Manipulation of sterol homeostasis for the production of 24-epi-ergosterol in industrial yeast

Jiang, Yiqi; Sun, Zhijiao; Lu, Kexin; Wu, Zeyu; Xue, Hailong; Zhu, Li; Li, Guosi; Feng, Yun; Wu, Mianbin; Lin, Jianping; Lian, Jiazhang; Yang, Lirong

doi:10.1038/s41467-023-36007-z

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Published: 27 January 2023

Manipulation of sterol homeostasis for the production of 24-epi-ergosterol in industrial yeast

Nature Communications volume 14, Article number: 437 (2023) Cite this article

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Abstract

Brassinolide (BL) is the most biologically active compound among natural brassinosteroids. However, the agricultural applications are limited by the extremely low natural abundance and the scarcity of synthetic precursors. Here, we employ synthetic biology to construct a yeast cell factory for scalable production of 24-epi-ergosterol, an un-natural sterol, proposed as a precursor for BL semi-synthesis. First, we construct an artificial pathway by introducing a Δ²⁴⁽²⁸⁾ sterol reductase from plants (DWF1), followed by enzyme directed evolution, to enable de novo biosynthesis of 24-epi-ergosterol in yeast. Subsequently, we manipulate the sterol homeostasis (overexpression of ARE2, YEH1, and YEH2 with intact ARE1), maintaining a balance between sterol acylation and sterol ester hydrolysis, for the production of 24-epi-ergosterol, whose titer reaches to 2.76 g L⁻¹ using fed-batch fermentation. The sterol homeostasis engineering strategy can be applicable for bulk production of other economically important phytosterols.

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Introduction

Brassinosteroids (BRs), now recognized as the sixth class of plant hormones¹, involved in the regulation of many vital plant physiological activities, such as cell elongation, cell division, seed germination, immunity, and reproduction². Brassinolide (BL), representing the most biologically active compound among natural brassinosteroids, has great potential for agricultural and industrial applications³. However, the natural abundance of this growth-promoting phytohormone is extremely low. For example, Grove et al. only isolated 4 mg BL from 40 kg of bee-collected rape pollen⁴. Thus, scalable production strategies other than plant extraction should be established for practical applications.

Considering the structural complexity of BRs, semi-synthesis based on naturally available sterols has been proposed and attempted⁵. Currently, only two relatively low active BRs (Supplementary Table 1), 24-epi-brassinolide (EBL) and 28-homo-brassinolide (HBL), which can be synthesized from ergosterol⁶ and stigmasterol⁷, have been commercially produced. As for the production of BL, crinosterol, isolated from a scarce invertebrate inhabiting the ocean (crinoidea), has been proposed as the synthetic precursor (Fig. 1a). Unfortunately, the availability of crinosterol is no better than BL^8,9. In recent years, the development of synthetic biology opens up the possibility for bulk production of complex natural products (e.g., BL or synthetic precursors) using microbial cell factories. Without the elucidation of BL or crinosterol biosynthetic pathways (Supplementary Fig. 1), fermentative production of sterol molecules with similar structures as crinosterol becomes a promising alternative for the semi-synthesis of BL. By comparing the side chains of ergosterol, stigmasterol, and crinosterol, we propose 24-epi-ergosterol as an alternative precursor for BL synthesis (Fig. 1a). Although the biosynthesis of 24-epi-ergosterol has not been found in nature, the expansion of genetic databases and the improvement of enzyme properties via directed evolution should enable the design of artificial pathways and microbial cell factories for scalable production of 24-epi-ergosterol.

**Fig. 1: Construction of engineered yeast strains for de novo biosynthesis of 24-epi-ergosterol, serving as a synthetic precursor for BL.**

In addition to the lack of 24-epi-ergosterol biosynthetic pathway, the tight regulation of sterol metabolism represents another major challenge to achieve high-level production. The sterol biosynthetic pathway in Saccharomyces cerevisiae has been studied in depth, which is rather complex, with almost 30 enzymes involved. In addition, ergosterol biosynthesis is subject to feedback regulation at transcriptional, translational, and posttranslational levels to strictly control the intracellular sterol contents¹⁰. Furthermore, to alleviate cytotoxicity, excessive free sterols, including both upstream sterols and downstream sterols, are acylated and stored in lipid droplets (LDs)¹¹. The sterol homeostasis between LDs and cellular membranes depends on two ER-localized acyl-CoA:sterol acyltransferases (ARE1 and ARE2)¹² and three steryl ester hydrolases (YEH1, YEH2, and TGL1)^13,14. Previous metabolic engineering efforts for the construction of sterol-overproducing yeast strains generally focus on boosting the metabolic fluxes towards sterol biosynthesis¹⁵. For example, overexpression of UPC2 (particularly the dominant mutant UPC2-1)^16,17 or ECM22¹⁸, two zinc-cluster transcription factors, upregulated the expression of multiple ergosterol biosynthetic pathway genes (e.g., ERG1, ERG11, ERG25, ERG6, ERG2, and ERG3). As several of the ergosterol biosynthesis enzymes are localized in the endoplasmic reticulum (ER)¹⁹, ER expansion has been employed to increase the yield of protopanaxadiol²⁰, medicagenic acid, and ergosterol²¹. On the other hand, sterols are mainly stored in LDs, and increasing the number and volume of LDs have been found to enhance steroid accumulation and alleviate adverse effects on growth²². What’s more, sterol production could be enhanced by re-localizing ER-targeted proteins to LDs to eliminate the spatial separation between enzymes and substrates²³. Recently, overexpression of ARE2 and ACC1 (encoding acetyl-CoA carboxylase) was found to be optimal for the accumulation and production of ergosterol²⁴. In other words, sterol homeostasis should be carefully manipulated and the biosynthesis, storage, and hydrolysis of sterols should be balanced for the production of 24-epi-ergosterol in yeast.

In this work, we aim to establish a yeast cell factory for scalable production of 24-epi-ergosterol, serving as the precursor for BL synthesis (Fig. 1b). First, we design an artificial pathway for de novo biosynthesis of 24-epi-ergosterol by introducing Δ²⁴⁽²⁸⁾ sterol reductases (DWF1) from plants. Using a high-throughput screening method based on the hypersensitivity of the erg4Δ yeast to sodium dodecyl sulfate (SDS) and Hygromycin B (HygB), we perform directed evolution of DWF1 to increase 24-epi-ergosterol conversion efficiency. Subsequently, we engineer sterol homeostasis to boost metabolic fluxes towards 24-epi-ergosterol. The optimal yeast strains are constructed by overexpressing ARE2, YEH1, and YEH2, without disrupting ARE1, whose titer is further increased by enhancing the expression of DWF1, ERG5 (encoding C-22 sterol desaturase), and ACC1. Finally, high-density cell fermentation enables the production of 24-epi-ergosterol with a titer of 2.76 g L⁻¹ and yield of 19.27 mg gDCW⁻¹. The present study highlights the significance of manipulating sterol homeostasis in achieving high-level production of 24-epi-ergosterol.

Results

Design of an artificial pathway for de novo production of 24-epi-ergosterol in yeast

As an unnatural sterol, no enzymes have been reported to convert ergosta-5,7,22,24(28)-tetraene-3β-ol to 24-epi-ergosterol directly, indicating the need to design an artificial biosynthetic pathway. Therefore, we chose to explore the genetic database of sterol biosynthesis in plants (Fig. 2a), with the chiral preference (Δ²⁴⁽²⁸⁾ reduction) and substrate structure similarity (sterol side chain) as the major criteria. By comparing sterol biosynthetic pathways in yeast and plants, we selected Dimunito/Dwarf1 (DWF1), a Δ²⁴⁽²⁸⁾ sterol reductase converting C28- and C29-Δ²⁴⁽²⁸⁾-olefinic sterols to 24-methyl- and 24-ethylcholesterols²⁵, as the best candidate for 24-epi-ergosterol production.

**Fig. 2: Design and optimization of an artificial pathway for de novo biosynthesis of 24-epi-ergosterol.**

To test the production of 24-epi-ergosterol, ERG4 was inactivated in S1-G-GU, which was based on an industrial yeast CICC1746 with the deletion of GAL80 and overexpression of UPC2-1. The resultant yeast strain YQE102 was further engineered by introducing DWF1 homologous genes from Arabidopsis thaliana (AtDWF1)²⁶, Ajuga reptans (ArDWF1)²⁵, Brassica rapa (BrDWF1), and Cannabis sativa (CsDWF1) (listed in Supplementary Data 1), respectively (Supplementary Figs. 2, 3a). Luckily, the integration of the DWF1 expression cassette into the erg4Δ yeast strain resulted in the formation of a sterol peak in our high-performance liquid chromatography (HPLC) analysis (Supplementary Fig. 3b), which was further confirmed to be 24-epi-ergosterol by mass spectrometry (MS, Supplementary Fig. 4) and nuclear magnetic resonance (NMR, Supplementary Fig. 5). Among multiple yeast strains, YQE224 bearing ArDWF1 produced larger amount of 24-epi-ergosterol, with the titer reaching to 13.79 mg L⁻¹ (Supplementary Fig. 3a). Although the enzyme promiscuity of DWF1 enabled the production of 24-epi-ergosterol in yeast, the activity towards ergosta-5,7,22,24(28)-tetraen-3β-ol was still much lower than ERG4 and the production level was still far from industrial applications, indicating the necessity of further modifications by protein engineering and metabolic engineering.

Directed evolution of DWF1 for the enhanced synthesis of 24-epi-ergosterol

After proof-of-concept verification of the biosynthesis of 24-epi-ergosterol, we next proposed to increase the enzymatic activity of DWF1 towards ergosta-5,7,22,24(28)-tetraen-3β-ol via protein engineering approaches. Due to the lack of crystal structures of DWF1 and homologous enzymes, we could only resort to directed evolution, for which a high-throughput screening (HTS) method is required. As previously reported, the erg4Δ yeast strain (accumulation of ergosta-5,7,22,24(28)-tetraen-3β-ol but not ergosterol as the final product) exhibited pleiotropic defects such as hypersensitivity to SDS²⁷ and HygB²⁸. Considering the structural similarity, 24-epi-ergosterol should be able to complement ergosterol deficiency to some extent, based on which we could establish an HTS method by coupling DWF1 activity to cell growth under SDS and HygB stressed conditions. To facilitate library construction and HTS, the haploid erg4Δ strain YQE101 based on the laboratory yeast BY4741 was chosen as the chassis for directed evolution efforts.

To establish the growth-associated HTS method, we constructed and compared the growth rate of four yeast strains, YQP1 (BY4741 harboring pRS42H, high-level production of ergosterol, positive control), YQP2 (YQE101 harboring pRS42H, no ergosterol or 24-epi-ergosterol production, negative control), YQP3 (YQE101 harboring pRS42H-AtDWF1, low-level production of 24-epi-ergosterol), and YQP4 (YQE101 harboring pRS42H-ArDWF1, slightly higher production of 24-epi-ergosterol), in YPD medium supplemented with 100 μg mL⁻¹ HygB and different concentration of SDS. As shown in Fig. 2b, the yeast strain with ERG4 (YQP1) grew normally with 0.01% SDS; the deletion of ERG4 (YQP2) resulted in significant growth inhibition with 0.005% SDS; while the introduction of DWF1 (YQP3 and YQP4), which enabled erg4Δ yeast to synthesize 24-epi-ergosterol, alleviated the growth inhibition with 0.01% and 0.005% SDS significantly. More importantly, the yeast strain (YQP4) producing a higher level of 24-epi-ergosterol exhibited better growth than a low-producing strain (YQP3), indicating a positive relationship between DWF1 activity (24-epi-ergosterol content) and cell growth under SDS and HygB stressed conditions.

We employed the established HTS method to screen the ArDWF1 mutant library generated by error-prone PCR (Supplementary Fig. 6a). About 2,000 colonies were selected from YPD/HygB + 0.01% SDS agar plates and tested for growth in YPD/Hyg + 0.025% SDS medium. Fortunately, we obtained six mutants (Supplementary Fig. 6b and Supplementary Table 2) with elevated growth rates and accordingly increased ArDWF1 catalytic activity. To evaluate the contribution of each mutation, we constructed 10 single mutants by site-directed mutagenesis and compared their performance (Fig. 2c). As all the mutations were found to be beneficial for ArDWF1 activity and it was impossible to test all the combinations individually, we performed multiplex-PCR-based recombination (MUPREC)²⁹ to construct a combinatorial library. Using the same HTS method, we obtained 28 positive combinatorial mutants, enabling better growth in YPD/Hyg + 0.025% SDS medium and higher ArDWF1 catalytic activity. The best mutant Ar207 with a combinatorial mutation of V143G, S306P, and Y338H showed higher ArDWF1 activity and 24-epi-ergosterol production, without losing stereoselectivity (Supplementary Fig. 4b). The introduction of Ar207 into YQE102 (YQE231) resulted in producing 24-epi-ergosterol to 46.72 mg L⁻¹, which was 3.46-fold higher than that of the control strain YQE224 (Fig. 2d and Supplementary Fig. 7).

Manipulation of sterol homeostasis for enhanced 24-epi-ergosterol production

The sterol homeostasis between LDs and cellular membranes is mainly regulated by two sterol acyltransferases (ARE1 and ARE2)¹² and three steryl ester hydrolases (YEH1, YEH2, and TGL1)^13,14. While YEH1, YEH2, and TGL1 were able to hydrolyze all steryl esters, ARE1 mainly acylates early sterols (e.g., lanosterol) and ARE2 mainly contributed to the acylation of late sterols (sterols harboring 5,7-dien, e.g., ergosterol)³⁰. To evaluate their contribution to sterol metabolism, we performed deletion or overexpression of each of these five genes, ARE1, ARE2, YEH1, YEH2, and TGL1. Although the disruption of ARE1 or overexpression of ARE2, YEH1, and YEH2 was beneficial for 24-epi-ergosterol biosynthesis, the improvement by single gene manipulation was rather limited, indicating a need to reconstruct sterol homeostasis through the engineering of sterol acylation and hydrolysis simultaneously (Fig. 3a). As expected, we observed a synergistic effect by simultaneous overexpression of acyltransferase genes (ARE2) and hydrolase genes (YEH1 and/or YEH2). More specifically, strain YQE717 overexpressing ARE2, YEH1, and YEH2 produced 71.04 mg L⁻¹ 24-epi-ergosterol and 220.07 mg L⁻¹ late sterols, which was 1.65- and 2.09-fold higher than that of YQE231, respectively (Fig. 3b). Notably, the introduction of an extra copy of YEH1 or YEH2 expression cassette failed to further increase the production of 24-epi-ergosterol or total late sterols.

**Fig. 3: Manipulation of sterol homeostasis for the production of 24-epi-ergosterol in yeast.**

Although the inactivation of ARE1 (YQE722) resulted in comparable production of 24-epi-ergosterol in shake flasks (Fig. 3b and Supplementary Fig. 8), its performance in the fed-batch bioreactor was adversely affected, including cell growth and product formation (Fig. 3c and Supplementary Figs. 9, 10), particularly in the ethanol fermentation stage. After 120 h fermentation, the cell density of YQE717 reached 186.05 g dry cell weight per liter (gDCW L⁻¹), which was 153.36 gDCW L⁻¹ for YQE722. As a result, higher-level production of 24-epi-ergosterol was achieved in YQE717, with the titer and yield reaching to 2.15 g L⁻¹ and 11.53 mg gDCW⁻¹, respectively. To verify the contribution of sterol homeostasis engineering to the increased production of 24-epi-ergosterol, we analyzed the percentage of un-acylated sterols in YQE231 (un-modified except for the introduction of an ArDWF1 mutant), YQE710 (ARE2), YQE711 (YEH1), YQE712 (YEH2), YQE717 (ARE2-YEH1-YEH2), and YQE722 (are1Δ-ARE2-YEH1-YEH2). The overexpression of ARE2, YEH1 or YEH2 individually either increased or decreased the percentage of un-acylated sterols. On the other hand, simultaneous overexpression of ARE2, YEH1, or YEH2 maintained the acylation ratio comparable to the un-modified yeast strain, indicating the reconstructed balance of sterol acylation and hydrolysis, which was disturbed by further inactivation of ARE1 (Supplementary Fig. 11). The above results highlighted the significance of sterol homeostasis, which should be carefully manipulated for the production of 24-epi-ergosterol and other sterol compounds.

In addition, we performed quantitative PCR (qPCR) to determine the relative transcriptional level of ARE2, YEH1, and YEH2 in YQE231 and YQE717 (Supplementary Fig. 12). In the first 36 h, the production of 24-epi-ergosterol and total sterols were comparable (Supplementary Fig. 8). Afterwards, sterol biosynthesis was nearly halted in YQE231, while YQE717 continued to accumulate significant amounts of sterols and 24-epi-ergosterol. The product formation pattern agreed well with the expression of ARE2, YEH1, and YEH2, which showed higher expression during 24–48 h in YQE717. These results suggested that the increased production of 24-epi-ergosterol was attributed to the enhanced transcriptional level of ARE2, YEH1, and YEH2, or the reconstructed sterol homeostasis in yeast. Considering the accumulation of sterols during the ethanol fermentation stage, the expression of ARE2, YEH1, and YEH2 driven by ethanol inducible promoters might result in increased production of 24-epi-ergosterol. Therefore, ARE2, YEH1, and YEH2 driven by different promoter combinations were investigated (Supplementary Table 3)³¹. Compared with YQE717, YQE717 SES, and YQE717 WSW resulted in a slightly higher level of production of 24-epi-ergosterol, whose total sterol levels were unfortunately decreased dramatically (Supplementary Fig. 13). Therefore, YQE717 was chosen for further metabolic engineering studies.

Increased production of 24-epi-ergosterol by strengthening pathway gene expression

Although the production of 24-epi-ergosterol was significantly increased, ergosta-5,7,22,24(28)-tetraen-3β-ol, the substrate for DWF1, was still accumulated at high levels (Fig. 3b). The accumulation of ergosta-5,7,22,24(28)-tetraen-3β-ol not only lowered the production of the desired product, but also increased downstream purification cost. To achieve higher ratio production of 24-epi-ergosterol, we evaluated several promoters (i.e. P_TEF1, P_TDH3, P_ERG4, P_ERG5, P_CIT2, and P_GAL1) to drive the expression of ArDWF1 mutant (Ar207). When P_CIT2 and P_GAL1 were used, the production of 24-epi-ergosterol was dramatically increased, representing 1.44- and 1.97-fold higher than that with the original P_TEF1, respectively (Fig. 4a). In addition, the overexpression of ACC1, encoding acetyl-CoA carboxylase, has been reported to strengthen fatty acids biosynthesis and accordingly expand 24-epi-ergosterol storage pool²⁴. Thus, we replaced the endogenous P_ACC1 with P_GAL10 to increase the expression level of ACC1 (Supplementary Fig. 14). The resultant strain (YQE729) further increased the production of 24-epi-ergosterol to 160.84 mg L⁻¹ (Fig. 4a). Interestingly, the expression of Ar207 driven by P_GAL1 caused the accumulation of 24-epi-ergosta-5,7-dien-3β-ol, another precursor in the 24-epi-ergosterol biosynthetic pathway. Thus, we constructed YQE734 by overexpressing ERG5 (Supplementary Fig. 14), encoding the Δ²² sterol desaturase, which decreased the accumulation of 24-epi-ergosta-5,7-dien-3β-ol from 43.02 to 3.27 mg L⁻¹ and accordingly increased the production of 24-epi-ergosterol from 160.84 to 171.31 mg L⁻¹, without the production of any ergosterol (Supplementary Fig. 15).

**Fig. 4: Biosynthetic pathway engineering for the production of 24-epi-ergosterol.**

Finally, we evaluated the performance of YQE729 and YQE734 in 2 L fed-batch bioreactors (Supplementary Figs. 16, 17). Due to the enhanced expression of Ar207 driven by P_GAL1 and overexpression of ERG5, ergosta-5,7,22,24(28)-tetraen-3β-ol and 24-epi-ergosta-5,7-dien-3β-ol were not accumulated to high levels, with the ratio of 24-epi-ergosterol to total late sterols reaching to 84.2% in YQE734. On the contrary, 1.68 g L⁻¹ 24-epi-ergosta-5,7-dien-3β-ol was accumulated at the end of fermentation in YQE729, with the ratio of 24-epi-ergosterol to total late sterols dropping to 52.1% (Fig. 4b). Notably, the total late sterols in YQE734 was lower than that in YQE729, probably due to metabolic burden caused by the overexpression of ERG5. In other words, we should fine-tune the expression level of ERG5 in our future studies. Overall, although YQE729 and YQE734 produced a similar amount of 24-epi-ergosta (~2.76 g L⁻¹), high ratio of the target product in total sterols made YQE734 more promising for industrial applications.

Discussion

Due to the lack of biosynthetic pathways and the scarcity of synthetic precursors, Brassinolide (BL), the most active BR compound, has not been widely applied in agriculture and industry yet. In the present study, we constructed an artificial biosynthetic pathway, followed by protein engineering and metabolic engineering, for the production of 24-epi-ergosterol in yeast, which could serve as a scalable route for the semi-synthesis of BL.

Although we have performed two rounds of directed evolution (the first round by error-prone PCR and the second round by DNA shuffling), the activity of ArDWF1 is still rather low, particularly when compared with that of ERG4 towards ergosta-5,7,22,24(28)-tetraen-3β-ol. In addition, the lack of crystal structures and the molecular mechanisms for improved enzymatic activity make further engineering of ArDWF1 rather challenging. To explore the possible mechanisms and provide insights for further protein engineering, we employ the recently developed Alpha fold2 model³² to predict the 3D structure of ArDWF1. As a number of the VAO/PCMH (vanillyl alcohol oxidase/para-cresol methylhydroxylase) flavoprotein family, DWF1 shared a conserved FAD-binding domain, where K122, Q137, V143, and V152 are located³³. V143, V152, and Y338 are located in the interface between the FAD-binding domain and the catalytic domain, and the substitution by smaller amino acid residues will make the domain more flexible to promote FAD turnover. In mutant Ar207 (combining V143G, S306P, and Y338H), the width of this interface is significantly increased (Supplementary Fig. 18). M235T is located at the periphery of the active domain, and the nucleophilic hydroxyl group may contribute to the formation of a hydrogen bond with 3β-OH, leading to improved ArDWF1 activity. The molecular mechanism for S306P, a site far from the catalytic center, is yet to be explored. Based on the predicted structures, most positive mutation sites are located at the interface between the FAD-binding domain and catalytic domain, serving as the entry channel for a substrate. Substitution by smaller amino acid residues is expected to create more space for substrate entry. In other words, sterol reductase like DWF1 could be strengthened by engineering a more flexible interface between the FAD-binding domain and the catalytic domain.

As major components of LDs, steryl esters are formed by the acylation of free sterols via ARE1 and ARE2³⁴. While ARE1 preferentially acylates early sterol intermediates like lanosterol, ARE2 utilizes late sterols as the major substrates, especially ergosterol. Thus, deletion of ARE1 is expected to lower precursor accumulation and push sterol fluxes towards late sterols, which can be further acylated by ARE2 for storage in LDs. Thus, most of the previous metabolic engineering efforts mainly focused on enhancing biosynthesis (such as overexpression of the ergosterol biosynthetic pathway genes) and strengthening storage (such as deletion of ARE1 and/or overexpression of ARE2), while paid less attention to the reversed process, steryl ester hydrolysis (YEH1, YEH2, and TGL1). In the present study, we found that enhancing the hydrolysis of steryl ester could not only improve the sterol fluxes towards the final products, but also significantly increased the total amount of late sterols (Fig. 3b). More specifically, overexpression of ARE2, YEH1, and YEH2 (YQE717 and YQE734) resulted in optimal performance of the engineered yeast strains for producing 24-epi-ergosterol. Interestingly, the inactivation of are1 (YQE722) led to impaired cell growth and lower production of 24-epi-ergosterol (Fig. 3c). In are1 deficient yeast strains, un-acylated lanosterol was accumulated to a higher level, which would stimulate DOA10 (ubiquitin ligase complex)-dependent degradation of ERG1, the first and major rate-limiting step in the post-squalene pathway^30,35. In other words, a circular metabolism may perform better than the linear counterpart for metabolic engineering applications. Notably, although the production of 24-epi-ergosterol and total late sterols were significantly increased in strain (YQE717) overexpressing ARE2, YEH1, and YEH2 simultaneously (Fig. 2b), the ratio of un-acylated sterols was similar to that of the un-modified strain YQE231 (Supplementary Fig. 11). On the contrary, single-gene overexpression, as well as are1 deletion, resulted in obvious changes in the ratio of un-acylated sterols (Supplementary Fig. 11), indicating the significance of maintaining a balance between sterol acylation and steryl ester hydrolysis for the production of 24-epi-ergosterol. Such a sterol homeostasis engineering strategy can be applied to producing other sterol compounds in yeast.

In summary, we constructed an artificial pathway, followed by protein engineering and sterol homeostasis engineering, for the production of 24-epi-ergosterol in S. cerevisiae, promising as a synthetic precursor for scalable production of BL. Using fed-batch fermentation, we were able to produce 2.76 g L⁻¹ 24-epi-ergosterol, with the yield reaching 19.27 mg gDCW⁻¹.

Methods

Chemicals and reagents

All chemicals and kits were purchased from Sangon Biotech (Shanghai, China) unless specifically mentioned. The ergosterol standard, polyethylene glycol (PEG), and deoxyribonucleic acid sodium salt from salmon testes (single-stranded DNA, ssDNA) were purchased from Sigma-Aldrich. PrimeStar DNA polymerase, Ex Taq® DNA Polymerase, and all restriction enzymes were purchased from Takara (Dalian, China). Phanta® Max Super-Fidelity DNA Polymerase and ClonExpress II One Step Cloning Kit were purchased from Vazyme (Nanjing, China). Yeast Plasmid Extraction Kit and DNA Gel Purification Kit were purchased from Solarbio Life Science (Beijing, China) and Thermo Scientific (Massachusetts, USA), respectively.

Strains and media

Yeast strains used in this study are listed in Supplementary Data 2. Yeast strain S1 (CICC1746) is an industrial strain for ergosterol production and was obtained from the China Center of Industrial Culture Collection. BY4741 is kindly provided by Prof. Zhinan Xu (Zhejiang University, China). CICC1746 genomic DNA was used for the amplification of ARE1, ARE2, YEH1, YEH2, and TGL1. Escherichia coli Trans-T1 (TransGen Biotech, China) was used as the host to construct, maintain, and amplify plasmids. E. coli strains were cultured in LB medium with 50 μg mL⁻¹ ampicillin. Yeast strains were cultivated in YPD medium (1% yeast extract, 2% peptone, and 2% d-glucose), with 100 μg mL⁻¹ hygromycin B (HygB) and 200 μg mL⁻¹ geneticin (G418) supplemented when necessary. YPD medium containing 100 μg mL⁻¹ HygB and 0.025% SDS was used for high-throughput screening of ArDWF1 mutants.

Plasmid construction

All plasmids and primers (synthesized by Sangon Biotech, Shanghai, China) used in this study are listed in Supplementary Data 3 and Supplementary Data 4, respectively. Kits used in DNA manipulation were purchased from Sangon Biotech (Shanghai, China). General DNA amplification from genomic DNA was carried out according to the standard protocol of Phanta® Max Super-Fidelity DNA Polymerase (Vazyme, Nanjing, China). A yeast plasmid extraction kit was purchased from Solarbio Life Science (Beijing, China).

DWF1 genes (AtDWF1, ArDWF1, BrDWF1, and CsDWF1) were codon-optimized for yeast expression and synthesized by Sangon Biotech, which were subsequently cloned into pRS42H, resulting in the construction of the plasmid pRS42H-AtDWF1, pRS42H-ArDWF1, pRS42H-BrDWF1, and pRS42H-CsDWF1, respectively. Plasmid pRS42H-SpCas9 and pKan100-ADE2.1³⁶, from Prof. Huimin Zhao (University of Illinois at Urbana‐Champaign, Urbana, Illinois), were used for genome editing in yeast. Specific N20 (from E-CRISP online tool³⁷) of the guide RNA (gRNA) was introduced in the primers used for amplification of the entire pKan100-ADE2.1 plasmid by inverse polymerase chain reaction (PCR)³⁸. The PCR product was then digested by DpnI and transformed into E. coli for amplification.

For co-expression of genes involved in sterol acylation and sterol ester hydrolysis, pEB-3-11 with three expression cassette was constructed based on pEASY®-Blunt Simple Cloning Vectors (TransGen Biotech, Beijing, China). To replace P_TEF1 in pRS42H-Ar207 with P_TDH3, P_ERG4, P_ERG5 P_CIT2, and P_GAL10-P_GAL1, the vector scaffold was amplified by reverse PCR using R-pRS42H-207-F and R-pRS42H-207-R, the desired promoters were obtained by PCR from CICC1746 genome, which were recombined to construct pRS42H-P_TDH3-Ar207, pRS42H-P_ERG4-Ar207, pRS42H-P_ERG5-Ar207, pRS42H-P_CIT2-Ar207, and pRS42H-P_GAL10-PGAL1-Ar207, respectively.

As for the construction of donor DNAs for the deletion of ERG4, ERG5, ARE1, ARE2, YEH1, YEH2, and TGL1, the upstream and downstream fragments were amplified from the CICC1746 and pieced together using overlap extension PCR. The full-length donor DNA fragments were gel purified and cloned into the pEASY®-Blunt Simple Cloning Vectors (TransGen Biotech, Beijing, China), to create pEASY-erg4Δ, pEASY-erg5Δ, pEASY-are1Δ, pEASY-are2Δ, pEASY-yeh1Δ, pEASY-yeh2Δ, and pEASY-tgl1Δ, respectively. To construct donor DNAs for the integration of ARE1, ARE2, YEH1, YEH2, and TGL1 expression cassettes, the corresponding genes were cloned into pRS42H using ClonExpress II One Step Cloning Kit (Vazyme, Nanjing, China).

Yeast transformation and strain construction

CRISPR/Cas9 guided gene knockout and integration were performed with some modifications³⁶. Yeast cells were transformed by the PEG/ssDNA/LiAc method³⁹. The Cas9-expressing strains were constructed by transforming pRS42H-SpCas9 (harboring HygB for hygromycin B resistance) into the corresponding yeast strains. For the co-transformation of gRNA expression plasmids (harboring KanMX for G418 resistance) and donor DNAs into Cas9-expressing strains, heat shock time was prolonged to 50 min, and the yeast strains were recovered in 1 mL YPD for 6 h to allow sufficient expression of the G418 resistance gene. Then the positive transformants harboring pRS42H-SpCas9 and gRNA expression plasmid were selected on YPD/HygB+G418 plates and subsequently confirmed by colony PCR and DNA sequencing.

Directed evolution of DWF1

For the directed evolution of DWF1, the mutant library with two 35 bp homologous arms to P_TEF1 and T_ADH2 in pRS42H was generated by error-prone PCR using Ex Taq® DNA Polymerase (Takara, Dalian, China) with primer pairs of Ep-ArDWF1-F & Ep-ArDWF1-R. The concentration of Mn²⁺ was set as 0.07 mM. Recombination-mediated PCR-directed plasmid construction in vivo in yeast was performed with some modifications⁴⁰. Linearized vector and insert fragments from error-prone PCR were co-transformed into YQE101 in a molar ratio of 1:6, and then the transformants were selected on YPD/HygB+0.01% SDS plates. The colonies in the plates were picked and cultured in 2 mL YPD medium containing 100 μg mL⁻¹ HygB as well as 0.025% SDS in 24-well plates. After three days, the grown strains were selected and cultured in 5 mL YPD/HygB to quantify the production of 24-epi-ergosterol. To minimize the effect of HygB on cell growth, the activity of DWF1 was defined as the ratio of the HPLC peak areas of 24-epi-ergosterol and ergosta-5,7,22,24(28)-tetraen-3β-ol. Plasmids of the positive mutants were extracted using a yeast plasmid extraction kit (Solarbio, Beijing, China) and transformed into E. coli. The corresponding mutations were verified by DNA sequencing. To evaluate the contribution of each mutation to improved DWF1 activity, single mutants of DWF1 were constructed by reverse PCR-based site-directed mutagenesis using PrimeStar DNA polymerase (Takara, Dalian, China).

24-epi-ergosterol production in shake flasks and fed-batch bioreactors

Shake-flask experiments were carried out in biological triplicates in 250 mL shake flasks containing 50 mL YPD. Single colonies were inoculated into 5 mL YPD and incubated at 30 °C for 24 h, and then transferred to 250 mL shake flasks with an initial OD₆₀₀ of 0.1. The yeast strains were cultured at 30 °C and 220 rpm for 96 h.

For fed-batch cultivation, Single colonies were inoculated into 5 mL YPD medium and cultured at 30 °C and 220 rpm for 24 h and then transferred into 250 mL shake flasks containing 50 mL of YPD medium. After 20 h cultivation, yeast cells from two shake flasks were used to inoculate 0.9 L fermentation medium (10 g L⁻¹ d-glucose, 10 g L⁻¹ (NH4)₂SO₄, 8 g L⁻¹ KH₂PO₄, 3 g L⁻¹ MgSO₄, 0.72 g L⁻¹ ZnSO₄.7H₂O, 10 mL L⁻¹ trace metal solution, and 12 mL L⁻¹ vitamin solution) in a 2 L bioreactor (T&J-MiniBox, Shanghai, China). Fermentations were carried out at 30 °C, and pH was controlled at 5.0 by the automatic addition of 5 M ammonia hydroxide. Dissolved oxygen (DO) was maintained at >25% saturation by adjusting the agitation rate (300 to 950 rpm) and airflow rate (1 vvm to 3 vvm). After the complete consumption of initial glucose and residual ethanol, a feeding solution containing 500 g L⁻¹ glucose and 12 mL L⁻¹ vitamin solution was fed into the bioreactor, based on the pseudo-exponential feeding model developed by O’Connor⁴¹. Afterward, to improve the intracellular accumulation of 24-epi-ergosterol, ethanol was fed to the fermenter at a rate of 5 or 6 mL h⁻¹, maintaining DO above 25%. Until the end of the fermentation. The feeding rate F_S during the pseudo-exponential feeding phase was determined by the following equations⁴²:

$${F}_{s=}\left(\frac{\mu }{{Y}_{\frac{x}{s}}}+m\right)\cdot \frac{{X}_{0}{V}_{0}}{S}\cdot {{{{{{\rm{e}}}}}}}^{\mu t}$$

(1)

Where X₀, V₀, and S were the initial biomass density (gDCW L⁻¹), the initial culture volume (L), and the glucose concentration (g L⁻¹) in the feeding medium; Y_X/S was the yield of the cell biomass on glucose (gDCW per g glucose); μ was the specific growth rate (h⁻¹); m was the maintenance coefficient (g glucose gDCW⁻¹ h⁻¹), and t was the time (h) after starting the feeding. A predetermined specific growth rate²⁴ of 0.12 h⁻¹ was used to avoid overflow metabolism. The values of Y_X/S and m were 0.5 and 0.05, respectively⁴³. The feeding rate was adjusted every hour, according to the theoretical model.

Real-time quantitative PCR analysis

Total RNA was isolated from yeast cells by TRIzol (Invitrogen) according to the manufacturer’s instructions. The degradation of genomic DNA and reverse transcription were conducted by ReverTra Ace^TM qPCR RT Master Mix (TOYOBO, Japan). Real-time Quantitative PCR was performed by 2×T5 Fast qPCR Mix (SYBR Green I) (TSINGKE, China) on LineGene 9600 Plus FQD-96A (Bioer Technology, China). The ACT1 gene (encoding actin) was used as the internal control for expression level normalization. The transcription level was analyzed using the 2^−ΔΔCT method⁴⁴. The primers for ACT1, ARE2, YEH1, YEH2, ACC1, Ar207, and ERG5 were synthesized by TSINGKE, and the corresponding sequences were listed in Supplementary Data 4.

Analytical methods

Cell growth was monitored by measuring optical density at 600 nm (OD₆₀₀) using a spectrophotometer (721 G, INESA, Shanghai, China). Glucose and ethanol concentrations were determined using a biosensor (SBA-40C; Biology Institution of Shandong Academy of Science, Jinan, China). 24-Epi-ergosterol and precursor sterols were extracted from yeast cells with some modification⁴⁵. About 500 μL yeast cell culture was harvested and washed twice using ddH₂O. About 600 μL alcoholic KOH solution (25% [w/v] in 50% ethanol) was added to the yeast pellets, which were vortexed for 1 min. Cell suspensions were then boiled for 1 h. After cooling on ice, sterols were extracted with 800 μL petroleum ether, followed by a vigorous vortex for 3 min. About 500 μL petroleum ether (top) layer was collected and dried with a vacuum dryer. Dried samples were dissolved in 500 μL ethanol and analyzed by HPLC, equipped with a Thermo C-18 column (ODS Hypersil, 4.6 × 250 mm, 5 μm) and a UV detector at 280 nm. Methanol/acetonitrile (80:20, v/v) was used as the mobile phase with an elution rate of 1 mL min⁻¹. LC-MS was performed through AB Sciex Triple TOF 5600+, equipped with a Thermo C-18 column (ODS Hypersil, 4.6 × 250 mm, 5 μm) and an atmospheric pressure chemical ionization (APCI) ion source. Sterols were separated on methanol/acetonitrile (80:20, v/v) over 20 min with a flow rate of 0.8 mL min⁻¹ at 30 °C. MS was operated in positive ionization mode, with a scanned m/z range of 100–1500. All results were reported as the average of at least three biological replicates.

The analysis of free sterols and sterol esters was performed with some minor modifications⁴⁶. About 4 mL yeast cell culture was harvested, washed twice using ddH₂O, and resuspended in 800 μL TE buffer. Then, 1 g glass beads (425–600 μm, acid washed, Sigma) was used to disrupt the cell walls mechanically by vigorous vortex for 10 min (30 s vortex and 30 s on ice). Afterward, sterols were extracted with 3.2 mL petroleum ether, followed by vigorous vortex for 3 min. For each extraction, a 500 μL petroleum ether (top) layer was collected separately in two tubes and dried with a vacuum dryer. One tube was analyzed by HPLC directly to determine un-acylated late sterols, while the other was subject to a saponification procedure before quantitative analysis by HPLC to determine total late sterols.

Preparation of 24-epi-ergosterol for NMR analysis

About 120 mL yeast cells were collected and resuspended in 240 mL ethanol–KOH solution (KOH: ethanol: H₂O = 25:50:50, w/v/v) in a 500 mL shake flask. The reaction mixtures were incubated at 95 °C for 2 h. After cooling to room temperature, the samples were extracted with petroleum ether (boiling point range, 60–90 °C) (3 × 200 mL). The organic layer was dried over Na₂SO₄ and evaporated, which was further purified by column chromatography using n-hexane:ethyl acetate (100:1) as the eluent. The resultant crude 24-epi-ergosterol sample also included the upstream precursors ergosta-5,7,22,24(28)-tetraen-3β-ol and ergosta-5,7-dien-3β-ol. The crude product was completely dissolved in 5–7 volumes of solvent (n-hexane:ethyl acetate = 1:1) at 60 °C and then cooled down to room temperature for 5 h. The precipitated solid was filtered and the recrystallization procedure was performed for multiple cycles until the purity of 24-epi-ergosterol was sufficient for NMR analysis. The purified 24-epi-ergosterol and ergosterol standard were dissolved in CDCl₃ for 500 M NMR analysis (BRUKER DMX-500).

Statistics and reproducibility

All experimental data were at least in triplicate and expressed as mean ± standard error. All data analyses were performed by Excel or OriginPro.

Reporting summary

Further information on research design is available in the Nature Portfolio Reporting Summary linked to this article.

Data availability

Data supporting the findings of this work are available within the paper and its Supplementary Information files. A reporting summary for this Article is available as a Supplementary Information file. All the protein structures are obtained from Alpha fold2. Heterologous gene sequences, strains, plasmids, and primers used in this study are provided in Supplementary Data 1–4, respectively. Source data are provided with this paper.

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Acknowledgements

This work was supported by the National Key Research and Development Program (2019YFA0905404), the Natural Science Foundation of Zhejiang Province (LR20B060003), and the Natural Science Foundation of China (22278361). We thank Prof. Zhinan Xu (Zhejiang University, China) for sharing BY4741 and Prof. Huimin Zhao (University of Illinois at Urbana‐Champaign, Urbana, Illinois) for generously providing pRS42H-SpCas9 and pKan100-ADE2.1.

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Key Laboratory of Biomass Chemical Engineering of Ministry of Education, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou, 310027, China
Yiqi Jiang, Zhijiao Sun, Kexin Lu, Zeyu Wu, Hailong Xue, Li Zhu, Guosi Li, Yun Feng, Mianbin Wu, Jianping Lin, Jiazhang Lian & Lirong Yang
ZJU-Hangzhou Global Scientific and Technological Innovation Center, Zhejiang University, Hangzhou, 310000, China
Jiazhang Lian & Lirong Yang
Zhejiang Key Laboratory of Smart Biomaterials, Zhejiang University, Hangzhou, 310027, China
Jiazhang Lian

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Yiqi Jiang
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Contributions

Y.J. and JP.L. designed the experiments. Y.J. performed the experiments, analyzed the data, and drafted the manuscript. Z.W. participated in the directed evolution of ArDWF1. Y.J., Z.S., and K.L. performed the bioreactor fermentation. Y.J., G.L., L.Z., and H.X. performed the establishment of quantitative analytical and separation methods for 24-epi-ergosterol. Y.J. and Y.F. performed qPCR analysis. M.W. and L.Y. participated in the discussion and coordination of the study. JZ.L. participated in data analysis, discussion, and revision of the manuscript. JP.L. supervised the whole research and revised the manuscript. All authors approved the manuscript.

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Correspondence to Jianping Lin or Jiazhang Lian.

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Jiang, Y., Sun, Z., Lu, K. et al. Manipulation of sterol homeostasis for the production of 24-epi-ergosterol in industrial yeast. Nat Commun 14, 437 (2023). https://doi.org/10.1038/s41467-023-36007-z

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Received: 11 October 2022
Accepted: 12 January 2023
Published: 27 January 2023
DOI: https://doi.org/10.1038/s41467-023-36007-z

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