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.     

Metabolic engineering of Thermoanaerobacterium saccharolyticum for n-butanol production

The thermophilic anaerobe Thermoanaerobacterium saccharolyticum JW/SL-YS485 was investigated as a host for n-butanol production. A systematic approach was taken to demonstrate functionality of heterologous components of the clostridial n-butanol pathway via gene expression and enzymatic activity assays in this organism. Subsequently, integration of the entire pathway in the wild-type strain resulted in n-butanol production of 0.85 g/L from 10 g/L xylose, corresponding to 21% of the theoretical maximum yield. We were unable to integrate the n-butanol pathway in strains lacking the ability to produce acetate, despite the theoretical overall redox neutrality of n-butanol formation. However, integration of the n-butanol pathway in lactate deficient strains resulted in n-butanol production of 1.05 g/L from 10 g/L xylose, corresponding to 26% of the theoretical maximum.     

Feruloyl esterase production by Aspergillus terreus CECT 2808 and subsequent application to enzymatic hydrolysis

Ferulic acid esterases (FAE) were produced by Aspergillus terreus CECT 2808 from vine trimming shoots (VTS) and corn cob. Later, the fungal extracts thus obtained were used to enzymatically release ferulic acid (FA) from both substrates. Our findings showed a higher FAE activity in the enzymatic extracts produced on corn cob (0.070 ± 0.004 U/mL). Nevertheless, the enzymatic extracts produced on VTS demonstrated a better performance for FA release from both corn cob (2.05 ± 0.01 mg/g) and VTS (0.19 ± 0.003 mg/g). This result was probably because of the higher xylanase/FAE ratio determined in VTS extract. Therefore, an additional assay was carried out by supplementing corn cob extract with a commercial xylanase to test the influence of FAE/xylanase ratio in FA release. The results revealed the relevance of the FAE/xylanase ratio for an optimal FA release.     

Production of 2-methyl-1-butanol and 3-methyl-1-butanol in engineered Corynebacterium glutamicum

The pentanol isomers 2-methyl-1-butanol and 3-methyl-1-butanol represent commercially interesting alcohols due to their potential application as biofuels. For a sustainable microbial production of these compounds, Corynebacterium glutamicum was engineered for producing 2-methyl-1-butanol and 3-methyl-1-butanol via the Ehrlich pathway from 2-keto-3-methylvalerate and 2-ketoisocaproate, respectively. In addition to an already available 2-ketoisocaproate producer, a 2-keto-3-methylvalerate accumulating C. glutamicum strain was also constructed. For this purpose, we reduced the activity of the branched-chain amino acid transaminase in an available C. glutamicum l-isoleucine producer (K2P55) via a start codon exchange in the ilvE gene enabling accumulation of up to 3.67 g/l 2-keto-3-methylvalerate. Subsequently, nine strains expressing different gene combinations for three 2-keto acid decarboxylases and three alcohol dehydrogenases were constructed and characterized. The best strains accumulated 0.37 g/l 2-methyl-1-butanol and 2.76 g/l 3-methyl-1-butanol in defined medium within 48 h under oxygen deprivation conditions, making these strains ideal candidates for additional strain and process optimization.     

Intracellular metabolism analysis of Clostridium cellulovorans via modeling integrating proteomics,metabolomics and fermentation

A consolidated bioprocess for cellulosic n-butanol production has been developed by engineering Clostridium cellulovorans to overexpress a bifunctional aldehyde/alcohol dehydrogenase. Rational metabolic engineering is important to further improve butanol production. This study aimed to investigate intracellular metabolism and identify the key regulators of cellulosic butanol formation in C. cellulovorans via integrated Omics and fermentation kinetics data analysis. First, comparative proteomics and metabolomics analyses of wild type and n-butanol producing mutant strain were conducted, which quantified 624 host cell proteins and 474 primary and secondary metabolites. Compared to wild type, most cellulases in cellulolysis were up-regulated, but three glycolysis enzymes and three enzymes in central pathway were down-regulated in the n-butanol producing strain. Second, a dynamic model integrating Omics and fermentation data was developed to identify key regulators in butanol biosynthesis, which were ranked by further metabolic control analysis. Finally, rational metabolic engineering was performed in C. cellulovorans by overexpressing two genes (thl and hbd) identified as important factors limiting butanol biosynthesis, which improved butanol yield and C4/C2 ratio. This study demonstrated a research approach to integrate multi-Omics and fermentation data of C. cellulovorans and guide its rational metabolic engineering, which can also be applied to other microorganisms.     

A hybrid synthetic pathway for butanol production by a hyperthermophilic microbe

Biologically produced alcohols are of great current interest for renewable solvents and liquid transportation fuels. While bioethanol is now produced on a massive scale, butanol has superior fuel characteristics and an additional value as a solvent and chemical feedstock. Butanol production has been demonstrated at ambient temperatures in metabolically-engineered mesophilic organisms, but the ability to engineer a microbe for in vivo high-temperature production of commodity chemicals has several distinct advantages. These include reduced contamination risk, facilitated removal of volatile products, and a wide temperature range to modulate and balance both the engineered pathway and the host׳s metabolism. We describe a synthetic metabolic pathway assembled from genes obtained from three different sources for conversion of acetyl-CoA to 1-butanol, and 1-butanol generation from glucose was demonstrated near 70 °C in a microorganism that grows optimally near 100 °C. The module could also be used in thermophiles capable of degrading plant biomass.     

Decanter cake waste as a renewable substrate for biobutanol production by Clostridium beijerinckii

The aim of this study was to determine if decanter cake waste from a palm oil mill could be used as a renewable substrate for biobutanol production. Decanter cake waste was first hydrolyzed to fermentable sugars by nitric acid and detoxified by activated-charcoal. The detoxified hydrolysate supplemented with whey protein and ammonium sulfate as cheap nitrogen sources, was used for butanol production by growing cells of Clostridium beijerinckii. The detoxified hydrolysate was also used as a co-substrate for direct conversion of butyric acid to butanol in a nitrogen-free medium. By these two steps, C. beijerinckii produced 3.42 g/L of butanol with a yield of 0.28 C-mol butanol/C-mol carbon in the first step and produced 6.94 g/L of butanol with a yield of 0.47 C-mol butanol/C-mol carbon in the second step. This study has showed that decanter cake waste could serve as a low-cost substrate for biobutanol production.     

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.     

Inhibition of cellulases by phenols

Enzyme hydrolysis of pretreated cellulosic materials slows as the concentration of solid biomass material increases, even though the ratio of enzyme to cellulose is kept constant. This form of inhibition is distinct from substrate and product inhibition, and has been noted for lignocellulosic materials including wood, corn stover, switch grass, and corn wet cake at solids concentrations greater than 10 g/L. Identification of enzyme inhibitors and moderation of their effects is of considerable practical importance since favorable ethanol production economics require that at least 200 g/L of cellulosic substrates be used to enable monosaccharide concentrations of 100 g/L, which result in ethanol titers of 50 g/L. Below about 45 g/L ethanol, distillation becomes energy inefficient. This work confirms that the phenols: vanillin, syringaldehyde, trans-cinnamic acid, and hydroxybenzoic acid, inhibit cellulose hydrolysis in wet cake by endo- and exo-cellulases, and cellobiose hydrolysis by β-glucosidase. A ratio of 4 mg of vanillin to 1 mg protein (0.5 FPU) reduces the rate of cellulose hydrolysis by 50%. β-Glucosidases from Trichoderma reesei and Aspergillus niger are less susceptible to inhibition and require about 10× and 100× higher concentrations of phenols for the same levels of inhibition. Phenols introduced with pretreated cellulose must be removed to maximize enzyme activity.     

Characterization of a highly thermostable ß-hydroxybutyryl CoA dehydrogenase from Clostridium acetobutylicum ATCC 824

Higher energy content and hydrophobicity make bio-based n-butanol a preferred building block for chemical and biofuels manufacturing. Butanol is obtained by Clostridium sp. based ABE fermentation process. While the ABE process is well understood, the enzyme systems involved have not been elucidated in detail. The important enzyme ß-hydroxybutyryl CoA dehydrogenase from Clostridium acetobutylicum ATCC 824 (Hbd) was purified and characterized. Surprisingly, Hbd shows extremely high temperature (T > 60 °C), pH (4–11) and solvent (1-butanol, isobutanol, ethanol) stability. Hbd catalyzes acetoacetyl CoA hydration to ß-hydroxybutyryl CoA up to pH 9.5, where the reaction is reversed. Substrate (acacCoA, ß-hbCoA) and cofactor (NADH, NAD⁺, NADPH and NADP⁺) specificities were determined. We identified NAD⁺ as an uncompetitive inhibitor. Identification of process relevant enzymes such as Hbd is key to optimize butanol production via cellular or cell-free enzymatic systems.     

Novozym 435-catalyzed 1,3-diacylglycerol preparation via esterification in t-butanol system

1,3-Diacylglycerol (1,3-DAG) oil has beneficial effects on suppressing the accumulation of body fat and preventing the increase of body weight. So, more and more attention has been paid to enzyme-mediated 1,3-DAG production in recent years due to its mild reaction condition and safe products. In this work, t-butanol was adopted as the reaction medium for lipase-catalyzed esterification for 1,3-DAG preparation. In t-butanol system, the harmful effects on lipase caused by glycerol could be eliminated completely, so the high enzymatic activity was maintained and the stability of the lipase could be improved significantly. Under the optimum conditions (60 °C, 1.00 g Novozym 435, 2.5:1 molar ratio of oleic acid to glycerol (10.0 g oleic acid and 1.3 g glycerol) and 6.0 g t-butanol), 1,3-DAG concentration of 40% was achieved and Novozym 435 can be used 100 times. A simplified model based on Ping-Pong Bi-Bi with substrate competitive inhibition by glycerol was found to fit the initial rate data and the kinetics parameters were evaluated by nonlinear regression analysis.     

Evaluating agro-industrial by-products as dietary roughage source on growth performance of fattening steers

Silages from pineapple peel, sweet corn husk and cob mixed with bagasse and vinasse were evaluated to determine their chemical composition and fermentation characteristics as well as feeding performance in fattening steers. The experiment, which lasted 90 days, involved 48 fattening steers (264 ± 37.4 kg BW) randomly allocated to three diets. Treatments included: a control diet containing rice straw and molasses (T1); diet containing bagasse–vinasse mixture including sweet corn husk and cob silage (BS; T2); and diet containing bagasse–vinasse mixture including pineapple peel silage (BP; T3). All treatments included a commercial concentrate feed (13% CP) and ad libitum rice straw throughout the experiment. Results from chemical analysis showed that dry matter (DM) of BS was higher than BP (P < 0.05), whereas the protein content of BS and BP was similar (P > 0.05). For fermentation characteristics, pH in BP was lower than BS (P < 0.05); in addition, acetic and butyric acids in BS were higher than BP (P < 0.05). Findings from growth trial showed that total DM intake in steers fed T1 was higher compared to the other dietary treatments (P < 0.05), whereas the average BW gain was found to be grater in T3 steers (P < 0.05). As result from our findings, bagasse–vinasse mixture with pineapple peel silage appeared to be a viable feed ingredient in fattening steer diet and moreover it could become an economically feasible agro-industrial by-product for farmers.     

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.     

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.     

Vanillin bioproduction from alkaline hydrolyzate of corn cob by Escherichia coli JM109/pBB1

Hydrolysis of corn cob performed for 6 h with 0.5 N NaOH at solid/liquid ratio of 0.084 g/g allowed obtaining a hydrolyzate containing 1171 ± 34 mg/l ferulic acid and 2156 ± 63 mg/l p-coumaric acid that was used as a medium for vanillin bioproduction by the engineered strain Escherichia coli JM109/pBB1. Aiming at maximizing vanillin bioproduction, the effects of medium heat sterilization, one-stage or two-stage pre-cultivation, adaptation of the microorganism to the hydrolyzate and inoculum biomass level were investigated. Biomass pre-cultivated once in unsterilized hydrolyzate was able to effectively convert ferulic and p-coumaric acids to a mixture of vanillin, vanillic acid and vanillyl alcohol provided with the typical vanilla flavor. At initial biomass concentration of 0.5 g_DM/l, maximum values of vanillin concentration (239 ± 15 mg/l), vanillin yield on consumed ferulic acid (0.66 ± 0.03 mol/mol) and vanillin volumetric productivity (10.9 ± 0.7 mg/lh) were obtained after 22 h.     

Fast biodegradation of long chain n-alkanes and crude oil at high concentrations with Rhodococcus sp. Moj-3449

Biodegradation of long chain n-alkanes and crude oil with fast rate and high concentration are desirable for bioremediation, especially in heavily oil-polluted areas, and enhanced oil recovery. We discovered Rhodococcus sp. Moj-3449 with such unique abilities by screening microorganisms for the growth on n-hexadecane at 30 mg/mL. The new strain grew very fast on 120 mg/mL of n-hexadecane giving a cell density of 14.7 g cdw/L after only 2 days’ incubation. During the growth with this strain, the oil–water phases were rapidly emulsified, giving rise to tolerance to high alkane concentration (250 mg/mL) and fast growth rate of 0.10–0.20 h^?1 for alkane concentration of 1–180 mg/mL. The degraded concentration of n-hexadecane increased linearly with the initial alkane concentration (1–250 mg/mL). Incubation on n-hexadecane at 250 mg/mL for 7 days gave a cell density of 13.5 g cdw/L and degraded 124 mg/mL of n-hexadecane. The strain grew also fast on n-dodecane (C12), n-tetradecane (C14), and n-octadecane (C18), with degradation preference of C14 (=C16) > C12 > C18. Different from many alkane-degrading strains, Rhodococcus sp. Moj-3449 was found to have subterminal oxidation pathway. Rhodococcus sp. Moj-3449 degraded also crude oil fast at 60–250 mg/mL, with a wide range of n-alkanes (C10–C35) as substrates in which C14–C19 are preferred. The degradation ability increased with initial oil concentration from 60 to 150 mg/mL and slightly decreased afterwards. Incubation on 150 mg/mL of crude oil for 7 days degraded 37% of n-alkanes. The outstanding ability of rapidly degrading long chain n-alkanes and crude oil at high concentration makes Rhodococcus sp. Moj-3449 potentially useful for bioremediation and microbial enhanced oil recovery.     

The production of a cold-induced extracellular biopolymer by Pseudomonas fluorescens BM07 under various growth conditions and its role in heavy metals absorption

The psychrotrophic bacterium Pseudomonas fluorescens BM07 was induced to excrete an extracellular biopolymer when cells were grown aerobically at 10 °C and its secretion was inhibited at 30 °C. The biopolymer was easily torn apart from the cells by using a shear force under centrifugation (8700 × g, 30 min) and collected as a well-separated mucoid layer in centrifuge tube. The production of the biopolymer was affected by factors such as the types of carbon and nitrogen sources, temperature, and pH. The best production of 2.5 g/l was obtained when the cells were grown on M1 medium containing 70 mM sucrose and 0.2% (w/v) Casamino Acids. In Kings B enriched medium a maximum biopolymer production of up to 3.4 g/l and growth rate of 2.1 g/l, were achieved using 1:1 ratio of C/N. Addition of NaCl and ethanol to the medium led to a decrease in biopolymer production and growth rate of BM07 strain. FT-IR spectroscopy demonstrated the presence of carboxyl, amine, hydroxyl and methoxyl functional groups in the biopolymer. BM07 biopolymer showed high ion binding capacity with particular preference to uptake cadmium and mercury (∼45 and 70%, respectively). The percentage removal of cobalt, zinc, nickel and copper cations were between 20 and 30%. Overall ion uptake by BM07 biopolymer showed a definite preference for larger over smaller cations (Hg > Cd > Ni > Zn > Cu > Co).     

Culture parameters affecting xylitol production by Debaryomyces hansenii immobilized in alginate beads

Yeast immobilization offers operational advantages such as high cell concentration, and some drawbacks related to cell leaking and restricted mass transfer inside particles. The influence of bead size, chitosan, bead charge, volume of liquid media, and the use of corncob hydrolyzates and vinasses as culture medium were analyzed on xylitol production by Debaryomyces hansenii immobilized in alginate beads. The results showed a profuse growth of free cells, accounting 75–95% of total biomass, but electron micrographs revealed the generation of a dense biofilm with hyphal morphology at the bead surface and a very low intraparticular growth. Xylitol production was not affected by the size of particle; however chitosan had a negative effect. The use of corn cob as carbon source and twofold diluted vinasses as economic nutrients incremented xylitol concentration to 13.7 g L^?1 (Y_P/S = 0.56 g g^?1; Q_P = 0.29 g L^?1 h^?1). The best conditions corresponded to high bead charges and intermediate liquid volumes (44 g Na-alginate and 110 mL liquid medium). These results showed the feasibility of employing these cheap substrates, reflected the importance of the microaerobical conditions, and pointed to the favorable effect of cell immobilization on the metabolism of xylitol production.     

Continuous 2-keto-gluconic acid (2KGA) production from corn starch hydrolysate by Pseudomonas fluorescens AR4

A continuous fermentation process for 2-keto-gluconic acid (2KGA) production from cheap raw material corn starch hydrolysate was developed using the strain Pseudomonas fluorescens AR4. The dilution rate and feeding glucose concentration had a significant effect on the cell concentrations, glucose utilization and 2KGA production performance. The optimal operating factors were obtained as: 0.065 h⁻¹ of dilution rate, 180 g/L of feeding glucose concentration, and 16 h of batch fermentation time as the starting point. Under these conditions, the steady state had the 135.92 g/L of produced 2KGA concentration, 8.83 g/L.h of average volumetric productivity, and 0.9510 g/g of yield. In conclusion, the proposed efficient and stable continuous fermentation process for 2KGA production by the strain P. fluorescens AR4 is potentially competitive for industrial production from corn starch hydrolysate in terms of 2KGA productivity and yield.     

Variation in polyphenolic profile and in vitro antioxidant activity of eastern teaberry (Gaultheria procumbens L.) leaves following foliar development

Seasonal dynamics in the polyphenolic composition, antioxidant activity, and their relationships during plant development were evaluated for eastern teaberry (Gaultheria procumbens L.) leaves, a traditional herbal medicine of North American natives. With the complementary UHPLC-PDA-ESI-MS³, HPLC-PDA-fingerprint, Folin-Ciocalteau, and n-butanol/HCl assays of methanol-water (75:25, v/v) extracts, the dried leaf samples harvested monthly across the growing season under Polish climate conditions were found rich in structurally diverse polyphenols (149.2–210.7 mg/g DW) including the dominating salicylates (64.6–107.5 mg/g DW), proanthocyanidins (53.0–66.8 mg/g DW), and flavonoids (17.3–25.3 mg/g DW), and the accompanying chlorogenic acid isomers (2.4–4.4 mg/g DW) and simple phenolic acids (0.9–1.1 mg/g DW). Among 28 detected analytes, gaultherin (64.6–107.5 mg/g DW), miquelianin (14.6–21.1 mg/g DW), procyanidin A-type trimer (5.5–9.5 mg/g DW), and (–)-epicatechin (5.8–7.8 mg/g DW) were the most abundant. The phenolic levels and antioxidant activity parameters in the DPPH (EC₅₀, 15.0–18.2 μg DW/mL; 0.95–1.16 mmol Trolox equivalents/g DW) and FRAP (2.3–3.4 mmol Fe ²⁺/g DW; 0.86–1.26 mmol Trolox equivalents/g DW) assays showed parallel seasonal trends with maxima in September and October. As the subsequent correlation studies confirmed the determinative impact of polyphenols on the leaf antioxidant activity and its seasonal fluctuations, the Fall season could be recommended as optimal for harvesting the plant material for medicinal purposes and cost-effective production of natural health products.