzymes in strain NRRL B592 started to increase about 1 h before the measured onset of solvent production and that the increase in activities of solvent-forming enzymes was not simultaneous. The degree of increase of these enzyme activities for both strains ranged from 2- to 165-fold, with acetoacetate decarboxylase and butanol-isopropanol dehydrogenase showing the largest activity increases. However, the pattern of increase of enzyme activities differed significantly in the two strains of C. beijerinckii. When an increase in solvent-forming enzyme activities was first detected in strain NRRL B592, the culture pH was at 5.7 and the concentrations of total acetic and butyric acids were 5.2 and 3.6 mM, respectively. For strain NRRL B593, the corresponding pH was 5.5. Thus, the culture conditions immediately preceding the expression of solvent-forming enzyme activities differed significantly from those that have been correlated with the production of solvents at later stages of growth.     

Butanol-Ethanol Dehydrogenase and Butanol-Ethanol-Isopropanol Dehydrogenase: Different Alcohol Dehydrogenases in Two Strains of Clostridium beijerinckii (Clostridium butylicum)

Alcohol-producing strains of Clostridium beijerinckii (Clostridium butylicum) produce, besides acetone, either n-butanol and ethanol or n-butanol, ethanol, and isopropanol as their characteristic products. Alcohol dehydrogenase has been isolated from a strain (NRRL B593) of C. beijerinckii producing isopropanol and from a strain (NRRL B592) not producing isopropanol. Butanol-ethanol dehydrogenase activities were present in both strains, but isopropanol dehydrogenase activity was present only in the isopropanol-producing strain. The butanol-ethanol dehydrogenase of strain NRRL B592 had M(r) 66,000 and a K(m) of 6 muM for butyraldehyde. In contrast, the butanol-ethanol-isopropanol dehydrogenase of strain NRRL B593 had a M(r) 100,000 and K(m)s of 9.5 and 1.0 mM for butyraldehyde and acetone, respectively. In a purification by four different types of separatory methods (DEAE-cellulose, hydroxyapatite, Sephacryl S-300, and Matrex Gel Red A), butanol-ethanol-isopropanol dehydrogenase activities of strain NRRL B593 were purified up to 200-fold (10 to 30% yield), and these activities were not separated. Gel electrophoresis followed by activity stain also revealed distinct mobilities for the butanol-ethanol dehydrogenase of strain NRRL B592 and the butanol-ethanol-isopropanol dehydrogenase of strain NRRL B593. In cell extracts from both strains, a higher alcohol dehydrogenase activity was measured with NADP(H) than with NAD(H). The 150- to 200-fold-purified alcohol dehydrogenase from strain NRRL B593 did not show any NAD(H)-linked activities. The K(m) for NADPH was 31 muM (with butyraldehyde as cosubstrate) and 18 muM (with acetone as cosubstrate) for the alcohol dehydrogenase of strain NRRL B593. This study showed that the alcohol dehydrogenases from two strains of C. beijerinckii differed significantly.     

Purification and properties of 3-hydroxybutyryl-coenzyme A dehydrogenase from Clostridium beijerinckii ("Clostridium butylicum") NRRL B593.

The enzyme 3-hydroxybutyryl-coenzyme A (CoA) dehydrogenase has been purified 45-fold to apparent homogeneity from the solvent-producing anaerobe Clostridium beijerinckii NRRL B593. The identities of 34 of the N-terminal 35 amino acid residues have been determined. The enzyme exhibited a native M(r) of 213,000 and a subunit M(r) of 30,800. It is specific for the (S)-enantiomer of 3-hydroxybutyryl-CoA. Michaelis constants for NADH and acetoacetyl-CoA were 8.6 and 14 microM, respectively. The maximum velocity of the enzyme was 540 mumol min-1 mg-1 for the reduction of acetoacetyl-CoA with NADH. The enzyme could use either NAD(H) or NADP(H) as a cosubstrate; however, kcat/Km for the NADH-linked reaction was much higher than the apparent value for the NADPH-linked reaction. Also, NAD(H)-linked activity was less sensitive to changes in pH than NADP(H)-linked activity was. In the presence of 9.5 microM NADH, the enzyme was inhibited by acetoacetyl-CoA at concentrations as low as 20 microM, but the inhibition was relieved as the concentration of NADH was increased, suggesting a possible mechanism for modulating the energy efficiency during growth.     

Butanol production by Clostridium beijerinckii. Part I: use of acid and enzyme hydrolyzed corn fiber

Fermentation of sulfuric acid treated corn fiber hydrolysate (SACFH) inhibited cell growth and butanol production (1.7 ± 0.2 g/L acetone butanol ethanol or ABE) by Clostridium beijerinckii BA101. Treatment of SACFH with XAD-4 resin removed some of the inhibitors resulting in the production of 9.3 ± 0.5 g/L ABE and a yield of 0.39 ± 0.015. Fermentation of enzyme treated corn fiber hydrolysate (ETCFH) did not reveal any cell inhibition and resulted in the production of 8.6 ± 1.0 g/L ABE and used 24.6 g/L total sugars. ABE production from fermentation of 25 g/L glucose and 25 g/L xylose was 9.9 ± 0.4 and 9.6 ± 0.4 g/L, respectively, suggesting that the culture was able to utilize xylose as efficiently as glucose. Production of only 9.3 ± 0.5 g/L ABE (compared with 17.7 g/L ABE from fermentation of 55 g/L glucose-control) from the XAD-4 treated SACFH suggested that some fermentation inhibitors may still be present following treatment. It is suggested that inhibitory components be completely removed from the SACFH prior to fermentation with C. beijerinckii BA101. In our fermentations, an ABE yield ranging from 0.35 to 0.39 was obtained, which is higher than reported by the other investigators.     

拜氏梭菌13-2发酵甘蔗渣水解液生产丁醇的研究

目的:蔗渣是一种重要的可再生生物质资源,蔗渣原料生产丁醇将大大降低丁醇的成本.方法:实验利用0.25 ～3.0%不同浓度稀H2SO4对蔗渣进行121℃的高温作用1h,以水解液为碳源,进行丁醇的发酵实验.结果:相对于8052菌株,13 -2菌株对甘蔗渣水解液具有更高的发酵效率,在0.5%硫酸用量条件下,13 -2菌株的丁醇发酵量最高,达到4.5g/L.而8052只有2.3g/L的丁醇发酵量.结论:在同等条件下,拜氏梭菌菌株13 -2比模式菌株8052具有更高的溶剂产量和抑制物耐受能力,最佳的蔗渣水解条件为1.5%硫酸用量,丁醇发酵量和总溶剂分别为4.57g/L和5.41 g/L.     

Enhanced Butanol Production by Clostridium beijerinckii BA101 Grown in Semidefined P2 Medium Containing 6 Percent Maltodextrin or Glucose

Dramatically elevated levels of butanol and acetone resulted in higher butanol and total solvent yields for hyperamylolytic Clostridium beijerinckii BA101 relative to the NCIMB 8052 parent strain grown in semidefined P2 medium containing either 6% glucose or STAR-DRI 5 maltodextrin. C. beijerinckii BA101 consistently produced on the order of 19 g of butanol per liter in 20-liter batch fermentations. This represents a greater than 100% increase in butanol concentration by the BA101 strain compared to the parent NCIMB 8052 strain. The kinetics of butanol production over time also indicate a more rapid rate of butanol production by BA101 in semidefined P2 medium containing glucose or maltodextrin. The lower levels of butyric and acetic acids produced over the course of the fermentation carried out by BA101 are consistent with an enhanced capacity for uptake and recycling of these acids. C. beijerinckii BA101 appears to more completely utilize carbohydrate compared to the 8052 strain. Carbon balance following fermentation by C. beijerinckii 8052 and BA101 indicates that sufficient carbon is available for the twofold increase in butanol concentration observed during BA101 fermentations. C. beijerinckii BA101 also has superior solvent production capacity during continuous culture fermentation in P2 medium containing 6% glucose. Volumetric solvent yields of 0.78 and 1.74 g/liter/h for BA101 and 0.34 and 1.17 g/liter/h for NCIMB 8052 were obtained at dilution rates of 0.05 and 0.20 h(sup-1), respectively. No drift towards acid synthesis (strain degeneration) was observed for up to 200 h (d = 0.05 h(sup-1)) and 100 h (d = 0.20 h(sup-1)).     

Purification and properties of an acetoacetyl coenzyme A-reacting phosphotransbutyrylase from Clostridium beijerinckii ("Clostridium butylicum") NRRL B593

During the study of acetoacetyl coenzyme A (CoA)-reacting enzymes of Clostridium beijerinckii NRRL B593, a phosphate-dependent acetoacetyl-CoA-utilizing activity was detected in protein fractions devoid of thiolase and phosphotransacetylase. Further purification of this acetoacetyl-CoA-utilizing activity yielded an enzyme which may be designated as phosphotransbutyrylase (PTB; phosphate butyryltransferase [EC 2.3.1.19]). PTB from C. beijerinckii NRRL B593 was purified 160-fold with a yield of 14% and, with the best fractions, purified 190-fold to near homogeneity. It showed a native Mr of 205,000 and a subunit Mr of 33,000. PTB activity was sensitive to pH changes within the physiological range of 6 to 8. PTB exhibited a broad substrate specificity. The Km values at pH 7.5 for butyryl-CoA, acetoacetyl-CoA, and acetyl-CoA were 0.04, 1.10, and 3.33 mM, respectively. The Vmax values with butyryl-CoA and acetoacetyl-CoA were comparable, but the Vmax/Km was higher for butyryl-CoA than for acetoacetyl-CoA. An apparent Km of 6.5 mM for phosphate was obtained with butyryl-CoA as the cosubstrate, whereas it was 12.9 mM with acetoacetyl-CoA as the cosubstrate. It remains to be established whether the putative compound acetoacetyl phosphate is produced in the PTB-catalyzed reaction with acetoacetyl-CoA.     

Butanol production by hypersolvent-producing mutant Clostridium beijerinckii BA101 in corn steep water medium containing maltodextrin

Clostridium beijerinckii NCIMB 8052 parent strain and BA101, a hypersolvent-producing mutant, fermented 6% (w/v) glucose, maltodextrin, maltose or xylose in a medium containing corn steep water (CSW) to produce butanol. Batch fermentation in an unoptimized 6% (w/v) maltodextrin plus 1.6% solids CSW medium demonstrated that C. beijerinckii NCIMB 8052 and BA101 produced 10.7 g butanol/L and 14.5 g butanol/L, respectively.     

Butanol production by Clostridium beijerinckii BA101 using cassava flour as fermentation substrate: enzymatic versus chemical pretreatments

Cassava flour (CF), a cost-effective source of starch, was employed as a substrate for successful acetone-butanol-ethanol (ABE) production by batch-fermentation with Clostridium beijerinckii. The effect of temperature, initial concentration of CF and chemical/enzymatic hydrolysis were studied in a 2³ factorial design. Results revealed that temperature and initial concentration of substrate exert a significant effect on ABE production, as well as interactions of temperature with the other variables. Solvent production was maximized when working at 40°C, 60 g l⁻¹ CF and enzymatic pretreatment. An average of 31.38 g l⁻¹ ABE was produced after 96 h, with a productivity of 0.33 g l⁻¹ h⁻¹. A posterior randomized block design (3 × 2) showed that enzymatic hydrolysis (with saccharification periods of 6 h at 60°C) enhances both reducing sugar and solvent production if compared to chemical pretreatments. Average ABE production in this case was 27.28 g l⁻¹, with a productivity of 0.28 g l⁻¹ h⁻¹. Results suggest that CF may be a suitable substrate for industrial ABE production.