| Literature DB >> 35630641 |
Victor Oliveira Nunes1, Nathália de Castro Vanzellotti1, Jully Lacerda Fraga1, Fernando Luiz Pellegrini Pessoa1,2, Tatiana Felix Ferreira1, Priscilla Filomena Fonseca Amaral1.
Abstract
Androstenedione (AD) is a key intermediate in the body's steroid metabolism, used as a precursor for several steroid substances, such as testosterone, estradiol, ethinyl estradiol, testolactone, progesterone, cortisone, cortisol, prednisone, and prednisolone. The world market for AD and ADD (androstadienedione) exceeds 1000 tons per year, which stimulates the pharmaceutical industry's search for newer and cheaper raw materials to produce steroidal compounds. In light of this interest, we aimed to investigate the progress of AD biosynthesis from phytosterols by prospecting scientific articles (Scopus, Web of Science, and Google Scholar databases) and patents (USPTO database). A wide variety of articles and patents involving AD and phytosterol were found in the last few decades, resulting in 108 relevant articles (from January 2000 to December 2021) and 23 patents of interest (from January 1976 to December 2021). The separation of these documents into macro, meso, and micro categories revealed that most studies (articles) are performed in China (54.8%) and in universities (76%), while patents are mostly granted to United States companies. It also highlights the fact that AD production studies are focused on "process improvement" techniques and on possible modifications of the "microorganism" involved in biosynthesis (64 and 62 documents, respectively). The most-reported "process improvement" technique is "chemical addition" (40%), which means that the addition of solvents, surfactants, cofactors, inducers, ionic liquids, etc., can significantly increase AD production. Microbial genetic modifications stand out in the "microorganism" category because this strategy improves AD yield considerably. These documents also revealed the main aspects of AD and ADD biosynthesis: Mycolicibacterium sp. (basonym: Mycobacterium sp.) (40%) and Mycolicibacterium neoaurum (known previously as Mycobacterium neoaurum) (32%) are the most recurrent species studied. Microbial incubation temperatures can vary from 29 °C to 37 °C; incubation can last from 72 h to 14 days; the mixture is agitated at 140 to 220 rpm; vegetable oils, mainly soybean, can be used as the source of a mixture of phytosterols. In general, the results obtained in the present technological prospecting study are fundamental to mapping the possibilities of AD biosynthesis process optimization, as well as to identifying emerging technologies and methodologies in this scenario.Entities:
Keywords: Mycobacterium; androstenedione; biosynthesis; pharmaceutical; phytosterol; steroid
Mesh:
Substances:
Year: 2022 PMID: 35630641 PMCID: PMC9147728 DOI: 10.3390/molecules27103164
Source DB: PubMed Journal: Molecules ISSN: 1420-3049 Impact factor: 4.927
Figure 1Biochemical pathway of androstenedione (AD) production from phytosterol, obtained from vegetable oils—mainly β-sitosterol. Dashed arrows indicate multiple enzymatic steps. HsD: 3β-hydroxysteroid dehydrogenase. The red dashed borders indicate the obstacles to AD production: the substrate’s low solubility and steroidal nucleus degradation. Green arrows indicate chemical reactions or extraction procedures [1,2,3,6].
Categories of the meso and micro perspectives of the technological prospecting study.
| Meso Perspective Group | Micro Perspective Group | References |
|---|---|---|
| Microorganism | Genetic modification or genetic identification | [ |
| Ks enzyme * | [ | |
| Resting cells, cell wall modifications or immobilization | [ | |
| Microbial selection | [ | |
| Process Improvement | Chemical addition | [ |
| Culture medium | [ | |
| Biphasic system | [ | |
| Operational mode or strategy | [ | |
| Process variables | [ | |
| Metabolic Intermediates and Hormones | PS ** or Co *** conversion into intermediates | [ |
| Hormone production from PS ** | [ | |
| Analytical Methods and others | Analytical methods | [ |
| Others | [ |
* Ks enzyme: The enzymes 3-ketosteroid-9α-hydroxylase (Ksh) and 3-ketosteroid-1-dehydrogenase (KstD); ** PS: phytosterol; *** Co: cholesterol.
Figure 2Numbers of publications related to androstenedione (AD) production from phytosterols over the years (2000 to 2021).
Figure 3Scientific articles that report the biosynthesis of androstenedione (AD) from phytosterols between 2000 and 2021, shown by country.
Figure 4Publications about the androstenedione (AD) biosynthesis from phytosterols by different institutions between 2000 and 2021.
Figure 5Different categories identified in the set of manuscripts involving androstenedione (AD) production from phytosterols, as found in the systematic search (meso analysis).
Process variables for microbial androstenedione (AD) and androstadienedione (ADD) production, from the most relevant scientific articles and patents found in a systematic search.
| Microorganism 1 | Substrate | Genetic Modifications | Reactional Conditions | Results | Differential | Ref. |
|---|---|---|---|---|---|---|
|
| ||||||
| Sterol mixture, weight percentage: 51.7% β-sitosterol, 27.2%; stigmasterol, 17.1% campesterol, and 4.0% brassicasterol—Soybean oil | Cofactor engineering: modification of enzymes related to NADH * and NAD+ * metabolism | pH: 7.2; 30 °C; 140 rpm; 144 h | conversion ratio 94% | nicotinic acid in the phytosterols fermentation system to increase intracellular NAD+/NADH | [ | |
| Phytosterol (98.4% purity) | - | 29 °C; 140 rpm; 120 h | molar yield of AD 55.8% | Oxygen vectors (n-hexadecane, perfluorohexane, soybean oil, PDMS, and PMPS *) | [ | |
| Sterol mixture, weight percentage: 51.7% β-sitosterol, 27.2% stigmasterol, 17.1% campesterol, and 4.0% brassicasterol | Overexpression of cytochrome p450 125 (cyp125-3) | pH: 7.2; 30 °C; 140 rpm; 120 h | Conversion: 96%; 1.98 g·L−1 in 96 h | phytosterols (3 g·L−1) and HP-β-CD ** (25 mM) | [ | |
| Phytosterol (98.4% purity/3 g·L−1) | Overexpression of nicotinic acid phosphoribosyltransferase (NAPRTase) | pH 7.2; 29 °C; 200 rpm; 96 h | molar yield of AD (D) (94.9%) | HP-CD ** (0 or 25 mM) | [ | |
| Phytosterol | - | T1 30 °C; T2 37 °C | 24.7 g·L−1 | two-step bioprocess, cell culture at 30 °C and bioconversion with resting cells at 37 °C | [ | |
| Phytosterol | - | 30 °C; 200 rpm | 11 mmol/L; 0.3 mmol/h/g dry cell | MCD **** | [ | |
| 4.5% β-sitosterol; 26.4% campesterol; 17.7% stigmasterol; 3.6% brassicasterol | Deletion | pH = 8; T = 37 °C; 200 rpm; 72 h | AD, 3.1 g·L−1 | HP-β-CD ***; increase in culture temperature to 37 °C to reduce nucleus degradation | [ | |
| Soybean phytosterols | Inactivation and augmentation of the primary 3-Ketosteroid-δ1-Dehydrogenase | 30 °C; 300 rpm; airflow 0.5 vvm; 96 h | ADD, 4.23 g·L−1; AD, 1.76 g·L−1; (57.8% mole conversion) | - | [ | |
| Phytosterol | - | 30 °C; 200 rpm; 30 h | 1.3–1.4 g·L−1 | Cholinium; amino acids Ionic liquids; Best: 1% ( | [ | |
| 51.7% sitosterol; 27.2% stigmasterol; 17.1% campesterol; 4.0% brassicasterol | - | 30 °C; 140 rpm; 120 h | 84.8% mole conversion | HP-β-CD *** | [ | |
| soybean sterols (20–30 g/L) | - | 30 °C; 220 rpm; phytosterol load of 30 g/L over 144 h | AD: 14.5–15.2 g·L−1 | Mixture of soy steroids (20–30 g/L) in the form of small crystals in suspension (particle size 5–15 μm) | [ | |
| phytosterol-containing vegetable oils | - | pH 7.8; at room temp.; 200 rpm | Best: with canola oil; yield: 7.92 mg/100 mL | Phytosterol-containing vegetable oils directly converted to AD | [ | |
| Phytosterols | - | Ionic liquid addition at 84 h, 20:1 ( | AD production reached 2.23 g·L−1 after 5 days | Ionic liquid to increase low substrate solubility | [ | |
|
| olive oil | - | 72 h; 30 °C | Conversion: 90% | Concrete was used as a tool to immobilize the microorganism | [ |
|
| Rice bran oil (RBO) | - | 36 h, pH 7; 30 °C | 0.22 mg AD/40 mg RBO | The unsaponifiable matter of rice bran oil was used as a raw material | [ |
| Phytosterol | nitrosoguanidine (NTG) mutagenesis | 5-L surface-aeration microprocessor-controlled fermentor; 30 °C | Conversion: 70.6% | - | [ | |
|
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| Sitosterol, cholesterol, stigmasterol and campesterol | Nitrosoguanidine mutagenesis | 30 °C; 14 days | - | - | [ | |
| Cyclodextrin-sterol complex | - | 30 °C; 5 days; 200 rpm | - | - | [ | |
| Alpha-sitosterol (AS) | - | 30 °C; 4 days; 220 rpm | 160 mg AD/1000 mg AS | - | [ | |
1 The microbial species names used are the ones re-classified by Gupta et al. [120] but that are mentioned in the cited manuscripts as the original names: Mycolicibacterium sp. (mentioned as Mycobacterium sp.); Mycolicibacterium neoaurum (mentioned as Mycobacterium neoaurum); Mycolicibacterium fortuitum (mentioned as Mycobacterium fortuitum); Mycolicibacterium phlei (mentioned as Mycobacterium phlei). * NADH and NAD+: Nicotinamide adenine dinucleotide (reduced and oxidized, respectively). ** PDMS polydimethylsiloxane and PMPS polymethylphenylsiloxane. *** HP-β-CD hydroxypropyl-β-cyclodextrin. **** MCD methylated β-cyclodextrin. ***** kshA1 and kstD1: Genes involved in the expression of the enzymes 3-ketosteroid-9α-hydroxylase (Ksh) and 3-ketosteroid-1-dehydrogenase (KstD), respectively.
Figure 6Different groups identified in the set of manuscripts, categorized as “microorganism” (microanalysis), for microbial androstenedione production from phytosterols.
Figure 7Different groups identified in the set of manuscripts categorized as “process improvement” (microanalysis) for microbial androstenedione production from phytosterols.
Figure 8Patents that report the biotransformation or biosynthesis of androstenedione (AD) between 1976 and March 2021.
Figure 9Patent-holding institutions and patent applications for androstenedione production between 1976 and March 2021. * Filled by Noh, Seung-Kwon; Kim, Myung-Kuk; Yoon, Won-Tae; Park, Kyung-Moon; Park, Sang-Ok. ** Partnership between Emory University, Hauptman–Woodward Medical Research Institute, and the Research Foundation for the State University of New York.