Sonoporation of Ganoderma lucidum Mycelium for High Biomass and Exopolysaccharide Productivity in Submerged Culture.
Ganoderma lucidum, known as Lingzhi in China and Reishi in Japan, is a famous medicinal mushroom that is commonly produced by solid-state fermentation. Recently, submerged culture has been considered as a promising alternative for production of G. lucidum. Herein, to provide a theoretical base for preparation of a homogenous inoculum for G. lucidum submerged culture we investigated the effect of sonoporation on G. lucidum mycelium. Submerged culture was also evaluated using the sonoporated mycelium. Microscopic investigation indicated that the mycelial pellets (0.55 g, dry weight) contained in 60 mL solution were almost completely disappeared within 20 s by sonoporation (20 kHz and 125 w). The homogenate obtained after sonoporation had a 3.75x106 cfu/mL cell concentration. The sonoporation caused rapid leakage of intracellular protein that increased linearly with time. The metabolic activity of the cells decreased rapidly after sonoporation.
Sonoporation also negatively affected laccase activity. When the homogenate was used at 4.76% (v/v) inoculum level, the cultures produced biomass and exopolysaccharide of 15.75 and 0.54 g/L, respectively; these values were 129.26 and 45.95% higher than that of the control culture using a pellet-type inoculum without sonoporation. Optimal inoculum size was 5.88-6.97% (v/v). We conclude that sonoporation is an effective method for homogenization of G. lucidum mycelium, and sonoporated mycelium can improve productivity significantly in G. lucidum submerged culture and requires lower levels of starting inoculum.
Keywords: Ganoderma lucidum; Sonoporation; Homogenous inoculum; Submerged culture; Polysaccharide
Ganoderma lucidum (Fr.) Karst is a species of basidiomycetes that belongs to polyporacceae (or Ganodermaceae) of Aphyllophorales. Its fan-like fruiting bodies with wood texture is commonly called "Lingzhi" in Chinese and "Reishi" in Japanese. For centuries in the Far East, the fruiting body of G. lucidum was regarded as a popular folk medicine for treating various human diseases, such as hepatitis, arthritis, nephritis, bronchitis, asthma, arteriosclerosis, hypertension, hypercholesterolemia, and gastric cancer (Jong and Birmingham, 1992; Paterson, 2006). The molecular mechanisms underlying the health and medical benefits of G. lucidum have been investigated extensively (Sone et al., 1985; Kimura et al., 2002; Chien et al., 2004). The major active components of G. lucidum include it's polysaccharide and ganoderic acid (Xu et al., 2010).
As the beneficial effect of G. lucidum on human health has been well-recognized, its demand is increasing rapidly in Asian countries, including China, Korea, Japan, and Thailand. However, G. lucidum occurs rarely in nature and hence, sufficient amounts of wild mushrooms cannot be collected for commercial exploitation. To meet the great demand for G. lucidum, artificial cultivation on solid substrates such as lignocellulosic materials, especially sawdust, supplemented with wheat or rice bran has been developed over the past several decades (Berovic et al., 2003), and is now a major method for producing G. lucidum products. However, the solid-state bioprocess has several significant disadvantages, including the requirement of a long production cycle and the continuous fluctuation of product quality (Tang and Zhong, 2002).
In recent years, submerged culture, a microbial bioprocess commonly used for producing various primary and secondary metabolites, has been utilized to cultivate higher basidiomycetes mushrooms for the production of biomass and various bioactive substances (Lee et al., 2003; Shih et al., 2006). The significant advantages of submerged culture over solid-state fermentation include shorter production period, lower production cost and easy regulation of environmental parameters (Bae et al., 2000; Chang et al., 2006). Consequently, submerged culture of G. lucidum as a promising alternative to solid-state fermentation has received special attention for the production of its biomass and bioactive substances (Xu et al., 2008; Zhang and Zhong, 2013).
As G. lucidum mainly grows in the form of mycelial pellets in liquid culture, its homogenization becomes essential before its inoculation into the fermentation medium. Currently, several techniques have been frequently used to prepare homogenous inocula of edible mushrooms, including the use of a blender (Jager et al., 1985), a homogenizer (Lee et al., 2007), a pestle-mortar (Upadhyay et al., 2014), agitation in shake flasks containing glass beads (Emelyanova, 2005), and simply washed mat cultures (Zhu et al., 2008). Among these, the homogenizer method has been most frequently used.
In the present study, to provide a theoretical base for the preparation of an inoculum for G. lucidum submerged culture, the homogenization efficiency of the cells by sonoporation was examined. Its effects on cellular constituents leakage, metabolic activity, and laccase activity was also determined. Moreover, submerged culture using sonoporated mycelium as inoculum was examined for biomass and exopolysaccharide (EPS) production, followed by optimization of inoculum level. The present study demonstrated that sonoporation can immediately and efficiently homogenize the mycelium of G. lucidum, and the sonoporated mycelium as inoculum showed high productivity of biomass and EPS in submerged culture.
Materials and Methods
Strains and Media
G. lucidum, registered as G10016, was obtained from the Mycological Research Centre, Fujian Agriculture and Forestry University, Fuzhou, China. It was maintained on potato dextrose slants at 4C and subcultured every four weeks. Growth was maintained at 25C for 7 days.
The medium used for both seed culture and submerged culture consisted of the following components (per liter): glucose, 35 g; peptone, 5 g; yeast extract, 4 g; KH2PO4, 1.5 g; MgSO4, 1 g; and vitamin B1, 10 mg. It was autoclaved at 121C for 20 min.
Slants were inoculated with G. lucidum mycelia in agar medium and incubated at 25C for 7 days. For the first pre-culture, an entire slant was squashed into approximately soybean-sized agar blocks with a sterile inoculated rake, and a half of the agar blocks were transferred into a 250 mL shake flask containing 80 mL medium. The inoculated flask was grown at 28C for 4 days with shaking at 170 rpm. For the second pre-culture, the first pre-culture (5 mL) was inoculated into 80 mL medium in a 250 mL flask, and cultivated at 28C for 3 days with shaking at 170 rpm.
For submerged culture, a 250 mL flask contained 80 mL medium was inoculated with 4 mL of the homogenate prepared by sonoporation (as described in the "Sonoporation" section) of the second pre-culture. Culture was carried out at 170 rpm and 28C for 6 days. As a control, the second pre-culture (4 mL) without sonoporation in the pellet-type form was used. For the optimization of inoculum size, 80 mL of medium was inoculated with the homogenate varying from 1 mL to 7 mL. At the end of cultivation, samples were analyzed for biomass, EPS, and intracellular polysaccharide (IPS).
To prepare samples for microscopic examination, plate count, and investigation of the effects of sonoporation on the leakage of cellular constituents, laccase activity, and metabolic activity, 60 mL of the second pre-culture broth was used to harvest the mycelia (about 0.55 g, dry weight) by filtration on a sterile nylon cloth with 60 um pore size that was then washed thoroughly with sterilized distilled water. The cells obtained were re-suspended in 60 mL sterile 0.75% saline in a 100 mL flask, and were employed for sonoporation for a total of 12 cycles (each cycle consisted of 5 s burst and 5 s break), and every two cycles samples were withdrawn. To prepare a homogenous inoculum for use in submerged culture, the second pre-culture broth of 60 mL was directly transferred into a 100 mL sterilized flask and sonoporated for 12 cycles.
An ultrasonicator (JY96-IIN, Ningbo Xingzhi Bioscience and Biotechnology Co., Ltd, Ningbo, China) was used, which provided a frequency of 20 kHz and a horn tip of 6 mm. The operation was as follows: the tip after disinfected with 75% ethanol was immersed into the samples contained in 100 mL flasks, with a distance of approximately 1 cm above the bottom of the flasks. Energy at a power of 125 w was applied in pulse mode with a 5 s burst and 5 s break. To prevent overheating, the flasks were placed in an ice bath during the process.
Sonoporated samples were initially diluted 10-fold. Aliquots of 50 uL were pipetted onto a clean slide and covered with a coverlip. A microscope with a 10X objective (DM750, Leica, Germany) and equipped with a camera (Leica DMC2900, Leica, Germany) was used for analysis.
Sonoporated samples were diluted 10-fold serially up to 10000-fold. After vortexing, aliquots of 0.2 mL were uniformly spread on PDA agar medium in a Petri dish (9 cm diameter) and sealed with a Parafilm membrane (Polisciences Inc., Warrington, USA). After incubation at 25C for 3 d, the number of colonies was counted and expressed as cfu/mL. For comparison, the number of pellets in 5 mL the second pre-culture was visually counted, and averaged to obtain the starting value of cfu/mL.
Protein Leakage Assay
The protein concentration was determined using the dye binding method as described by Bradford (1976), using bovine serum albumin (BSA) as a standard.
Laccase Activity Assay
Laccase activity was assayed according to the method of Bourbonnais and Paice (1990) using 2, 2'-azinobis (3-ethylbenzothiazoline-6-sulfonic acid) (ABTS) as a substrate. The assays were conducted in a 3 mL reaction mixture consisting of 2.5 mL of 0.1 M sodium acetate buffer (pH 5.0), 0.2 mL of 1 mM ABTS solution, and 0.3 mL supernatant of the homogenate. The change in absorbance at 420 nm was recorded over 3 min and one activity unit was defined as the amount of enzyme that oxidized 1 umol ABTS/min. The extinction coefficient of 3.6 x 104 mol-1 cm-1 was used for oxidized ABTS (Bourbonnais and Paice, 1990).
Metabolic Activity Assay
Fluorescent dye 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyltetrazolium bromide (MTT) was utilized for determining metabolic activity of the cells. It was dissolved in sterilized phosphate-buffered saline (PBS) buffer at 5 mg/mL and stored at -20C. Before use, the stock MTT solution was thawed at room temperature. Samples of 0.5 mL and 0.1 mL MTT solution were subsequently added into 0.4 mL sterile water with a total volume of 1 mL in a 5 mL vial, yielding a final MTT concentration of 0.5 mg/mL. Samples were stained for 8 h at 28C on a rotary shaker at 120 rpm.
After staining, the mycelia were harvested and washed twice with distilled water by centrifugation at 8000 rpm for 10 min. For extraction of the MTT-formazan, the mycelial pellets were suspended in 3 mL acidified isopropyl alcohol (0.04 M/L HCl in isopropanol) and shaken at 150 rpm in a rotary incubator for 5 h. After centrifugation, the absorbance of the supernatants was measured at 570 nm with acidified isopropyl alcohol as the control. For improving accuracy, the initial metabolic activity was determined from a large volume sample (5 mL) without sonoporation, and then its initial value in 0.5 mL volume was calculated. The initial metabolic activity was considered as 100%.
As G. lucdium mainly grows as a pellet form in liquid fermentation, obtaining a sample from a flask culture by a pipette was not feasible. For this reason, three flasks were taken as three replicates at the end of submerged culture. Whole culture broth in each shake flask was used to separate the mycelial biomass by centrifuging at 8000 g for 10 min. The precipitated mycelia were washed three times with distilled water, and dried at 60C for a sufficient time to a constant weight.
Measurement of Polysaccharides
For determination of EPS, the crude EPS in supernatants was precipitated by the addition of four times the volume of 95% (v/v) ethanol and left overnight. The insoluble components were harvested by centrifugation at 8000 g for 10 min, suspended in 1 M NaOH, and kept at 60C for 1 h. After centrifugation, the resultant supernatant was used for EPS measurement. For IPS determination, the dried mycelia (100 mg) were ground into fine powder (60 mesh), and then suspended in 5 mL of 1 M NaOH at 60C for 1 h. The supernatant was obtained and used for analysis. Both supernatants were measured by the phenol-sulfuric acid method (Dubois et al., 1956).
All experiments were performed in triplicate and data were analyzed using SAS (version 8; SAS Institute, Inc., Cary, NC, USA). Results are expressed as the mean SD.
Visual and Microscopic Observation of Sonoporated Mycelia and Plate Count Assay
Fig. 1 shows the morphology of pellets of G. lucidum before and after sonoporation. Fig. 1A shows that G. lucidum grew mainly as large fluffy pellets in submerged culture and also many spike-like mycelia can be observed on the surface of the pellets (Fig. 1B). Fig. 1C shows the complete homogenization of the pellets after 60 s sonoporation. Here, it should be noted that most of the pellets were disappeared within 10 s sonoporation. Fig. 1D-F shows mycelia by microscopy after different sonoporation times and from these it appears that the homogenization content of mycelia increased with sonoporation time.
As shown in Fig. 2, the cell (in the form of hyphal fragment and mycelial aggregate) concentration increased sharply from an initial value of 1.26 log cfu/mL to 5.87 log cfu/mL within 10 s sonoporation, indicating that the mycelial pellet of G. lucidum can be immediately and effectively homogenized. At 20 s sonoporation it increased to 6.48 log cfu/mL, and thereafter the increase was not obvious, suggesting that the homogenization content of mycelia did not significantly improve. This result was in general accordance with our microscopic examination, which showed that most of the pellets were disappeared by 10 s sonoporation. By combining the microscopic data with the plate count, it can be concluded that sonoporation can immediately and effectively homogenize the liquid-cultured pellets of G. lucidum.
Table 1: Results of biomass, EPS, and IPS in flask cultures using either sonoporated or unsonoporated mycelia as inoculums
Inoculuma###Biomass (g/L )###EPSb (g/L)###IPSb (mg/100 mg dry weight)
Sonoporated mycelia###15.75 1.32###0.54 0.08###1.59 0.06
Unsonoporated mycelia###6.87 0.74###0.37 0.05###1.87 0.09
Effects of Sonoporation on Leakage of Cellular Constituents, Laccase Activity and Metabolic Activity
Leakage of intracellular protein is often used as an indicator for assessing cell damage caused by physical, chemical, and biological treatment (Woo et al., 2000). Time profile of protein leakage, leaked laccase activity and residual metabolic activity of G. lucidum mycelia during sonoporation is shown in Fig. 3. Substantial protein leakage from the mycelium was detected after 10 s sonoporation, and increased almost linearly with time in the period tested (0-60 s), possibly indicating that the content of fragmented mycelia steadily improved. However, the cell concentration remained almost unchanged as compared to the sample after 20 s sonoporation (see Fig. 2). This inconsistency may be due to the strong aggregation of the fragmented mycelia in the subsequent experiments, which led to the reduction of number of hyphal fragment and mycelial aggregate, since the mycelial aggregation is a common phenomenon manifested by filamentous fungi in liquid culture (Yang et al., 2009).
Laccase is one of the most important enzymes involved the degradation of lignocellulosic wastes, and produced by various white-rot fungi like G. lucidum. Fig. 3 indicates that significant laccase activity was detected after 10 s sonoporation. However, only a trend towards increase was observed after that time point. Apparently, laccase activity did not positively correlate with the amount of protein leakage, perhaps due to the inactivation of laccase that may have occurred in the regions of very high temperature and pressure during the collapse of cavitation bubbles during sonoporation (Ho et al., 2006).
As shown in Fig. 3, the metabolic activity of the fungus decreased considerably from 100% to 63.12% within 10 s sonoporation, and then decreased to 45.53% after a further 10 s treatment. Thereafter, it decreased at a very low rate. The sharp decrease in the initial period (0-20 s) may be mainly due to the mycelial fragmentation, since most of the pellets were fragmented in this period, as observed by microscopic examination. On the other hand, little loss of the metabolic activity post the 20 s sonoporation time point suggests that the activity of the fragmented mycelia was not significantly influenced by sonoporation.
Performance of Sonoporated Mycelia as Inoculum for Submerged Culture
The comparative results of submerged culture with the sonoporated and unsonoporated (the control) mycelia as inocula are listed in Table 1, and the corresponding morphology of pellets is shown in Fig. 4. As presented in Table 1, the production of biomass and EPS reached 15.75 g/L and 0.54 g/L, respectively in cultures with the sonoporated inoculum. These were 129.26% and 45.95% higher than those obtained in the control culture (6.87 g/L and 0.37 g/L). Significantly enhanced productivity may be closely related to the high amounts of hyphal fragment and mycelial aggregates as growing points in the culture broth, resulting in rapid growth and complete utilization of the substrate. Fig. 4 shows that small, smooth and compact pellets were formed in cultures using the sonoporated mycelium as homogenized inoculum, while large, fluffy and loose pellets were formed in the control culture (pellet-type inoculum), perhaps due to the difference in the hyphal growing points in the culture broth.
Effect of the Inoculum Size of Sonoporated Mycelium on Biomass and EPS Production
As shown in Fig. 5, the final biomass production generally increased with increasing inoculum, up to 6 mL (6.97%, v/v), and there was still a slight increase when the inoculum was increased to 7 mL (8.05%, v/v). However, compared with the gross trend of biomass increase, an increase in the inoculum level from 2 mL (2.44%, v/v) to 3 mL (3.61%, v/v) was not obvious. It can be reasonably assumed that the concentration of the hyphal fragment and mycelial aggregate at this inoculum level in culture broth favored mycelial aggregation, resulting in little increase in hyphal growing points for the culture with increased inoculum level.
The EPS production increased with an increase in inoculum size up to 5 mL (5.88%, v/v); however, a further increase in inoculum size led to a reduction in EPS production. Several researchers have reported that relatively high sugar concentrations were beneficial for EPS production (Fang and Zhong, 2002; Kim et al., 2006). We, therefore, proposed that the reduction in final EPS production may be related to the low level of glucose present in culture broth during the late culture period, since high inoculum level promoted mycelial growth significantly and thereby consumed much more glucose. From these data, it can be concluded that optimized inoculum level for biomass growth and EPS production is different.
Sonoporation that utilizes ultrasound to generate microbubbles is known to cause chemical and physical changes in biological structures (in a liquid medium), owing to the rapid formation and destruction of the generated bubbles (Koolman et al., 2014). Currently, in the field of biotechnology, sonoporation has a broad range of applications, including its use for inhibition of food-borne pathogens in processed food (Forghani et al., 2013; Koolman et al., 2014), disruption of various kinds of cells (Ren et al., 2007; Sudar et al., 2013; Zhou et al., 2014), and assistance in bioactive component extraction (Kwun et al., 2009; Liu et al., 2011). The present study demonstrated that sonoporation can immediately and effectively homogenize liquid-cultured mycelial pellets of G. lucidum, and highly uniform mycelia can be obtained. The fermentation potential of sonoporated mycelium of G. lucidum is pronounced, although the process of sonoporation negatively affected the fungus.
To our knowledge, this is the first report on the use of sonoporation for preparing homogenized mycelia for use in submerged fermentation of mushrooms.
In the present study, we find that using the sonoporated mycelia as homogenous inoculum significantly improves the production of biomass and EPS production as compared to the pellet-type inoculum. Besides this, the inoculum level can be significantly reduced, since in G. lucidum pellet-type submerged fermentation, it is usually required at 10% (v/v) or above (Tang and Zhong, 2002; Liu and Zhang, 2007). On the other hand, the morphology of mycelia should be considered seriously during the development of submerged culture as it significantly affects the formation of metabolites and product recovery (Du et al., 2003; Papagianni, 2004). As to the edible and medicinal mushrooms, the formation of pellets is generally considered as excellent. Therefore, the formation of small compact pellets as observed in this work may be an additional advantage of the homogenized inoculum prepared by sonoporation for submerged culture.
Taken together, the inoculum prepared by sonoporation holds great promise for use in large scale industrial submerged culture.
In previous studies, a homogenizer-like polytron operated at a high agitation speed has been frequently used to obtain uniform inoculum for fungal liquid fermentation. In the present study, sonoporation appears to be a suitable approach for the preparation of homogenized inoculum of G. lucidum. Compared to the homogenizer method, a major unobvious advantage of sonoporation is that it can be easily integrated with a fermentor, since the horn tip can be separated from the ultrasonicator. Therefore, sonoporation as a means of disrupting the mycelia of edible and medicinal mushrooms for obtaining homogenized inocula on a large scale holds great potential for industrial use.
The present study demonstrated that sonoporation can effectively and quickly homogenize G. lucidum mycelia. Despite the fact that the sonoporation process negatively affected the mycelia of G. lucidum in terms of protein leakage, laccase activity, and metabolic activity, these mycelia as an inoculum still showed high biomass and exopolysaccharide productivity in submerged fermentation, and moreover desirable mycelia morphology was formed.
The authors would like to thank the financial support by the Program of Talent Introduction of Ningde Normal University (no. 2013Y008).
Bae, J.T., J. Sinha, J.P. Park, C.H. Song and J.W. Yun, 2000. Optimization of submerged culture conditions for exo-biopolymer production of Paecilomyces japonica. J. Microbiol. Biotechnol., 10: 482-487
Berovic, M., J. Habijanic, I. Zore, B. Wraber, D. Hodzar, B. Boh and F. Pohleven, 2003. Submerged cultivation of Ganoderma lucidum biomass and immunostimulatory effects of fungal polysaccharides. J. Biotechnol., 103: 77-86
Bourbonnais, R. and M.G. Paice, 1990. Oxidation of non-phenolic substrates, an expanded role for laccase in lignin biodegradation. FEBS Lett., 267: 99-102
Bradford, M.M., 1976. A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. Anal. Biochem., 72: 248-254
Chang, M.Y., G.J. Tsai and J.Y. Houng, 2006. Optimization of the medium composition for the submerged culture of Ganoderma lucidum by Taguchi array design and steepest ascent method. Enzyme Microb. Tech., 38: 407-414
Chien, C.M., J.L. Cheng, W.T. Chang, M.H. Tien, C.M. Tsao, Y.H. Chang, H.Y. Chang, J.F. Hsieh, C.H. Wong and S.T. Chen, 2004. Polysaccharides of Ganoderma lucidum alter cell immunophenotypic expression and enhance CD56+ NK-cell cytotoxicity in cord blood. Bioorg. Med. Chem., 12: 5603-5609
Du, L.X., S.J. Jia and F.P. Lu, 2003. Morphological changes of Rhizopus chinesis 12 in submerged culture and its relationship with antibiotic production. Process Biochem., 38: 1643-1646
Dubois, M., K.A. Gilles, J.K. Hamilton, P.A. Rebers and F. Smith, 1956. Colorimetric method for determination of sugars and related substances. Anal. Chem., 28: 350-356
Emelyanova, E.V., 2005. Effects of cultivation conditions on the growth of the basidiomycete Coriolus hirsutus in a medium with pentose wood hydrolyzate. Process Biochem., 40: 1119-1124
Fang, Q.H. and J.J. Zhong, 2002. Effect of initial pH on production of ganoderic acid and polysaccharide by submerged fermentation of Ganoderma lucidum. Process Biochem., 37: 769-774
Forghani, F., S.M.E. Rahman, M.S. Park, J.H. Park, J. Park, K.B. Song and D.H. Oh, 2013. Ultrasonication enhanced low concentration electrolyzed water efficacy on bacteria inactivation and shelf extension on lettuce. Food Sci. Biotechnol., 22: 131-136
Ho, C.W., T.K. Chew, T.C. Ling, S. Kamaruddin, W.S. Tan and B.T. Tey, 2006. Efficient mechanical cell disruption of Escherichia coli by an ultrasonicator and recovery of intracellular hepatitis B core antigen. Process Biochem., 41: 1829-1834
Jager, A., S. Croan and T.K. Kirk, 1985. Production of ligninases and degradation of lignin in agitated submerged cultures of Phanerochaete chrysosporium. Appl. Environ. Microbiol., 50: 1274-1278
Jong, S.C. and J.M. Birmingham, 1992. Medicinal benefits of the mushroom Ganoderma. Adv. Appl. Microbiol., 37: 101-134
Kim, H.M., S.Y. Paik, K.S. Ra, K.B. Koo, J.W. Yun and J.W. Choi, 2006. Enhanced production of exopolysaccharides by fed-batch culture of Ganoderma resinaceum DG-6556. J. Microbiol., 44: 233-242
Kimura, Y., M. Taniguchi and K. Baba, 2002. Antitumor and antimetastatic effects on liver of triterpenoid fractions of Ganoderma lucidum: Mechanism of action and isolation of an active substance. Anticancer Res., 22: 3309-3318
Koolman, L., P. Whyte, J. Meade, J. Lyng and D. Bolton, 2014. A combination of chemical and ultrasonication treatments to reduce Campylobacter jejuni on raw poultry. Food Bioprocess Technol., 7: 3602-3607
Kwun, K.H., G.J. Kim and H.J. Shin, 2009. Ultrasonication assistance increases the efficiency ofisoflavones extraction from Kudzu (Pueraria lobata Ohwi) roots waste. Biotechnol. Bioprocess Eng., 14: 345-348
Lee, B.C., J.T. Bae, H.B. Pyo, T.B. Choe, S.W. Kim, H.J. Hwang and Y.W. Yun, 2003. Biological activities of the polysaccharides produced from submerged culture of the edible Basidiomycete Grifola frondosa. Enzyme Microb. Tech., 32: 574-581
Lee, W.Y., Y. Park, J.W. Ahn, K.H. Ka and S.Y. Park, 2007. Factors influencing the production of endopolysaccharide and exopolysaccharide from Ganoderma applanatum. Enzyme Microb. Tech., 40: 249-254
Liu, G.Q. and K.C. Zhang, 2007. Enhancement of polysaccharides production in Ganoderma lucidum by the addition of ethyl acetate extracts from Eupolyphaga sinensis and Catharsius molossus. Appl. Microbiol. Biotechnol., 74: 572-577
Liu, Y.M., T.N. Chen, Y.P. Qiu, Y. Cheng, Y. Cao, A.H. Zhao and W. Jia, 2011. An ultrasonication-assisted extraction and derivatization protocol for GC/TOFMS-based metabolite profiling. Anal. Bioanal. Chem., 400: 1405-1417
Papagianni, M., 2004. Fungal morphology and metabolite production in submerged mycelial process. Biotechnol. Adv., 22: 189-259
Paterson, R.R.M., 2006. Ganoderma-A therapeutic fungal biofactory. Phytochemistry, 67: 1985-2001
Ren, X.D., D.W. Yu, L.Yu, G. Gao, S.P. Han and Y. Feng, 2007. A new study of cell disruption to release recombinant thermostable enzyme from Escherichia coli by thermolysis. J. Biotechnol., 129: 668-673
Shih, I.L., K. Pan and C. Hsieh, 2006. Influence of nutritional components and oxygen supply on the mycelial growth and bioactive metabolites production in submerged culture of Antrodia cinnamomea. Process Biochem., 41: 1129-1135
Sone, Y., R. Okuda, N. Wada, E. Kishida and A. Misaki, 1985. Structures and antitumor activities of the polysaccharides isolated from fruiting body and the growing fermentation of mycelium of Ganoderma lucidum. Agric. Biol. Chem., 49: 2641-2653
Sudar, M., D. Valinger, Z. Findrik, D. Vasic-Racki and Z. Kurtanjek, 2013. Effect of different variables on the efficiency of the Baker's yeast cell disruption process to obtain alcohol dehydrogenase activity. Appl. Biochem. Biotechnol., 169: 1039-1055
Tang, Y.J. and J.J. Zhong, 2002. Fed-batch fermentation of Ganoderma lucidum for hyperproduction of polysaccharide and ganoderic acid. Enzyme Microb. Tech., 31: 20-28
Upadhyay, M., B. Shrivastava, A. Jain, M. Kidwai, S. Kumar, J. Gomes, D.G. Goswami, A.K. Panda and R.C. Kuhad, 2014. Production of ganoderic acid by Ganoderma lucidum RCKB-2010 and its therapeutic potential. Ann. Microbiol., 64: 839-846
Woo, I.S., I.K. Rhee and H.D. Park, 2000. Differential damage in bacterial cells by microwave radiation on the basis of cell wall structure. Appl. Environ. Microbiol., 66: 2243-2247
Xu, J.W., W. Zhao and J.J. Zhong, 2010. Biotechnological production and application of ganoderic acids. Appl. Microbiol. Biotechnol., 87: 457-466
Xu, P., Z.Y. Ding, Z. Qian, C.X. Zhao and K.C. Zhang, 2008. Improved production of mycelial biomass and ganoderic acid by submerged culture of Ganoderma lucidum SB97 using complex media. Enzyme Microb Tech., 42: 325-331
Yang, F.C., M.J. Yang and S.H. Cheng, 2009. A novel method to enhance the mycelia production of Ganoderma lucidum in submerged cultures by polymer additives and agitation strategies. J. Taiwan Inst. Chem. Eng., 40: 148-154
Zhang, W.X. and J.J. Zhong, 2013. Oxygen limitation improves Ganoderic acid biosynthesis in submerged cultivation of Ganoderma lucidum. Biotechnol. Bioprocess Eng., 18: 972-980
Zhou, N.D., X.L. Gu, X.H. Zha and Y.P. Tian, 2014. Purification and characterization of a urethanase from Penicillium variabile. Appl. Biochem. Biotechnol., 172: 351-360
Zhu, L.W., J.J. Zhong and Y.J. Tang, 2008. Significance of fungal elicitors on the production of ganoderic acid and Ganoderma polysaccharides by the submerged culture of medicinal mushroom Ganoderma lucidum. Process Biochem., 43: 1359-1370
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|Author:||Shengrong Liu; Weirui Zhang; Yunbo Kuang; Shengyang Zheng|
|Publication:||International Journal of Agriculture and Biology|
|Date:||Aug 31, 2016|
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