| Literature DB >> 34976991 |
Xiuyun Wu1, Tao Wu1, Ailin Huang1, Yuanyuan Shen1, Xuanyu Zhang2, Wenjun Song1, Suying Wang1, Haihua Ruan1.
Abstract
Cordyceps militaris, a traditional medicinal ingredient with a long history of application in China, is regarded as a high-value fungus due to its production of various bioactive ingredients with a wide range of pharmacological effects in clinical treatment. Several typical bioactive ingredients, such as cordycepin, D-mannitol, cordyceps polysaccharides, and N6-(2-hydroxyethyl)-adenosine (HEA), have received increasing attention due to their antitumor, antioxidant, antidiabetic, radioprotective, antiviral and immunomodulatory activities. Here, we systematically sorted out the latest research progress on the chemical characteristics, biosynthetic gene clusters and pathways of these four typical bioactive ingredients. This summary will lay a foundation for obtaining low-cost and high-quality bioactive ingredients in large amounts using microbial cell factories in the future.Entities:
Keywords: N6-(2-hydroxyethyl)-adenosine (HEA); biosynthesis; cordycepin; cordyceps polysaccharides; d-Mannitol
Year: 2021 PMID: 34976991 PMCID: PMC8719641 DOI: 10.3389/fbioe.2021.801721
Source DB: PubMed Journal: Front Bioeng Biotechnol ISSN: 2296-4185
FIGURE 1Cordyceps militaris cultured on a wheat medium (A) and on pupae (B) (Guo et al., 2016), and three typical bioactive components (C–E) of Cordyceps militaris.
FIGURE 2Cordycepin biosynthesis pathway. Abbreviations: 5′-RP, ribose-5-phosphate; PRPP, phosphoribosyl pyrophosphate; IMP, inosine monophosphate; ASUC, N6-(1,2-dicarboxyethyl)-AMP; AMP, adenosine-5′-monophosphate; ADP, adenosine diphosphate; 2′-dADP, 2′-deoxyadenosine diphosphate; 2′,3′-cAMP, 2′3′-cyclic monophosphate; 3′-dAMP, adenosine-3′-monophosphate; 2′-C-3′-dA, 2′-carbonyl-3′-deoxyadenosine; PTN, pentostatin; 3′-dI, 3′-deoxyinosine; PRPPK, phosphoribose pyrophosphate kinase; ADS, adenylosuccinate synthase; ADL, adenylosuccinate lyase; ADEK, adenylate kinase; NT5E, 5′-nucleotidase; ADK, adenosine kinase; ADN, adenosine nucleosidase; RNR, ribonucleotide reductases; RNRM, RNR small subunit, NK/CNS3, an N-terminal nucleoside kinase of Cns3; HisG/CNS3, a C-terminal HisG family of ATP phosphoribosyl transferases in Cns3; CNS2, HDc family of metal-dependent phosphohydrolase domain in Cns2; CNS1, the oxidoreductase/dehydrogenase domain in Cns1; ADA, adenosine deaminase. The bold arrow indicates the main synthesis direction of cordycepin, the dashed arrow represents the pathway that needs further verification, the full line represents the established pathway.
FIGURE 3D-mannitol biosynthetic pathway in lactic-acid bacteria, H. sinensis and E. coli. (A) a. Proposed mannitol metabolism in non-lactic-acid bacteria and homofermentative lactic-acid bacteria and b. heterofermentative lactic-acid bacteria PTS: phosphoenolpyruvate-dependent mannitol phosphotransferase system. The size of the arrow indicates the trend of reaction. (B) A recombinant oxidation/reduction cycle in Escherichia coli for D-mannitol formation. (C) The predicted biosynthetic pathway of D-mannitol in H. sinensis. AGP: glucose pyrophosphorylase; GALM: galactose mutarotase; HK: hexokinase; PGM: phosphoglucomutase; GPI: glucose phosphate isomerase; MTLD:mannitol-1-phosphate dehydrogenas; manA: hexokinase-like mRNA coding protein (manA1-manA5). (D) Synthetic pathway constructed in Escherichia coli leading to mannitol production from glucose. Bold arrows indicate overexpression.
FIGURE 4Flow chart of the purification of polysaccharides from C. militaris.
Comparison of extraction methods for polysaccharides.
| Extraction methods | Advantages | Disadvantages |
|---|---|---|
| Hot or boiling water | Simple operation, wide range of applications, cheap solvent | Short storage time and many product impurities |
| Backflow method | Controllable temperature, less solvent consumption, simple operation | Low efficiency, long time |
| Enzyme-assisted extraction | Specificity, high efficiency and mild reaction conditions | Strict reaction conditions, the enzyme is easy to be inactivate, and the conditions need to be optimized |
| Ultrasonic extraction | Low extraction temperature, simple operation | Restricted by ultrasonic attenuation factors, the extraction rate is limited |
| Microwave extraction | High selectivity, simple and fast, can assist other extraction techniques to work together, save solvent, high extraction rate, low cost | Less samples processed at one time |
| Ultra-high pressure extraction | Preserve the activity of the extract | High equipment investment |
| Subcritical water extraction | Simple equipment, short extraction time, large selection of solvents, less pollution, wide application prospects | Use more solvents, longer extraction time, and relatively high cost |
Polysaccharides from C. militaris: extraction methods, characteristics, chemical structures and bioactivities.
| Living strains | Extraction | Category | Components | Linkages | Bioactivities | References |
|---|---|---|---|---|---|---|
|
| size exclusion chromatography (SEC) | Fr-I | — | — | — |
|
| Fr-II | ||||||
| Fr-III | ||||||
| Fr-IV | ||||||
|
| ethanol precipitation, deproteination and gel-filtration chromatography | CPS-2 | Rha:Glc:Gla = 1: 4.46: 2.43 | 1→4, 1→6 linkages | — |
|
| CPS-3 | D-glucose,ɑ-D-glucose | 1→4, 1→6 linkages | — | |||
|
| boiling water | APS | D-galactose,L-arabinose,D-xylose, L-rhamnose, and D-galacturonic acid | Araf-(1f, f5)-Araf-(1f, f4)-Galp-(1f and f4)-GalAp-(1f residues | modulation of the immune function of macrophages |
|
|
| hot water extraction and ethanol precipitation | CMP Fr I | — | — | — |
|
| CMP Fr II | Glu:Gal:Man = 3.28:1.53:1 | 1→2, 1→4, 1→6 linkages | Upregulate the phenotypic functions of macrophages | |||
| CMP Fr III | — | — | — | |||
|
| hot water and precipitated by 50% ethanol | W-CBP50-II | ɑ-glucose,ɑ-mannose | ɑ-type glycosidic linkages | antioxidant activities |
|
| ɑ-galactose and ɑ-arabinose uronic acid and protein | ||||||
|
| Soxhlet extraction using temperature gradient | β-(1→3)-D-glucan | D-glucan | 1→3 linkages | anti-inflammatory |
|
|
| DEAE-52 cellulose anion exchange column and a Sepharose | CMN1 | L-rhamnose, L-arabinose, D-mannose, D-galactose | 1→2, 1→3, 1→4, 1→6 linkages | anti-hypoxic |
|
| G-100 column | ||||||
|
| Subcritical water extraction (SWE) | CMP-W1 | Glu:Gal:Man = 1:1.29:2.84 | — | immunostimulatory activity |
|
| CMP-S1 | Glu:Gal:Man = 1:1.09:2.05 | — | ||||
|
| Column chromatography | CM3-SⅡ | Glu:Gal:Man = 1:3.7:10.6 | 1→2, 1→4, 1→6 linkages | Hypolipidemic |
|
|
| hot water extraction and ethanol precipitation | SDQCP-1 | Glu:Gal:Man = 1:9.7:13.3 | 1→2, 1→4, 1→6 linkages | antioxidant and immunomodulatory |
|
FIGURE 5Analysis of the putative metabolic pathway of N6 -(2-hydroxyethyl) adenosine (HEA); Abbreviations: PTDSS, phosphatidylserine synthase; PSD, phosphatidylserine decarboxylase; EPT, ethanolamine-phosphotransferase; PLC, phospholipase C; ETNK: ethanolamine kinase; ADHOS, adenylohydroxyethyl synthetase; NT5E, 5′-nucleotidase.
Comparison of four bioactives existing methods of acquisition.
| Bioactives | Existing methods of acquisition | Productivity | Advantages | Disadvantages |
|---|---|---|---|---|
| Cordycepin |
| 6,200 mg/L (fermentation broth) | Relatively high yield | Strains degeneracy, long fermentation cycle |
| 6.63 mg/g (sclerotium) | ||||
| Chemical synthesis | 36% (starting from adenosine) | Convenient, quick effect, controllable conditions | High cost for the treatment of the pollution | |
| Microbial cell factory | 137.27 mg/L (Recombinant | Low cost and less pollution, short fermentation cycle, conducive to industrial production | Lower yield than | |
| D-mannitol | Bioreactor fermentation | 61.6 g/L (fermentation broth with fructose as substrate) | Relatively high yield | High fermentation cost, difficult to remove undesirable metabolites |
| Chemical hydrgenation of high-fructose | 65% (starting from D-sorbitol, D-glucose, D-fructose) | Relatively high yield | Requires high pressures, high temperatures, hydrogen gas, and raney nickel catalyst | |
| Biotransformation | 87% (starting from glucose) | High total sugar utilization, without the use of complex media components and elaborate process control mechanisms | Unstable over a long term | |
| Microbial cell factory | 218 mg/L (fermentation broth) | Short fermentation cycle, low cost and less pollution | Relatively low yield | |
| Polysaccharides |
| Varies due to different extraction and purification methods | — | Lack of standard method of polysaccharide collection |
| Yield can be increased by homologous co-overexpression of genes involved in precursor nucleotide sugars biosynthesis | Conducive to genetic manipulation and metabolic engineering to super-produce polysaccharides in other fungi | Need further research | ||
| N6-(2-hydroxyethyl) -adenosine |
| 94 mg/L (fermentation broth) | Relatively high yield | Strains degeneracy, long fermentation cycle |
| Chemical synthesis | 74% (acrylic acid and chloroethanol) | High yield | High material cost and polluted |