Separation of targeted ganoderic acids from Ganoderma lucidum by reversed phase liquid chromatography with ultraviolet and mass spectrometry detections

Ganoderic acids are valuable bioactive secondary metabolites produced by a traditional medicinal mushroom Ganoderma lucidum (“Ling-zhi” in Chinese and “Reishi” in Japanese). In this work, a fast and efficient method for the recovery and purification of ganoderic acid T (GA-T) and ganoderic acid Me (GA-Me) from triterpene-enriched extracts of G. lucidum mycelia was developed by using reversed phase HPLC (RP-HPLC) on a C₁₈ column with an acidified methanol–water mobile phase in combination with ultraviolet (UV) detection and electrospray ionization mass spectrometry (ESI-MS). The presence of each targeted GA (GA-T and GA-Me) in its corresponding peak was easily identified and confirmed by UV and MS. The chemical structures of the purified GA-T and GA-Me were further confirmed by ¹H NMR. The retention behaviors of the two GAs over a temperature range of 15–55 °C were also investigated. From the retention time data, van’t Hoff plots were obtained. The estimated enthalpy (ΔH) and entropy (ΔS) data suggest that the retention time difference between GA-T and GA-Me might be driven by an enthalpy difference. Furthermore, a semi-preparative HPLC purification was achieved on a semi-preparative C₁₈ column using the conditions optimized for the analytical column. The method presented in this work can be a valuable tool for the rapid semi-preparative purification of targeted GAs, and it may also be applicable to some other natural products.     

Stimulatory effects of Coix lacryma-jobi oil on the mycelial growth and metabolites biosynthesis by the submerged culture of Ganoderma lucidum

Effects of Coix lacryma-jobi oil (CLO) addition on the mycelia growth and production of bioactive metabolites, such as triterpenoids, exopolysaccharide (EPS), and intracellular polysaccharide (IPS) in the submerged culture of Ganoderma lucidum were studied. The results showed that when a level of 2% CLO was added at the beginning of culture, the biomass, triterpenoids, EPS, and IPS productions reached a maximum of 10.71 g/L, 92.94 mg/L, 0.33 g/L, and 0.389 g/L, respectively, that were 3.34-fold, 2.76-fold, 2.2-fold, and 2.23-fold compared to that of control. Analysis of fermentation kinetics of G. lucidum suggested that glucose concentration in the culture of CLO-added group decreased more quickly as compared to the control group from day 2 to day 7 of fermentation process, while the triterpenoids and polysaccharides biosynthesis were promoted at the same culture period. However, the culture pH profile was not affected by the addition of CLO. There were no new components in the two types of polysaccharides obtained by the addition of CLO. Enzyme activities analysis indicated CLO or its fatty acids affected the synthesis level of phosphoglucose isomerase and α-phosphoglucomutase at different stage.     

Novel hypoglycemic effects of Ganoderma lucidum water-extract in obese/diabetic (+db/+db) mice

In this study, we evaluated the pharmacological effects of Ganoderma lucidum (G. lucidum) (water-extract) (0.003, 0.03 and 0.3 g/kg, 4-week oral gavage) consumption using the lean (+db/+m) and the obese/diabetic (+db/+db) mice. Different physiological parameters (plasma glucose and insulin levels, lipoproteins-cholesterol levels, phosphoenolpyruvate carboxykinase (PEPCK), 3-hydroxy-3-methylglutaryl coenzyme A reductase (HMG CoA reductase) and isolated aorta relaxation of both species were measured and compared. G. lucidum (0.03 and 0.3 g/kg) lowered the serum glucose level in +db/+db mice after the first week of treatment whereas a reduction was observed in +db/+m mice only fed with 0.3 g/kg of G. lucidum at the fourth week. A higher hepatic PEPCK gene expression was found in +db/+db mice. G. lucidum (0.03 and 0.3 g/kg) markedly reduced the PEPCK expression in +db/+db mice whereas the expression of PEPCK was attenuated in +db/+m mice (0.3 g/kg G. lucidum). HMG CoA reductase protein expression (in both hepatic and extra-hepatic organs) and the serum insulin level were not altered by G. lucidum. These data demonstrate that G. lucidum consumption can provide beneficial effects in treating type 2 diabetes mellitus (T2DM) by lowering the serum glucose levels through the suppression of the hepatic PEPCK gene expression.     

Functional and structural analyses of a 1,4-β-endoglucanase from Ganoderma lucidum

Ganoderma lucidum is a saprotrophic white-rot fungus which contains a rich set of cellulolytic enzymes. Here, we screened an array of potential 1,4-β-endoglucanases from G. lucidum based on the gene annotation library and found that one candidate gene, GlCel5A, exhibits CMC-hydrolyzing activity. The recombinant GlCel5A protein expressed in Pichia pastoris is able to hydrolyze CMC and β-glucan but not xylan and mannan. The enzyme exhibits optimal activity at 60 °C and pH 3–4, and retained 50% activity at 80 and 90 °C for at least 15 and 10 min. The crystal structure of GlCel5A and its complex with cellobiose, solved at 2.7 and 2.86 Å resolution, shows a classical (β/α)₈ TIM-barrel fold as seen in other members of glycoside hydrolase family 5. The complex structure contains a cellobiose molecule in the +1 and +2 subsites, and reveals the interactions with the positive sites of the enzyme. Collectively, the present work provides the first comprehensive characterization of an endoglucanase from G. lucidum that possesses properties for industrial applications, and strongly encourages further studying in the cellulolytic enzyme system of G. lucidum.     

Use of lignocellulosic wastes of pecan (Carya illinoinensis) in the cultivation of Ganoderma lucidum

Background

The wastes of pecan nut (Carya illinoinensis (Wangenh.) K. Koch) production are increasing worldwide and have high concentrations of tannins and phenols.

Estimating the contribution of N-sulfocarbamoyl paralytic shellfish toxin analogs GTX6 and C3 + 4 to the toxicity of mussels (Mytilus galloprovincialis) over a bloom of Gymnodinium catenatum

Gymnodinium catenatum, a dinoflagellate species with a global distribution, is known to produce paralytic shellfish poisoning (PSP) toxins. The profile of toxins of G. catenatum is commonly dominated by sulfocarbamoyl analogs including the C3 + 4 and GTX6, which to date has no commercial certified reference materials necessary for their quantification via chemical methods, such as liquid chromatography. The aim of this study was to assess the presence of C3 + 4 and GTX6 and their contribution to shellfish toxicity. C3 + 4 and GTX6 were indirectly quantified via pre-column oxidation liquid chromatography with fluorescence detection after hydrolysis conversion into their carbamate analogs. Analyses were carried out in mussel samples collected over a bloom of G. catenatum (>63 × 10³ cells l⁻¹) in Aveiro lagoon, NW Portuguese coast. Concentration levels of sulfocarbamoyl toxin analogs were two orders of magnitude higher than decarbamoyl toxins, which were in turn one order of magnitude higher than carbamoyl toxins. Among the sulfocarbamoyl toxins, C1 + 2 were clearly the dominant compounds, followed by C3 + 4 and GTX6. The least abundant sulfocarbamoyl toxin was GTX5. The most important compounds in terms of contribution for sample toxicity were C1 + 2, which justified 26% of the PSP toxicity. The lesser abundant dcSTX constitutes the second most important compound with similar % of toxicity to C1 + 2, C3 + 4 and GTX6 were responsible for approximately 11% and 13%, respectively. The median of the sum of C3 + 4 and GTX6 was 27%. These levels reached a maximum of 60% as was determined for the sample collected closest to the G. catenatum bloom. This study highlights the importance of these low potency PSP toxin analogs to shellfish toxicity. Hydrolysis conversion of C3 + 4 and GTX6 is recommended for determination of PSP toxicity when LC detection methods are used for PSP testing in samples exposed to G. catenatum.     

Multi-fed batch culture integrated with three-stage light irradiation and multiple additions of copper ions for the hyperproduction of ganoderic acid and Ganoderma polysaccharides by the medicinal mushroom Ganoderma lucidum

To further enhance the accumulation of the bioactive metabolite ganoderic acid (GA) by fermentation of the medicinal mushroom Ganoderma lucidum, a novel integrated strategy was developed by simultaneously adopting a strategy of multiple Cu²⁺ additions, three-stage light irradiation and multi-pulse feeding of carbon and nitrogen sources. Maximal GA content (i.e., 4.1 mg/100 mg DW) and production (i.e., 720.8 mg/L) were obtained using the novel integrated strategy. Not only the biomass but also the total GA production obtained in this work is the highest reported for a shaker flask culture of G. lucidum. This work is useful for the large-scale production of GA by G. lucidum fermentation.     

Enzymatic hydrolysis of corncob and ethanol production from cellulosic hydrolysate

 Enzymatic hydrolysis of corncob and ethanol fermentation from cellulosic hydrolysate were investigated. After corncob was pretreated by 1% H₂SO₄ at 108 °C for 3 h, the cellulosic residue was hydrolyzed by cellulase from Trichoderma reesei ZU-02 and the hydrolysis yield was 67.5%. Poor cellobiase activity in T. reesei cellulase restricted the conversion of cellobiose to glucose, and the accumulation of cellobiose caused severe feedback inhibition to the activities of β-1,4-endoglucanase and β-1,4-exoglucanase in cellulase system. Supplementing cellobiase from Aspergillus niger ZU-07 greatly reduced the inhibitory effect caused by cellobiose, and the hydrolysis yield was improved to 83.9% with enhanced cellobiase activity of 6.5 CBU g⁻¹ substrate. Fed-batch hydrolysis process was started with a batch hydrolysis containing 100 g l⁻¹ substrate, with cellulosic residue added at 6 and 12 h twice to get a final substrate concentration of 200 g l⁻¹. After 60 h of reaction, the reducing sugar concentration reached 116.3 g l⁻¹ with a hydrolysis yield of 79.5%. Further fermentation of cellulosic hydrolysate containing 95.3 g l⁻¹ glucose was performed using Saccharomyces cerevisiae 316, and 45.7 g l⁻¹ ethanol was obtained within 18 h. The research results are meaningful in fuel ethanol production from agricultural residue instead of grain starch.     

Performance analyses of a pH-shift and DOT-shift integrated fed-batch fermentation process for the production of ganoderic acid and Ganoderma polysaccharides by medicinal mushroom Ganoderma lucidum

Investigations on Ganoderma lucidum fermentation suggested that the responses of the cell growth and metabolites biosynthesis to pH and dissolved oxygen tension (DOT) were different. The ganoderic acid (GA) production of 321.6 mg/L was obtained in the pH-shift culture by combining a 4-day culture at pH 3.0 with the following 6-day culture at pH 4.5, which was higher by 45% and 300% compared with the culture at pH 3.0 and 4.5, respectively. The GA production of 487.1 mg/L was achieved in the DOT-shift culture by combining a 6-day culture at 25% of DOT with a following 6-day culture at 10% of DOT, which was higher by 43% and 230% compared with the culture at 25% and 10% of DOT, respectively. A fed-batch fermentation process by combining the above-mentioned pH-shift and DOT-shift strategies resulted in a significant synergistic enhancement of GA accumulation up to 754.6 mg/L, which is the highest reported in the submerged fermentation of G. lucidum in stirred-tank bioreactor.     

Enzymatic synthesis of β-N-(γ-l(+)-glutamyl)-4-carboxyphenylhydrazine with Escherichia coli γ-glutamyltransferase

A new method for the synthesis of β-N-(γ-l(+)-glutamyl)-4-carboxyphenylhydrazine, a precursor of agaritine, is presented. This compound was prepared from l-glutamine and 4-hydrazinobenzoic acid through the transpeptidation reaction catalyzed by the Escherichia coli γ-glutamyltransferase. The optimum reaction conditions for the production of β-N-(γ-l(+)-glutamyl)-4-carboxyphenylhydrazine were 50 mM l-glutamine, 500 mM 4-hydrazinobenzoic acid and 40 U γ-glutamyltransferase/mL at pH 8 and 37 °C for 24 h. The product was obtained with a conversion rate of 90% (mol/mol). γ-Glutamyltransferase activity was not inhibited by 4-hydrazinobenzoic acid at concentrations up to 1000 mM. This simple and efficient method would facilitate the synthesis of glutamyl phenylhydrazine analogs, including agaritine.     

Glucoamylase production by the marine yeast Aureobasidium pullulans N13d and hydrolysis of potato starch granules by the enzyme

Under the optimal conditions, 10 U/ml of glucoamylase was produced by the marine yeast Aureobasidium pullulans N13d. It was noticed that the crude glucoamylase actively hydrolyzed potato starch granules, but poorly digested raw corn starch and sweet potato starch, resulting in conversion of 68.5, 19 and 22% of them into glucose within 6 h of incubation in the presence of 40 g/l of potato starch granules and 20 U/ml of the crude enzyme. When potato starch granules concentration was increased from 10 to 80 g/l, hydrolysis extent was decreased from 85.6 to 60%, while potato starch granules concentration was increased from 80 to 360 g/l, hydrolysis extent was decreased from 60 to 56%. Ratio of hydrolysis extent of potato starch granules to hydrolysis extent of gelatinized potato starch was 86.0% and the hydrolysis extent of potato starch granules by action of the crude glucoamylase (1.0 U/ml) was 18.5% within 30 min at 60 °C. Only glucose was detected during the hydrolysis, indicating that the crude enzyme could hydrolyze both α-1,4 and α-1,6 linkages of starch molecule in the potato starch.     

Triterpenoid biosynthesis and the transcriptional response elicited by nitric oxide in submerged fermenting Ganoderma lucidum

Ganoderic triterpenoid (GT) is a promising anti-tumour constituent in Ganoderma lucidum. The aim of this study was to investigate induction by and a possible signalling mechanism of nitric oxide (NO) for GT synthesis. Compared to the control, the biomass decreased by 43.5% at 120 h and the GT yield increased by 40.94% at 72 h in the presence of a 5 mM NO donor sodium nitroprusside supplement. The gene expression profiles of G. lucidum in response to NO were investigated by RNA-sequencing. Functional annotation and an enrichment analysis of the differentially expressed genes indicated that NO inhibited mycelial growth probably via the suppression of the glycolysis genes involved in carbohydrate metabolism. NO may function directly as a regulator of gene expression in the mevalonate pathway to induce GT biosynthesis, and the hyper-production of GT in response to NO could also be accomplished by a signalling function involving Ca²⁺ and a reactive oxygen species (ROS) pathway. The results of this study are useful for large-scale GT production and can facilitate further studies on the endogenous signalling pathways involved in the GT biosynthetic pathway.     

Challenges in enzymatic hydrolysis and fermentation of pretreated Arundo donax revealed by a comparison between SHF and SSF

The perennial herbaceous crop Arundo donax is a potential feedstock for second-generation bioethanol production. In the present work, two different process options were investigated for the conversion of two differently steam-pretreated batches of A. donax. The pretreated raw material was converted to ethanol with a xylose-consuming Saccharomyces cerevisiae strain, VTT C-10880, by applying either separate hydrolysis and fermentation (SHF) or simultaneous saccharification and fermentation (SSF). The highest overall ethanol yield and final ethanol concentration were achieved using SHF (0.27 g g^?1 and 20.6 g L^?1 compared to 0.24 g g^?1 and 19.0 g L^?1 when SSF was used). The performance of both SHF and SSF was improved by complementing the cellulolytic enzymes with hemicellulases. The higher amount of acetic acid in one of the batches was shown to strongly affect xylose consumption in the fermentation. Only half of the xylose was consumed when batch 1 (high acetic acid) was fermented, compared to that 94% of the xylose was consumed in fermentation of batch 2 (lower acetic acid). Furthermore, the high amount of xylooligomers present in the pretreated materials considerably inhibited the enzymatic hydrolysis. Both the formation of xylooligomers and acetic acid thus need to be considered in the pretreatment process in order to achieve efficient conversion of A. donax to ethanol.     

Optimization and modeling of lactose hydrolysis in a packed bed system using immobilized β-galactosidase from Aspergillus oryzae

This work studied the hydrolysis of lactose using β-galactosidase from Aspergillus oryzae immobilized with a combination of adsorption and glutaraldehyde cross-linking onto the ion exchange resin Duolite A568 as a carrier. A central composite design (CCD) was used to study the effects of lactose concentration and feed flow rate on the average hydrolysis reaction rate and lactose conversion in a fixed bed reactor operating continuously with an upflow at a temperature of 35 ± 1 °C. The optimal conditions for the average hydrolysis reaction rate and the lactose conversion included a lactose concentration of 50 g/L and a feed flow rate of 6 mL/min. The average reaction rate and conversion reached 2074 U and 65%, respectively. The immobilized enzyme activity was maintained during the 30 days of operation in a fixed bed reactor with a 0.3 mL/min feed flow rate of a 50 g/L lactose solution at room temperature. Feed flows ranging from 0.6 to 12 mL/min were used to determine the distribution of residence times and the kinetics of the fixed bed reactor. A non-ideal flow pattern with the formation of a bypass flow in the fixed bed reactor was identified. The conditions used for the kinetics study included a lactose solution concentration of 50 g/L at pH 4.5 and a temperature of 35 ± 1 °C. Kinetic models using a PFR and axial dispersion methods were used to describe the lactose hydrolysis in the fixed bed reactor, thus accounting for the competitive inhibition by galactose. To increase the lactose conversion, experiments were performed for two fixed bed reactors in series, operating in continuous duty with upflow, with the optimal conditions determined using the CCD for a fixed bed reactor. The total conversion for the two reactors in series was 82%.     

Effect of chaotropes in reverse micellar extraction of kallikrein

Reverse micellar extraction is a promising technique in large-scale bioseparation. However, low recovery and high salt concentration in back extraction limit its application. In CTAB/n-octane/n-hexanol reverse micellar system, the enzyme, pancreatic kallikrein could be effectively enwrapped into reverse micelles in forward extraction, but was difficult to be released during back extraction. In this study, dilute chaotropes (urea and GuHCl) were introduced to enhance the release of enzyme instead of high salts in back extraction. Kallikrein enwrapped in reverse micelles was released effectively in the presence of dilute urea and GuHCl during back extraction. Nearly 100% activity recovery of kallikrein from commercial product was obtained by adding 0.60 M urea, and for kallikrein from crude material, the recovery increased greatly by adding 0.80 M urea and 0.08 M GuHCl in the stripping solution. The mechanism of chaotrope for enhancing the release of enzyme from micelles was explored and dynamic light scatter analysis showed that the chaotrope would influence the sizes of micelles during reverse micellar extraction.     

Efficient preparation of enantiopure l-tert-leucine through immobilized penicillin G acylase catalyzed kinetic resolution in aqueous medium

Racemic _DL-tert-leucine (_DL-Tle) was resolved to obtain enantiopure _L-Tle through enantioselective hydrolysis of its N-phenylacetyl derivative with immobilized penicillin G acylase (PGA). The effects of pH, reaction temperature, substrate concentration and reaction time on the reaction were investigated. The reaction was conveniently carried out at 0.4 M substrate concentration in water at pH 8.0 and 30 °C. Under the optimized reaction conditions, _L-Tle was obtained in an enantiopure form (>99% ee) with 45.8% substrate conversion after 4 h. The thermal stability and operational stability of immobilized PGA were examined. Furthermore, the preparation of _L-Tle was successfully performed in a recirculating packed bed reactor (RPBR) system and immobilized PGA exhibited a long-term stability for 51 days with a slight decrease of activity. The isolated _D-enantiomer was racemized at 160 °C for 15 min and reused as substrate. The results obtained clearly demonstrated a potential for industrial application of immobilized PGA in the preparation of _L-Tle through enantioselective hydrolysis of its N-phenylacetyl derivative.     

Immobilized β-glucosidase on magnetic chitosan microspheres for hydrolysis of straw cellulose

β-Glucosidase immobilized on magnetic chitosan microspheres for potential recycling usage in hydrolysis of cellulosic biomass was investigated. The immobilized enzyme had an activity of 6.4 U/g support under optimized condition when using cellobiose as substrate. Immobilization resulted in less increase of the apparent K_m, low drift of the optimal pH, as well as improved stability relative to the free enzyme. The immobilized β-glucosidase was applied to enzymatic hydrolysis of corn straw to produce 60.2 g/l reducing sugar with a conversion rate of 78.2% over the course of a 32-h reaction. This conversion rate was maintained above 76.5% after recycling the enzyme for use in eight batches (total 256 h), showing favorable operational stability of the immobilized enzyme.     

High-loading oil palm empty fruit bunch saccharification using cellulases from Trichoderma koningii MF6

Strain Trichoderma koningii D-64 was improved for enhanced cellulase production. A potential mutant MF6 was obtained and its enzymes contained filter paper cellulase (FPase), carboxymethylcellulase (CMCase), β-glucosidase and xylanase with respective activities of 2.0, 1.3, 2.0 and 3.0 folds of those for the parental strain. MF6 cellulases showed enhanced hydrolysis performance for the treated lignocellulosic biomass. Hydrolysis of treated oil palm empty fruit bunch (OPEFB), horticulture wastes (HW) and wood chips (WC) resulted in cellulose to glucose conversion of 96.3 ± 2.2%, 98.2 ± 3.0% and 81.9 ± 1.4%, respectively. The corresponding conversions of xylan to xylose were 96.9 ± 1.5%, 95.0 ± 2.2% and 76.1 ± 3.1%. Consistently, high sugar yield of 770–844 mg/g biomass was obtained for high-loading (10–16%, w/v) of OPEFB hydrolysis and sugar titer of 135.1 g/L was obtained for 16% (w/v) OPEFB loading at 96 h. In addition, MF6 enzymes alone performed equally well for high-loading OPEFB hydrolysis compared to the enzyme mixture of β-glucosidase from Aspergillus niger and cellulase from T. reesei Rut C30.     

Enzyme-assisted extraction of fucoxanthin and lipids containing polyunsaturated fatty acids from Undaria pinnatifida using dimethyl ether and ethanol

A novel method for the efficient extraction of fucoxanthin and lipids containing polyunsaturated fatty acids (PUFAs) from the brown seaweed Undaria pinnatifida was developed and demonstrated at a laboratory scale. U. pinnatifida, also known as Wakame, contains a number of biologically active lipophilic compounds, particularly fucoxanthin, which has anti-oxidant, anti-cancer, anti-obesity and anti-inflammatory properties. The yield of fucoxanthin and lipids containing PUFAs was determined by extraction from wet and freeze-dried seaweed using dimethyl ether (DME) and ethanol and from enzyme-pretreated seaweed using the same solvents. The highest yields of fucoxanthin (94%) and lipids (94%) rich in PUFAs were obtained from fresh (wet) U. pinnatifida by enzyme pre-processing, followed by extraction using DME with ethanol as a co-solvent. In comparison, ethanol extraction resulted in lower extraction yields for both fucoxanthin (86%) and lipids (73%) under the conditions described. Enzyme pre-processing using alginate lyase resulted in the hydrolysis of cell wall polysaccharides, resulting in high extraction yields. The hydrolysis time, pH and temperature were found to be the most important parameters for the enzyme pre-processing step and for minimizing fucoxanthin losses due to oxidative degradation. The removal of water-soluble compounds (polysaccharides) following the enzyme pre-treatment prior to DME extractions doubled the throughput and maximized the yield. The residual biomass was colorless or a pale-brown color after the DME extraction, which indicated the highly effective extraction of fucoxanthin. The PUFA content and fucoxanthin levels were not affected by the enzyme or extraction using the described enzyme-assisted DME + ethanol co-solvent process.