Ethanol production from sulphuric acid wood hydrolysate ofPinus radiata using free and immobilized cells ofPichia stipitis

Summary Ethanol was produced by a strain ofPichia stipitis adapted to an inhibitory acid wood hydrolysate ofPinus radiata. The best ethanol productivity for batch cultures was 0.21 g/l h at 0.7% ethanol. Varying culture conditions increased ethanol concentration to 0.76%, however the productivity decreased to 0.18 g/l h. A decrease in ethanol concentration in the culture fluid was noted late in the batch which suggested ethanol catabolism. Values of kinetic parameters (K _m,K _s, _max, andV _max) were evaluated for this system. The use of calcium alginate immobilized cells in a continuous-flow stirred tank reactor lead to enhanced fermentative performance, namely a maximum productivity of 0.27 g/l h and 1.13% ethanol yield. The immobilized cells in continuous flow reactors represent an attractive option for fermenting sugars released by sulphuric acid hydrolysis ofP. radiata wood.     

Anthrahydroquinone-2,6,-disulfonate (AH<Subscript>2</Subscript>QDS) increases hydrogen molar yield and xylose utilization in growing cultures of <Emphasis Type="Italic">Clostridium beijerinckii</Emphasis>

H₂ production and xylose utilization were investigated using the fermentative culture Clostridium beijerinckii NCIMB 8052. Adding anthrahydroquinone-2,6-disulfonate (AH₂QDS) increased the extent of xylose utilization by 56% and hydrogen molar yield by 24–37%. Enhanced hydrogen molar yield correlated with increased xylose utilization and increases in the acetate/butyrate product ratio. An electron balance indicated that AH₂QDS shifted the electrons from the butyric acid pathway (NADH-dependent pathway) to the acetic acid pathway (non-NADH-dependent pathway), putatively creating a surplus of reducing equivalents that were then available for hydrogen production. These data demonstrate that hydrogen yield and xylose utilization can be manipulated by amending redox active molecules into growing cultures. This will impact biohydrogen/biofuel production by allowing physiological manipulations of growing cells for increased (or decreased) output of selected metabolites using amendments that are not consumed during the reactions. Although the current yield increases are small, they suggest a target for cellular alterations. In addition, increased xylose utilization will be critical to the fermentation of pretreated lignocellulosic feedstocks, which may have higher xylose content.     

Hydrogen production conditions from food waste by dark fermentation with Clostridium beijerinckii KCTC 1785

The optimum conditions for biological hydrogen production from food waste by Clostridium beijerinckii KCTC 1875 were investigated. The optimum initial pH and fermentation temperature were 7.0 and 40°C, respectively. When the pH of fermentation was controlled to 5.5, a maximum amount of hydrogen could be obtained. Under these conditions, about 2,737 mL of hydrogen was produced from 50 g COD/L of food waste for 24 h, and the hydrogen content in the biogas was 38%. Hydrogen production rate and yield were about 108 mL/L·h and 128 mL/g COD_degraded, respectively. High concentrations of acetic (< 5,000 mg/L) or butyric acid (< 3,000 mg/L) significantly inhibited hydrogen production.     

酒色着色菌利用产酸克雷伯氏菌发酵废液产氢

研究了酒色着色菌(Chromatium vinosum DSM185)利用产酸克雷伯氏菌（Klebsiella oxytoca HP1）发酵产氢废液进行光发酵和暗发酵产氢的可行性,以达到对产氢底物的充分利用和对产氢废液的进一步处理。研究结果表明C.vinosum可以利用K.oxytoca的发酵废液进行光发酵产氢和暗发酵产氢。C.vinosum发酵产氢后废液中残余还原糖和主要有机酸（丁酸）的含量明显降低,发酵产氢的最佳pH为6.5,添加0.1%(W/W)NH₄Cl能促进产氢。在光照条件下丁酸利用率可达54.38%,产氢量达36.97 mL/mg;在黑暗条件下丁酸利用率可达36.01%,产氢量达37.50mL/mg。     

The effect of aminopterin (4-amino folic acid) on growth and cell division of fermentative versus oxidative yeasts

In a related brewing study detailed characteristics of fermentations displaying effective yeastaminopterin interaction were presented.Fermentative yeast types (certain Saccharomyces species and Selenotila intestinalis) proved effective aminopterin reactors whereas oxidative yeasts (certain Candida, Cryptococcus, Pichia, Rhodotorula, Saccharomyces, and Trigonopsis species) proved ineffective reactors. In general effective reactors were polyploids characterized by the lack of film or pellicle formation and ineffective reactors the opposite. In stationary fermentations the Fleischmann 139 strain of S. cerevisiae proved a fair reactor. When aerated it proved an ineffective reactor and aminopterin or products there-of stimulated growth. Conversely aeration enhanced aminopterin activity of effective reactor yeasts.The positive effect of biotin on aminopterin activity and the negative effect of yeast extract, L-asparagine, adenine and thymine is shown and compared and contrasted with earlier reported studies.These findings supported by outside data suggest that oxidative yeasts (and bacteria) can readily elicit enzymes capable of inactivating aminopterin whereas fermentative types are lacking in this capability. Finally that past yeast-aminopterin studies were conducted with oxidative yeast types.Advantages of effective aminopterin reactor yeasts to be published elsewhere include improved ultrastructure using KMnO₄–OsO₄ fixation, a yeast bioassay procedure for detecting aminopterin in plasma and urine, and cell synchronization.Non-Standard Abbreviation apt aminopterin     

Hydrogen and methane production from desugared molasses using a two‐stage thermophilic anaerobic process

Hydrogen and methane production from desugared molasses by a two‐stage thermophilic anaerobic process was investigated in a series of two up‐flow anaerobic sludge blanket (UASB) reactors. The first reactor that was dominated with hydrogen‐producing bacteria of Thermoanaerobacterium thermosaccharolyticum and Thermoanaerobacterium aciditolerans could generate a high hydrogen production rate of 5600 mL H₂/day/L, corresponding to a yield of 132 mL H₂/g volatile solid (VS). The effluent from the hydrogen reactor was further converted to methane in the second reactor with the optimal production rate of 3380 mL CH₄/day/L, corresponding to a yield of 239 mL CH₄/g VS. Aceticlastic Methanosarcina mazei was the dominant methanogen in the methanogenesis stage. This work demonstrates that biohydrogen production can be very efficiently coupled with a subsequent step of methane production using desugared molasses. Furthermore, the mixed gas with a volumetric content of 16.5% H_2, 38.7% CO₂, and 44.8% CH₄, containing approximately 15% energy by hydrogen is viable to be bio‐hythane.     

Growth and butyric acid production by Clostridium populeti

The growth of Clostridium populeti in 2% (w/v) glucose medium containing 0.2% (w/v) yeast extract was optimal with 10 mM NH₄Cl as the nitrogen source. Although the maximum specific growth rate (=0.32 h^-1) with 5 mM NH₄Cl was similar, the biomass yield was about 30% lower than that at the optimum. Either sodium sulphide or cysteine-HCl at an optimum concentration of 0.33 mM and 5.0 mM respectively, could serve as the sole sulphur source for growth. The growth rate was unaffected by initial glucose concentrations of up to 10% (w/v), but in the presence of 15% glucose it declined by about 35%. The molar yield of butyric acid (mol/mol glucose) declined from 0.70 in 1% (w/v) initial glucose medium to 0.39 in 10% glucose medium. In 5.7% initial glucose medium, butyric acid levels of 6.3 g/l were obtained (0.56 mol butyrate/mol glucose) after 72 h of incubation in 2.5 l batch cultures. A decrease of about 50% in the maximum specific growth rate of C. populeti was observed in the presence of an initial concentration of either 1.2 g/l of butyric acid or 18.9 g/l of acetic acid.This paper is issued as NRCC No. 29032     

Hydrogen-producing capability of anaerobic activated sludge in three types of fermentations in a continuous stirred-tank reactor

A continuous stirred-tank reactor was used as an anaerobic sludge system and the hydrogen production capabilities of three typical fermentations, in terms of specific hydrogen production rates, were investigated under the same hydraulic retention times (8 h) and influent chemical oxygen demand (5000 mg/L) at 35 °C. The reactor was continuously fed with diluted molasses, while the pH and oxidation reduction potential in the reactor were regulated to control the type of fermentation. The specific hydrogen production rate of the anaerobic sludge reached 2.96 mol/kg mixed liquid volatile suspended solid (MLVSS)/day, (mol•kg MLVSS^− 1 d^− 1), in ethanol-type fermentation, while 0.57 mol·kg MLVSS^− 1 d^− 1 in butyric acid-type fermentation, and 0.022 mol·kgMLVSS^− 1 d^− 1 in propionic acid-type fermentation. The hydrogen production capability of ethanol-type fermentation was 4.11 times greater than that of butyric acid-type fermentation and 148 times that of propionic acid-type fermentation.     

Hybrid Cavitation/Constructed Wetland Reactors for Treatment of Chlorinated and Non‐Chlorinated Organics

Mitigation strategies can be implemented to decrease chlorinated and non‐chlorinated organic exposures to biota of aquatic receiving systems thereby reducing associated risks. In this work, we investigated the concept of coupling a physical/chemical reactor (i.e. a cavitation reactor) with a biological reactor (i.e. a constructed wetland) in an effort to efficiently transform PCE, TCE, and petroleum in freshwater into non‐toxic chemical forms or concentrations. Rates of TCE degradation due to cavitation ranged from 0.010 to 0.026 min^‐1 with corresponding half‐lives of 69 to 27 min. Compared to controls, degradation of petroleum in water by cavitation was not detected in these experiments. After treatment in anaerobic wetland reactors, TCE and PCE decreased by more than 99 % under two flow regimes (5‐d and 20‐d HRT). In reciprocating constructed wetland reactors receiving petroleum, mean COD, BOD₅, and total Zn decreased by 90.0, 88.8, and 86.8 %, respectively, in wetland outflows compared to the initial conditions (96‐h HRT). Percent survival (96‐h) of D. magna and P. promelas increased from zero percent in initial conditions to 80.1 (± 18.9) and 80.0 (± 21.4) %, respectively, after treatment in the constructed wetland reactors. The experimental results obtained in the laboratory‐scale set‐up and the theoretical model for the hybrid reactor concept will be used to obtain the intrinsic kinetic coefficients for the appropriate reactors. This kinetic information will be used to scale‐up the hybrid reactor model concept for the same level of pollutant removal.     

异化铁还原细菌Clostridium sp.LQ25分离及其产氢与铁还原特性

[背景] 一些异化铁还原细菌兼具铁还原和发酵产氢能力,可作为发酵型异化铁还原细菌还原机制研究的对象。[目的] 筛选出一株发酵型异化铁还原细菌。在异化铁还原细菌培养体系中,设置不同电子供体并分析电子供体。[方法] 通过三层平板法从海洋沉积物中筛选纯菌株,基于16S rRNA基因序列进行菌株鉴定。通过测定细菌培养液Fe （II）浓度及发酵产氢量分析菌株异化铁还原和产氢性质。[结果] 菌株LQ25与Clostridium butyricum的16S rRNA基因序列相似性达到100%,结合电镜形态观察,菌株命名为Clostridium sp.LQ25。在氢氧化铁为电子受体培养条件下,菌株生长较对照组（未添加氢氧化铁）显著提高。菌株LQ25能够利用丙酮酸钠、葡萄糖和乳酸钠进行生长。丙酮酸钠为电子供体时,菌株LQ25细胞生长和异化铁还原效率最高,菌体蛋白质含量是（78.88±3.40） mg/L,累积产生Fe （II）浓度为（8.27±0.23） mg/L。以葡萄糖为电子供体时,菌株LQ25发酵产氢量最高,达（475.2±14.4） mL/L,相比对照组（未添加氢氧化铁）产氢量提高87.7%。[结论] 筛选到一株具有异化铁还原和发酵产氢能力的菌株Clostridium sp.LQ25,为探究发酵型异化铁还原细菌胞外电子传递机制提供了新的实验材料。     

Temporal and spatial distribution of <Emphasis Type="Italic">Bacillus</Emphasis> and <Emphasis Type="Italic">Clostridium histolyticum</Emphasis> in swine manure composting by fluorescent in situ hybridization (FISH)

The temporal and spatial distribution of the genus Bacillus and Clostridium histolyticum group in swine manure composting was determined by fluorescent in situ hybridization using fluorescently labeled 16S rRNA-targeted oligonucleotide probes LGC353b and Chis150, respectively. The temporal distribution of total bacteria, Bacillus and C. histolyticum, detected in each layer of the composting pile was noticeable in that the number of them detected at the high-temperature stage was higher than that of the cooling stage. The number detected at the cooling stage was higher than that of the temperature-rising stage. The number of the total bacteria distributed in three locations achieved balance at the stage of cooling. The spatial distribution of the genus Bacillus cells was that the number and the relative abundance of Bacillus cells detected in the middle layer of composting pile were the lowest at each stage of composting. However, the minimum value of the relative abundance exceeded 8%. Compared with Bacillus spp., the C. histolyticum group displayed higher relative abundance in the same layer at different stages of composting except in the top layer at the stage of high temperature. However, the characteristic of the spatial distribution was not noticeable. The detected limits of the genus Bacillus and C. histolyticum group were both found to be the high cell density of 10⁶ cells g⁻¹ (wet weight). These results indicated that the genus Bacillus and C. histolyticum group were the predominant bacteria in the swine manure composting process and may play important role in this complex environment.     

Variations of Bacterial Populations in Human Feces Measured by Fluorescent In Situ Hybridization with Group-Specific 16S rRNA-Targeted Oligonucleotide Probes

Six 16S rRNA-targeted oligonucleotide probes were designed, validated, and used to quantify predominant groups of anaerobic bacteria in human fecal samples. A set of two probes was specific for species of the Bacteroides fragilis group and the species Bacteroides distasonis. Two others were designed to detect species of the Clostridium histolyticum and the Clostridium lituseburense groups. Another probe was designed for the genera Streptococcus and Lactococcus, and the final probe was designed for the species of the Clostridium coccoides-Eubacterium rectale group. The temperature of dissociation of each of the probes was determined. The specificities of the probes for a collection of target and reference organisms were tested by dot blot hybridization and fluorescent in situ hybridization (FISH). The new probes were used in initial FISH experiments to enumerate human fecal bacteria. The combination of the two Bacteroides-specific probes detected a mean of 5.4 × 10¹⁰ cells per g (dry weight) of feces; the Clostridium coccoides-Eubacterium rectale group-specific probe detected a mean of 7.2 × 10¹⁰ cells per g (dry weight) of feces. The Clostridium histolyticum, Clostridium lituseburense, and Streptococcus-Lactococcus group-specific probes detected only numbers of cells ranging from 1 × 10⁷ to 7 × 10⁸ per g (dry weight) of feces. Three of the newly designed probes and three additional probes were used in further FISH experiments to study the fecal flora composition of nine volunteers over a period of 8 months. The combination of probes was able to detect at least two-thirds of the fecal flora. The normal biological variations within the fecal populations of the volunteers were determined and indicated that these variations should be considered when evaluating the effects of agents modulating the flora.     

Interactions between Clostridium beijerinckii and Geobacter metallireducens in co‐culture fermentation with anthrahydroquinone‐2, 6‐disulfonate (AH2QDS) for enhanced biohydrogen production from xylose

To enhance biohydrogen production, Clostridium beijerinckii was co‐cultured with Geobacter metallireducens in the presence of the reduced extracellular electron shuttle anthrahydroquinone‐2, 6‐disulfonate (AH₂QDS). In the co‐culture system, increases of up to 52.3% for maximum cumulative hydrogen production, 38.4% for specific hydrogen production rate, 15.4% for substrate utilization rate, 39.0% for substrate utilization extent, and 34.8% for hydrogen molar yield in co‐culture fermentation were observed compared to a pure culture of C. beijerinckii without AH₂QDS. G. metallireducens grew in the co‐culture system, resulting in a decrease in acetate concentration under co‐culture conditions and a presumed regeneration of AH₂QDS from AQDS. These co‐culture results demonstrate metabolic crosstalk between the fermentative bacterium C. beijerinckii and the respiratory bacterium G. metallireducens and suggest a strategy for industrial biohydrogen production. Biotechnol. Bioeng. 2013; 110: 164–172. © 2012 Wiley Periodicals, Inc.     

Kinetics of hydrolysis of type I, II, and III collagens by the class I and II Clostridium histolyticum collagenases.

The kinetics of hydrolysis of rat tendon type I, bovine nasal septum type II, and human placental type III collagens by class I and class IIClostridium histolyticum collagenases (CHC) have been investigated. To facilitate this study, radioassays developed previously for the hydrolysis of these [³H]acetylated collagens by tissue collagenases have been adapted for use with the CHC. While the CHC are known to make multiple scissions in these collagens, the assays are shown to monitor the initial proteolytic events. The individual kinetic parametersk _cat andK _M have been determined for the hydrolysis of all three collagens by both class I and class II CHC. The specific activities of these CHC toward fibrillar type I and III collagens have also been measured. In contrast to human tissue collagenases, neither class of CHC exhibits a marked specificity toward any collagen type either in solution or in fibrillar form. The values of the kinetic parametersk _cat andK _M for the CHC are similar in magnitude to those of the human enzymes acting on their preferred substrates. Thus, the widely held view that the CHC are more potent collagenases is not strictly correct. As with the tissue collagenases, the local collagen structure at the cleavage sites is believed to play an important role in determining the rates of the reactions studied.     

Characterization of microbial community and kinetics for spent sulfidic caustic applied autotrophic denitrification

Spent sulfidic caustic was applied to sulfur utilizing autotrophic denitrification as the simultaneous source of electron donor and alkalinity. The two experiment set-up of upflow anoxic hybrid growth reactor (UAHGR) and upflow anoxic suspended growth reactor (UASGR) was adopted and nitrate removals were similar in both reactors. Approximately 90% of the initial nitrate was denitrified at nitrate loading rate of 0.15∼0.40 kgNO₃ ⁻/m³·d. The experimental stoichiometric ratio of sulfate production to nitrate removal was ranged from 1.5 to 2.1 mgSO₄ ²⁻/mgNO₃ ⁻. During the operation period, denaturing gradient gel electrophoresis (DGGE) analysis of polymerase chain reaction (PCR)-amplified 16S rDNA fragments for the sludge sample of both reactors showed the change of microbial communities. Thiobacillus denitrificans-like microorganism occupied 28.5% (18 clones) of the 63 clones by cloning the PCR products from the sludge sample of UAHGR. Acidovorax avenae, which can reduce nitrate to nitrogen gas while oxidizing phenol (heterotrophic denitrifier), was also found in 7 clones (11.1%). Although an organic carbon source was not added to the medium, a microorganism (Kaistella koreensis) capable of oxidizing organic compounds was found in 7 clones (11.1%). Therefore, the microbial community of spent sulfidic caustic applied autotrophic denitrification process well corresponds to the substrate components of spent sulfidic caustic. Through the batch cultivation of microorganisms in UAHGR, the microbial kinetic coefficients of spent sulfidic caustic applied autotrophic denitrification were estimated to be μ _max = 0.097 h⁻¹, k _d = 0.0021 h⁻¹, K _s = 200 mgNO₃ ⁻/L, and Y = 0.31 mgMLVSS/mgNO₃ ⁻.     

Biosynthesis of butyric acid from cabbage stem and molasses by the strain Clostridium butyricum VKPM B-9619

The acidogenesis of the strain Clostridium butyricum VKPM B-9619 on synthetic medium SOL, a fermentative hydrolyzate of cabbage stem, and molasses as cheap sources of carbohydrate nutrition of micro-organisms, has been studied. The yield of butyric acid was no less than 43%. It was found that, in addition to hexoses, the strain ferments pentoses (xylose and arabinose), which enables the processing of wastes of pentosan- and cellulose-containing plant raw materials with the addition of molasses. The fermentation liquid of the strain can be used for the isolation of butyric acid by the ion exchange method.     

Hydrogen production by the newly isolated Clostridium beijerinckii RZF-1108

A fermentative hydrogen-producing strain, RZF-1108, was isolated from a biohydrogen reactor, and identified as Clostridium beijerinckii on the basis of the 16S rRNA gene analysis and physiobiochemical characteristics. The effects of culture conditions on hydrogen production by C. beijerinckii RZF-1108 were investigated in batch cultures. The hydrogen production and growth of strain RZF-1108 were highly dependent on temperature, initial pH and substrate concentration. Yeast extract was a favorable nitrogen source for hydrogen production and growth of RZF-1108. Hydrogen production corresponded to cell biomass yield in different culture conditions. The maximum hydrogen evolution, yield and production rate of 2209 ml H₂/l medium, 1.97 mol H₂/mol glucose and 104.20 ml H₂/g CDW h⁻¹ were obtained at 9 g/l of glucose, initial pH of 7.0, inoculum volume of 8% and temperature of 35 °C, respectively. These results demonstrate that C. beijerinckii can efficiently produce H₂, and is another model microorganism for biohydrogen investigations.     

克氏梭菌硫解酶的鉴定及其功能研究

【目的】硫解酶是梭菌属微生物合成短中链脂肪酸的关键酶。克氏梭菌(Clostridium kluyveri)具有3个高度同源的硫解酶编码基因,对这3个基因的功能鉴定是解析克氏梭菌高己酸合成能力的关键。【方法】通过发酵动力学分析确定克氏梭菌的己酸和丁酸生成动力学特征;转录组测序结合反转录-荧光定量RCR分析克氏梭菌3个硫解酶编码基因的表达水平和时序表达特征;在大肠杆菌中异源表达这3个硫解酶,并对其硫解酶动力学参数进行测定。【结果】克氏梭菌生成丁酸、己酸、辛酸,其中己酸为主要代谢产物;转录组数据显示,在乙酸消耗完全之前,thlA1基因维持恒定表达,thlA2基因表达时序上调,thlA3基因表达时序下调,转录组测序表明3个硫解酶编码基因均具有较高水平的转录活性,thlA2和thlA3的最高表达量分别约为thlA1的29%和43%;硫解酶动力学参数测定结果表明,克氏梭菌3个硫解酶对于四碳底物均显示出相似的底物亲和力(K_m),但ThlA1对四碳底物的催化效率(k_(cat)/K_m)略低于ThlA2和ThlA3。【结论】克氏梭菌的3个硫解酶均具有催化活性,在克氏梭菌体内均呈活跃表达,表明克氏梭菌拥有3个具有催化活性的硫解酶,这为后续深入研究克氏梭菌己酸合成机理奠定了基础。     

Glycine fermentation by Clostridium histolyticum

Clostridium histolyticum grew on glycine, arginine, or threonine as sole substrate. Arginine degradation preceded that of glycine and partially inhibited that of threonine when two amino acids were present. Each amino acid seemed to be individually catabolized, not by a Stickland type of reaction. Glycine fermentation required the presence of complex ingredients. Therefore, an effect of selenite on glycine catabolism could only be demonstrated after scavenging selenium contamination by preculturing Peptostreptococcus glycinophilus in that medium. C. acidiurici was not suited as selenium accumulating organism as C. histolyticum was inhibited by the residual uric acid. Arginine catabolism was unaffected by seleniuum depriviation. The labelling pattern obtained in acetate after incubation of C. histolyticum with [1-¹⁴C]- or [2-¹⁴C]glycine strongly indicated the metabolism of glycine via the glycine reductase pathway.     

Influence of Reduced Electron Shuttling Compounds on Biological H<Subscript>2</Subscript> Production in the Fermentative Pure Culture <Emphasis Type="Italic">Clostridium beijerinckii</Emphasis>

Several reports suggest that extracellular electron shuttles influence fermentative metabolism in a beneficial manner for bioremediation and biotechnology strategies. The focus of this research was to characterize the effects of reduced electron shuttling molecules on fermentative H₂ production. Reduced electron shuttles may provide reducing equivalents to generate H₂, which influences alternate cellular processes. Electron shuttling compounds cycle between reduced-oxidized states and influence fermentative physiology. Clostridium beijerinckii fermentation was altered using a physiological approach that resulted in H₂ production with the reduced extracellular electron shuttle anthrahydroquinone-2,6,-disulfonate (AH₂QDS) and biologically reduced humic substances as the primary electron donors. Cells were suspended in a buffer with an excess of the biological electron transfer molecule NAD⁺, with AH₂QDS (100–1000 μM) or biologically reduced humic substances (0.01–0.025 g/L) as the sole electron source. Increasing concentrations of AH₂QDS and reduced humics increased H₂ production, while H₂ production was suppressed by Fe(III) hydroxides, which outcompeted the cells for electrons from the reduced shuttles, suggesting that the shuttles are in fact electron donors for H₂ production. Oxidized AQDS/humics did not increase H₂ production. Organic acid production shifted toward butyric acid in the presence of reduced electron shuttles, particularly with growing cells. Growth and hydrogen production rates in growing cells were initially faster in the presence of the reduced electron shuttles; however, the final biomass yield was inversely proportional to the starting AH₂QDS concentration, which suggests that reduced shuttles may compete with anabolic cell processes for available energetic resources or that the shift to excess butyrate becomes toxic to the cells.