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Psilocybin Production With Genetically Modified Aspergillus nidulans Under Pressurized Conditions

Sophie Weiser, Sidney Jung, Bettina Bardl, Johann E. Kufs, Slavica Janevska, Vito Valiante, Dirk Hoffmeister, Lars Regestein

Biotechnology and Bioengineering December 30, 2025 DOI: 10.1002/bit.70137 via OpenAlex

Summary

AI-generated from the abstract

A bioprocess using a genetically modified strain of the fungus Aspergillus nidulans produced 542 mg per liter of psilocybin from glucose in 68 hours. The filamentous culture broth was sensitive to oxygen availability and power input, which affected viscosity and mass transfer. Scaling up from shake flasks to a 7-liter stirred tank reactor based on specific power input, along with enhanced oxygen supply in a pressure reactor and nitrogen limitation addressed by adding ammonium sulfate, yielded a robust batch process. This biotechnological approach could supplement chemical synthesis for supplying psilocybin for pharmaceutical use and demonstrates pressurized bioprocessing to overcome oxygen limitations for shear-sensitive filamentous organisms.

Study at a glance

Characteristics Experimental study Peer reviewed
Population Genetically modified Aspergillus nidulans strain
Intervention pressurized bioprocess
Duration 68 hours
Topics Psilocybin
Keywords Bioprocess Chemistry Tryptamine Biochemical engineering
Citations 1
Key finding A batch bioprocess using an overproduction strain of Aspergillus nidulans produced 542 mg L−1 psilocybin within 68 hours from glucose.

Abstract

ABSTRACT Psilocybin, an indole alkaloid of psychedelic mushrooms, has the potential to sustainably improve the treatment of several psychiatric diseases. So far, the psilocybin demand for clinical trials has been met by chemical synthesis. In this study, we pursued the biotechnological approach to develop a psilocybin production process utilizing an overproduction strain of Aspergillus nidulans . The developed shake flask cultivation regime was characterized rheologically and was evaluated concerning the sensitivity to changes in oxygen availability and power input. Due to the strong impact of power input on viscosity and thus, (oxygen) mass transfer and mixing of the filamentous culture broth, the bioprocess was scaled up from shake flask to 7 L stirred tank reactor according to the specific power input. Utilizing a pressure reactor, the oxygen supply of the viscous culture broth was enhanced. Subsequently, the nitrogen limitation was addressed by supplementing the cultivation medium with additional ammonium sulfate to provide sufficient building blocks for protein biosynthesis. By producing 542 mg L −1 psilocybin within 68 h from glucose, a robust and efficient batch bioprocess for psilocybin production was developed to potentially contribute to the future supply of psilocybin for pharmaceutical purposes. Moreover, we demonstrated the suitability of pressurized bioprocesses to counteract oxygen limitations for shear‐sensitive, filamentous organisms.

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