| Literature DB >> 34911574 |
Miao Tian1,2, Lingmei Yang1, Zhiyuan Wang1, Pengmei Lv3, Junying Fu1, Changlin Miao1, Ming Li1,4, Tao Liu5, Wen Luo6.
Abstract
BACKGROUND: Liquid lipases are widely used to convert oil into biodiesel. Methanol-resistant lipases with high catalytic activity are the first choice for practical production. Rhizomucor miehei lipase (RML) is a single-chain α/β-type protein that is widely used in biodiesel preparation. Improving the catalytic activity and methanol tolerance of RML is necessary to realise the industrial production of biodiesel.Entities:
Keywords: Biodiesel; Methanol tolerance; N‑Glycosylation; Rhizomucor miehei lipase; α-Helix region
Year: 2021 PMID: 34911574 PMCID: PMC8675521 DOI: 10.1186/s13068-021-02087-6
Source DB: PubMed Journal: Biotechnol Biofuels ISSN: 1754-6834 Impact factor: 6.040
Fig. 1SDS-PAGE analysis of the N9A/N59A and glycosylation mutants. +: processed without PNGase F; −: processed with PNGase F
Fig. 2Enzyme activity of the WT, N9A/N59A and glycosylation mutants
Fig. 3Optimal reaction conditions. The optimal pH (A) and temperature (B) of the WT, N9A/N59A and its mutants were assessed using para-nitrophenyl palmitate (PNPP) as the substrate
Fig. 4Thermostability assay of ProRML. Thermostability of the enzyme was determined using PNPP as the substrate. The thermostability was measured by evaluating the residual activity after enzyme was pre-incubated for 1 h at different temperatures (A) and pre-incubated for 24 h at 45 °C (B). The activity of the unheated sample was set to 100%, and the relative hydrolytic activity at each time point is presented as a percentage
Kinetic parameters and thermostability at 50 °C of WT, N9A/N59A, and glycosylation mutants
| Mutants | Km (mM) | kcat (min−1) | kcat/Km (min−1 mM−1) | Thermostability at 50 °C (2.5 h) |
|---|---|---|---|---|
| WT | 1.16 | 105.29 ± 2.96 | 90.49 ± 2.55 | 26.92 ± 2.26 |
| N9A/N59A | 0.35 | 50.61 ± 2.31 | 145.35 ± 6.65 | 25.77 ± 9.83 |
| N93 | 4.70 | 3816.33 ± 157.15 | 812.33 ± 33.45 | 12.79 ± 6.36 |
| N115 | 0.64 | 435.51 ± 16.61 | 679.43 ± 25.91 | 8.62 ± 4.31 |
| N183 | 0.36 | 71.15 ± 0.38 | 195.49 ± 1.05 | 14.66 ± 0.85 |
| N260 | 1.25 | 293.27 ± 8.94 | 235.56 ± 7.18 | 10.47 ± 4.31 |
| N218 | 13.2 | 51,322.99 ± 1563.66 | 3888.11 ± 118.46 | 29.02 ± 5.52 |
Fig. 5Methanol tolerance of ProRML. Methanol tolerance of the enzyme was determined using PNPP as the substrate. The methanol tolerance was measured by evaluating the residual activity after enzyme was pre-incubated for 1 h at different methanol concentrations (A) and pre-incubated for 8 h at a 50% methanol concentration (B). The activity of the unheated sample was set to 100%, and the relative hydrolytic activity at each time point is presented as a percentage
Fig. 6Biotransformation of FAME. Biotransformation of 5 g colza oil and waste soybean oil to FAME when 0.2 g methanol (molar ratio of 6:1 methanol to oil) is added in one-shot using 5 mL WT and mutant enzymes. C24: biotransformation of colza oil for 24 h; C48: biotransformation of colza oil for 48 h; S24: biotransformation of waste soybean oil for 24 h; S48: biotransformation of waste soybean oil for 48 h