Lipase in biphasic alginate beads as a biocatalyst for esterification of butyric acid and butanol in aqueous media

Esterification of organic acids and alcohols in aqueous media is very inefficient due to thermodynamic constraints. However, fermentation processes used to produce organic acids and alcohols are often conducted in aqueous media. To produce esters in aqueous media, biphasic alginate beads with immobilized lipase are developed for in situ esterification of butanol and butyric acid. The biphasic beads contain a solid matrix of calcium alginate and hexadecane together with 5 mg/mL of lipase as the biocatalyst. Hexadecane in the biphasic beads serves as an organic phase to facilitate the esterification reaction. Under optimized conditions, the beads are able to catalyze the production of 0.16 mmol of butyl butyrate from 0.5 mmol of butyric acid and 1.5 mmol of butanol. In contrast, when monophasic beads (without hexadecane) are used, only trace amount of butyl butyrate is produced. One main application of biphasic beads is in simultaneous fermentation and esterification (SFE) because the organic phase inside the beads is very stable and does not leach out into the culture medium. SFE is successfully conducted with an esterification yield of 6.32% using biphasic beads containing iso-octane even though the solvent is proven toxic to the butanol-producing Clostridium spp.     

体外法探究猪空肠和回肠黏膜微生物对低聚半乳糖和低聚甘露糖的发酵特性

【背景】小肠黏膜微生物是肠道菌群的重要组成部分,大量研究表明日粮添加低聚半乳糖（galacto-oligosaccharides,GOS）和低聚甘露糖（manno-oligosaccharides,MOS）能够调控猪的大肠菌群结构,但关于其调控小肠黏膜微生物的研究较少。【目的】通过体外发酵法探究猪空肠黏膜和回肠黏膜微生物发酵GOS和MOS的规律。【方法】以生长猪的空肠黏膜微生物和回肠黏膜微生物作为接种物,以GOS和MOS作为底物进行厌氧发酵,在发酵0、6、12、24 h时采样测定总菌数量、pH、氨态氮（ammonia nitrogen,NH₃-N）、菌体蛋白（microbial crude protein,MCP）和有机酸,在24 h收集微生物提取DNA进行细菌定量分析。【结果】在24 h时,回肠黏膜组的NH₃-N浓度显著低于空肠黏膜组,而MCP浓度显著高于空肠黏膜组（P<0.05）。在发酵的前6 h各组pH无明显变化,有机酸积累较少。在12 h时,MOS组的乳酸、乙酸、丁酸和总短链脂肪酸产量显著高于GOS组（P<0.05）,此时只有回肠黏膜组有少量丙酸产生。在24 h时,MOS回肠黏膜组乳酸产量最高而pH值最低（P<0.05）。相较于MOS组,GOS组显著提高了丙酸的产量（P<0.05）。相较于GOS组,MOS组显著提高了乙酸的产量,在空肠黏膜组中显著提高了丁酸和总短链脂肪酸的产量（P<0.05）。定量结果表明,在24 h时,各处理组的厚壁菌门数量都接近总菌数量,属于优势菌门。相较于MOS组,GOS组显著提高了拟杆菌门、链球菌属、韦荣氏球菌属和普拉梭菌细菌的数量,提高了空肠黏膜组中Clostridium cluster IV和回肠黏膜组中Clostridium cluster XIVa的数量（P<0.05）。相较于GOS组,MOS组显著提高了大肠杆菌和乳酸杆菌属的数量,提高了回肠黏膜组中罗氏菌属的数量（P<0.05）。【结论】猪小肠黏膜微生物对GOS和MOS具有不同的发酵模式,主要表现在有机酸的产生和促进细菌的增殖方面。GOS具有产丙酸优势,提高了拟杆菌门和韦荣氏球菌属的数量;MOS促进了乙酸的产生,提高了大肠杆菌和乳酸杆菌的数量。     

Butyric acid production from brown algae using <Emphasis Type="Italic">Clostridium tyrobutyricum</Emphasis> ATCC 25755

Butyric acid fermentation by Clostridium tyrobutyricum ATCC 25755 using glucose or brown algae as a carbon source was carried out. Initially, different fermentation modes (batch, fed-batch, and semi-continuous) at pH 6 and 37°C were compared using a model medium containing glucose as a carbon source. By feeding the whole medium containing 40 ∼ 50 and 30 g/L of glucose into the fed-batch and semi-continuous fermentations, very similar butyrate yields (0.274 and 0.252 g butyrate/g glucose, respectively) and productivities (0.362 and 0.355 g/L/h, respectively) were achieved. The highest butyrate concentration was about 50 g/L, which was observed in the fed-batch fermentation with whole medium feeding. However, semi-continuous fermentation sustained a longer fermentation cycle than the fed-batch fermentation due to end-product and metabolic waste inhibition. The established conditions were then applied to the fermentation using brown algae, Laminaria japonica and Undaria pinnatifida, as substrates for butyric acid fermentation. To hydrolyze brown algae, 7.5 ∼ 10% (w/v) dried brown algae powder was suspended in 1% (w/v) NaOH or 0.5 ∼ 2.5% (w/v) H₂SO₄ and then autoclaved at 121°C for 30 ∼ 90 min. The resulting butyrate concentration was about 11 g/L, which was produced from 100 g/L of L. japonica autoclaved for 60 min in 1.5% H₂SO₄ acid solution.     

Effects of Acetate and Butyrate During Glycerol Fermentation by Clostridium butyricum

The effects of acetate and butyrate during glycerol fermentation to 1,3-propanediol at pH 7.0 by Clostridium butyricum CNCM 1211 were studied. At pH 7.0, the calculated quantities of undissociated acetic and butyric acids were insufficient to inhibit bacterial growth. The initial addition of acetate or butyrate at concentrations of 2.5 to 15 gL⁻¹ had distinct effects on the metabolism and growth of Clostridium butyricum. Acetate increased the biomass and butyrate production, reducing the lag time and 1,3-propanediol production. In contrast, the addition of butyrate induced an increase in 1,3-propanediol production (yield: 0.75 mol/mol glycerol, versus 0.68 mol/mol in the butyrate-free culture), and reduced the biomass and butyrate production. It was calculated that reduction of butyrate production could provide sufficient NADH to increase 1,3-propanediol production. The effects of acetate and butyrate highlight the metabolic flexibility of Cl. butyricum CNCM 1211 during glycerol fermentation. Received: 2 January 2001 / Accepted: 6 February 2001     

Triphasic esterification of butanol and butyric acid in fermentation media

Butanol and butyric acid produced from acetone-butanol-ethanol (ABE) fermentation can be used to produce butyl butyrate, an important fragrance ester. However, low levels of butanol and butyric acid need to be purified from culture media first with energy-intensive distillation processes. In this study, a triphasic (organic/aqueous/fluorous) system is developed to esterify butanol and butyric acid in spent culture media into butyl butyrate directly without purification. The produced butyl butyrate forms a distinct organic phase floating on top and can then be separated easily. In a model system containing 37.1 g/L of butanol and 44.1 g/L of butyric acid, 57% of the butanol is converted to butyl butyrate after 8 h of esterification. With multiple cycles of esterification and product removal, butanol conversion can be further increased to 86%. When spent culture medium containing 7.12 g/L of butanol and 4.81 g/L of butyric acid is used for esterification, 38% of butanol (0.36 mmol) is consumed and 0.33 mmol of butyl butyrate is produced. However, when ABE fermentation and esterification are carried out simultaneously, only 0.042 mmol of butyl butyrate is produced, probably due to the incompatible pH requirements for cell growth (pH 5–7) and esterification (pH 2–3).     

Photoautotrophic synthesis of butyrate by metabolically engineered cyanobacteria

Direct conversion of carbon dioxide into chemicals using engineered autotrophic microorganisms offers a potential solution for both sustainability and carbon mitigation. Butyrate is an important chemical used in various industries, including fragrance, food, and plastics. A model cyanobacterium Synechococcus elongatus PCC 7942 was engineered for the direct photosynthetic conversion of CO ₂ to butyrate. An engineered Clostridium Coenzyme A (CoA)-dependent pathway leading to the synthesis of butyryl-CoA, the precursor to butyrate, was introduced into S. elongatus PCC 7942. Two CoA removal strategies were then individually coupled to the modified CoA-dependent pathway to yield butyrate production. Similar results were observed between the two CoA removal strategies. The best butyrate producing strain of S. elongatus resulted in an observed butyrate titer of 750 mg/L and a cumulative titer of 1.1 g/L. These results demonstrated the feasibility of photosynthetic butyrate production and expanded the chemical repertoire accessible for production by photoautotrophs.     

泸型酒窖泥中梭菌的分离及代谢产物分析

[目的] 分离窖泥中的梭菌微生物并对其代谢产物进行评估。[方法] 对窖泥中梭菌群落的16S rRNA基因进行高通量测序;利用高丰度的梭菌OTU序列在KOMODO数据库进行培养基的预测,定向分离窖泥中梭菌菌株;采用顶空固相微萃取结合气相色谱质谱联用仪对窖泥和代表性梭菌菌株的挥发性代谢产物进行检测。[结果] 利用KOMODO数据库预测的梭菌培养基共计筛选到31株梭菌微生物,分属于梭菌属的14个种;根据风味代谢特性,这些菌株主要分为两大类,一是C.carboxidivorans、C.sporogenes和C.tyrobutyricum等产酸为主的梭菌,二是C.beijerinckii、C.butyricum和C.sphenoides等产醇为主的梭菌。[结论] 利用测序序列预测培养基有助于从窖泥中分离获得丰富的梭菌菌株,其物种和代谢能力的多样性对解析白酒复杂风味形成机理奠定了一定的基础。     

Initial butyrate producers during infant gut microbiota development are endospore formers

The acquisition of the infant gut microbiota is key to establishing a host-microbiota symbiosis. Microbially produced metabolites tightly interact with the immune system, and the fermentation-derived short-chain fatty acid butyrate is considered an important mediator linked to chronic diseases later in life. The intestinal butyrate-forming bacterial population is taxonomically and functionally diverse and includes endospore formers with high transmission potential. Succession, and contribution of butyrate-producing taxa during infant gut microbiota development have been little investigated. We determined the abundance of major butyrate-forming groups and fermentation metabolites in faeces, isolated, cultivated and characterized the heat-resistant cell population, which included endospores, and compared butyrate formation efficiency of representative taxa in batch cultures. The endospore community contributed about 0.001% to total cells, and was mainly composed of the pioneer butyrate-producing Clostridium sensu stricto. We observed an increase in abundance of Faecalibacterium prausnitzii, butyrate-producing Lachnospiraceae and faecal butyrate levels with age that is likely explained by higher butyrate production capacity of contributing taxa compared with Clostridium sensu stricto. Our data suggest that a successional arrangement and an overall increase in abundance of butyrate forming populations occur during the first year of life, which is associated with an increase of intestinal butyrate formation capacity.     

A computer-controlled system to simulate conditions of the large intestine with peristaltic mixing, water absorption and absorption of fermentation products

This paper introduces a new type of system to simulate conditions in the large intestine. This system combines removal of metabolites and water with peristaltic mixing to obtain and handle physiological concentrations of microorganisms, dry matter and microbial metabolites. The system has been designed to be complementary to the dynamic multi-compartmental system that simulates conditions in the stomach and small intestine described by Minekus et al. [Minekus M, Marteau P, Havenaar R, Huis in't Veld JHJ (1995) ATLA 23:197–209]. High densities of microorganisms, comparable to those found in the colon in vivo, were achieved by absorption of water and dialysis of metabolites through hollow-fibre membranes inside the reactor compartments. The dense chyme was mixed and transported by peristaltic movements. The potential of the system as a tool to study fermentation was demonstrated in experiments with pectin, fructo-oligosaccharide, lactulose and lactitol as substrates. Parameters such as total acid production and short-chain fatty acid (SCFA) patterns were determined with time to characterize the fermentation. The stability of the microflora in the system was tested after inoculation with fresh fecal samples and after inoculation with a microflora that was main-tained in a fermenter. Both approaches resulted in total anaerobic bacterial counts higher than 10¹⁰ colony-forming units/ml with physiological levels of Bifidobacterium, Lactobacillus, Enterobacteriaceae and Clostridium. The dry matter content was approximately 10%, while the total SCFA concentration was maintained at physiological concentrations with similar molar ratios for acetic acid, propionic acid and butyric acid as measured in vivo. Received: 4 February 1999 / Received revision: 4 June 1999 / Accepted: 4 June 1999     

Efficient production of butyric acid from Jerusalem artichoke by immobilized Clostridium tyrobutyricum in a fibrous-bed bioreactor

Butyric acid is an important specialty chemical with wide industrial applications. The feasible large-scale fermentation for the economical production of butyric acid requires low-cost substrate and efficient process. In the present study, butyric acid production by immobilized Clostridium tyrobutyricum was successfully performed in a fibrous-bed bioreactor using Jerusalem artichoke as the substrate. Repeated-batch fermentation was carried out to produce butyric acid with a high butyrate yield (0.44 g/g), high productivity (2.75 g/L/h) and a butyrate concentration of 27.5 g/L. Furthermore, fed-batch fermentation using sulfuric acid pretreated Jerusalem artichoke hydrolysate resulted in a high butyric acid concentration of 60.4 g/L, with the yield of 0.38 g/g and the selectivity of ∼85.1 (85.1 g butyric acid/g acetic acid). Thus, the production of butyric acid from Jerusalem artichoke on a commercial scale could be achieved based on the system developed in this work.     

Continuous cultivation of Clostridium thermobutyricum in a rotary fermentor system

The growth behavior of Clostridium thermobutyricum JW171K and its production of butyric acid were investigated under continuous cultivation in a recently developed rotary fermentor. Using low dilution rates (up to 40 times the shortest doubling time), the continuous culture conditions caused metabolic shifts from butyrate formation to the production of acetate. Using an 18-h volumetric retention time, no true steady state in butyrate formation was achieved after 22 days, although the optical density was stable. Acetate and butyrate were formed in an oscillatory mode with an alternating predominance between these two products, indicating an oscillation between the less exergonic acetate-forming but higher ATP (4ATP mol⁻¹ glucose) forming mode, and the more exergonic butyrate and 3ATP mol⁻¹ glucose forming mode. During the continuous culture drastic changes in cell morphology occurred and, at the lower dilution rates, long, granulose-containing, filamentous cells with rounded protuberances and swellings were observed. A maximal butyrate concentration of 18.4 g L⁻¹ and a productivity of about 2.4 g L⁻¹ per h (at 25–27 mM concentration in the broth) were obtained. Journal of Industrial Microbiology & Biotechnology (2000) 24, 7–13. Received 26 April 1999/ Accepted in revised form 16 August 1999     

Regulation of acetate kinase and butyrate kinase by acids in Clostridium acetobutylicum

Abstract The effects of acetic acid and butyric acid on acetate kinase, butyrate kinase and acetoacetate decarboxylase levels are studied. It is shown that acetate kinase biosynthesis is regulated by acetic acid whereas butyric acid has no effect. Acetate kinase specific activity is found to be maximal at the beginning of the fermentation, and decreases as acetic acid concentration increases in the medium. Butyrate kinase is not regulated by the end-product acids; its specific activity is constant during the fermentation. In the presence of acetic acid, acetoacetate decarboxylase biosynthesis represents a 4-fold increase in activity over a culture without acetate and a 1.7-fold increase over that obtained in presence of butyrate. The technique of fermentation used allows us to show that bacterial growth and solventogenesis may occur simultaneously.     

Solvent production byClostridium pasteurianum in media of high sugar content

Summary The fermentation end products ofClostridium pasteurianum ATCC 6013 are normally acetic and butyric acids. When grown in media of high sugar content however, significant quantities of solvents (acetone, butanol and ethanol) were produced. Solvent production was not stimulated by added acetic and butyric acids, nor was the effect due to a low water activity of the mediumper se.     

Prolonged conversion of n-butyrate to n-butanol with Clostridium saccharoperbutylacetonicum in a two-stage continuous culture with in-situ product removal

n‐Butanol was produced continuously in a two‐stage fermentor system with integrated product removal from a co‐feed of n‐butyric acid and glucose. Glucose was always required as a source of ATP and electrons for the conversion of n‐butyrate to n‐butanol and for biomass growth; for the latter it also served as a carbon source. The first stage generated metabolically active planktonic cells of Clostridium saccharoperbutylacetonicum strain N1‐4 that were continuously fed into the second (production) stage; the volumetric ratio of the two fermentors was 1:10. n‐Butanol was removed continuously from the second stage via gas stripping. Implementing a two‐stage process was observed to dramatically dampen metabolic oscillations (i.e., periodical changes of solventogenic activity). Culture degeneration (i.e., an irreversible loss of solventogenic activity) was avoided by periodical heat shocking and re‐inoculating stage 1 and by maintaining the concentration of undissociated n‐butyric acid in stage 2 at 3.4 mM with a pH‐auxostat. The system was successfully operated for 42 days during which 93% of the fed n‐butyrate was converted to n‐butanol at a production rate of 0.39 g/(L × h). The molar yields Y_{n‐butanol/n‐butyrate} and Y_{n‐butanol/glucose} were 2.0, and 0.718, respectively. For the same run, the molar ratio of n‐butyrate to glucose consumed was 0.358. The molar yield of carbon in n‐butanol produced from carbon in n‐butyrate and glucose consumed (Y_{n‐butanol/carbon}) was 0.386. These data illustrate that conversion of n‐butyrate into n‐butanol by solventogenic Clostridium species is feasible and that this can be performed in a continuous system operating for longer than a month. However, our data also demonstrate that a relatively large amount of glucose is required to supply electrons and ATP for this conversion and for cell growth in a continuous culture. Biotechnol. Bioeng. 2012; 109:913–921. © 2011 Wiley Periodicals, Inc.     

Microbial Consortia for Hydrogen Production Enhancement

Ten efficient hydrogen-producing strains affiliated to the Clostridium genus were used to develop consortia for hydrogen production. In order to determine their saccharolytic and proteolytic activities, glucose and meat extract were tested as fermentation substrates, and the best hydrogen-producing strains were selected. The C. roseum H5 (glucose-consuming) and C. butyricum R4 (protein-degrading) co-culture was the best hydrogen-producing co-culture. The end-fermentation products for the axenic cultures and co-cultures were analyzed. In all cases, organic acids, mainly butyrate and acetate, were produced lowering the pH and thus inhibiting further hydrogen production. In order to replace the need for reducing agents for the anaerobic growth of clostridia, a microbial consortium including Clostridium spp. and an oxygen-consuming microorganism able to form dense granules (Streptomyces sp.) was created. Increased yields of hydrogen were achieved. The effect of adding a butyrate-degrading bacteria and an acetate-consuming archaea to the consortia was also studied.     

Effects of extractive fermentation on butyric acid production byClostridium acetobutylicum

Summary The addition of an oleyl alcohol extractant to a batch fermentation of glucose byClostridium acetobutylicum resulted in a concentration profile that was distinctly different from the non-extractive control fermentation. The concentration of butyric acid increased and subsequently decreased in the control fermentation. The concentration of butyric acid increased but did not subsequently decrease in the oleyl alcohol extractive fermentation. The production of butyric acid was found to have been prolonged into the solventogenic phase in the oleyl alcohol extractive fermentation. Butyric acid was continually replenished from glucose while it was being converted to butanol. Supplementation of exogenous acetic and butyric acids, the metabolic uncoupler carbonyl cyanide 3-chlorophenylhydrazone, or decanol to the oleyl alcohol extractive fermentation helped to reinstate the normal butyric acid concentration profile. These findings are discussed with respect to the effects of these additives on the pH ofC. acetobutylicum and its importance with regard to the production of butyric acid.     

Buffering as a means for increasing growth and butanol production byClostridium acetobutylicum

Summary The objective of this work was to optimize butanol formation in the acetone-butanol-ethanol (ABE) fermentation by examining the level of buffering as it affects the dissociation of butyric acid to the less toxic butyrate anion. Experiments were carried out in batch culture using chemically defined (P2) or complex media containing various buffering agents. These included salts of acetate, citrate, phosphate, nitrate, or bicarbonate, representing a range of pK _a values and buffering capacities. Growth in highly buffered medium was found to increase the stationary phase cell density, carbohydrate utilization, and the final butanol concentration. At higher levels of buffering, increased growth and elevated concentrations of butyric acid were required to initiate solventogenesis, suggesting the involvement of a critical threshold level of undissociated butyric acid.     

Role of the global regulator Rex in control of NAD+‐regeneration in Clostridioides (Clostridium) difficile

For the human pathogen Clostridioides (also known as Clostridium) difficile, the ability to adapt to nutrient availability is critical for its proliferation and production of toxins during infection. Synthesis of the toxins is regulated by the availability of certain carbon sources, fermentation products and amino acids (e.g. proline, cysteine, isoleucine, leucine and valine). The effect of proline is attributable at least in part to its role as an inducer and substrate of D‐proline reductase (PR), a Stickland reaction that regenerates NAD⁺ from NADH. Many Clostridium spp. use Stickland metabolism (co‐fermentation of pairs of amino acids) to generate ATP and NAD⁺. Synthesis of PR is activated by PrdR, a proline‐responsive regulatory protein. Here we report that PrdR, in the presence of proline, represses other NAD⁺‐generating pathways, such as the glycine reductase and succinate‐acetyl CoA utilization pathways leading to butyrate production, but does so indirectly by affecting the activity of Rex, a global redox‐sensing regulator that responds to the NAD⁺/NADH ratio. Our results indicate that PR activity is the favored mechanism for NAD⁺ regeneration and that both Rex and PrdR influence toxin production. Using the hamster model of C. difficile infection, we revealed the importance of PrdR‐regulated Stickland metabolism in the virulence of C. difficile.     

Enzymatic esterification in organic media: role of water and organic solvent in kinetics and yield of butyl butyrate synthesis

Summary The respective roles of organic solvent and of water in butyl butyrate synthesis from n-butanol and n-butyric acid in n-hexane by Mucor miehei lipase have been investigated by analysis of the kinetics and the reaction balances. Esterificaton was found to take place in both low water systems containing solid enzyme in hexane and in biphasic aqueous enzyme solution/hexane systems. In the solid enzyme system, the enzyme adsorbed the water produced, thus delaying the appearance of a discrete aqueous phase. As expected, the presence of some water was indispensable for this system, as its removal or exclusion by various means (adsorption, distillation) affected enzyme activity. However, water removal had little effect on the final yield of esterification. Reaction velocities were quite similar for the solid enzyme/hexane system and for the biphasic aqueous enzyme solution/hexane system. In the latter case, the butyl butyrate formed was almost exclusively found in the organic phase. Ethyl butyrate, a more polar compound, was synthesized with a lower yield. These results allow the conclusion that the reaction took place in a phase consisting of either solid hydrated enzyme with no discrete aqueous phase or of an aqueous enzyme solution by basically similar mechanisms according to the amount of water available to the system, the esterification being driven to completion by transfer of the ester into the organic phase because of a favourable partition coefficient. Offprint requests to: F. Monot     

Extractive fermentation for butyric acid production from glucose by Clostridium tyrobutyricum

A novel extractive fermentation for butyric acid production from glucose, using immobilized cells of Clostridium tyrobutyricum in a fibrous bed bioreactor, was developed by using 10% (v/v) Alamine 336 in oleyl alcohol as the extractant contained in a hollow-fiber membrane extractor for selective removal of butyric acid from the fermentation broth. The extractant was simultaneously regenerated by stripping with NaOH in a second membrane extractor. The fermentation pH was self-regulated by a balance between acid production and removal by extraction, and was kept at approximately pH 5.5 throughout the study. Compared with conventional fermentation, extractive fermentation resulted in a much higher product concentration (>300 g/L) and product purity (91%). It also resulted in higher reactor productivity (7.37 g/L. h) and butyric acid yield (0.45 g/g). Without on-line extraction to remove the acid products, at the optimal pH of 6.0, the final butyric acid concentration was only approximately 43.4 g/L, butyric acid yield was 0.423 g/g, and reactor productivity was 6.77 g/L. h. These values were much lower at pH 5.5: 20.4 g/L, 0.38 g/g, and 5.11 g/L. h, respectively. The improved performance for extractive fermentation can be attributed to the reduced product inhibition by selective removal of butyric acid from the fermentation broth. The solvent was found to be toxic to free cells in suspension, but not harmful to cells immobilized in the fibrous bed. The process was stable and provided consistent long-term performance for the entire 2-week period of study.