ArticleMicrobial cell factories2022
Optimization of the production process for the anticancer lead compound illudin M: process development in stirred tank bioreactors.
Article in Microbial cell factories, 2022. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 4 papers.
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4 citing papers in PubMed, 9 citations in OpenAlex.
- Spore-Derived Isolates from a Single Basidiocarp of BioluminescentMicroorganisms · 2025Article
- IMA fungus · 2025Review
- Optimization of the production process for the anticancer lead compound illudin M: downstream processing.Microbial cell factories · 2022Article
- Optimization of the production process for the anticancer lead compound illudin M: improving titers in shake-flasks.Microbial cell factories · 2022Article
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2 authors at 2 institutions in 1 country.
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Abstract
backgroundThe fungal natural products illudin S and M have been investigated as precursors for the development of semisynthetic anticancer agents such as Irofulven (illudin S derivative) which is currently in phase II clinical trials. Recently, illudin M derivatives have shown improved in vitro selectivity towards cancer cells encouraging further investigation. This requires a stable supply of the precursor which is produced by Basidiomycota of the genus Omphalotus. We have recently reported a robust shake flask process for the production of gram quantities of illudin M from Omphalotus nidiformis aiming to transfer that process into stirred tank bioreactors, which can be used in a commercial production set-up. However, process transfer across different systems is not straightforward and particularly challenging when the producer is morphologically complex. There are only a few reports that address the development of bioprocesses for the production of compounds from Basidiomycota as these organisms have not been extensively studied because of their complex life cycles and often are difficult to cultivate under laboratory conditions.
resultsThe recently developed shake flask process delivering stable titers of ~ 940 mg L
conclusionBy identifying and controlling key process parameters, the production process for illudin M was transferred from shake flasks into 2 L stirred tank bioreactors reaching a comparable titer (> 900 mg L
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