| Literature DB >> 35004648 |
Thien-Kim Le1, Yu-Jin Lee1,2, Gui Hwan Han3, Soo-Jin Yeom1,2.
Abstract
One-carbon (C1) chemicals are potential building blocks for cheap and sustainable re-sources such as methane, methanol, formaldehyde, formate, carbon monoxide, and more. These resources have the potential to be made into raw materials for various products used in our daily life or precursors for pharmaceuticals through biological and chemical processes. Among the soluble C1 substrates, methanol is regarded as a biorenewable platform feedstock because nearly all bioresources can be converted into methanol through syngas. Synthetic methylotrophy can be exploited to produce fuels and chemicals using methanol as a feedstock that integrates natural or artificial methanol assimilation pathways in platform microorganisms. In the methanol utilization in methylotrophy, methanol dehydrogenase (Mdh) is a primary enzyme that converts methanol to formaldehyde. The discovery of new Mdhs and engineering of present Mdhs have been attempted to develop synthetic methylotrophic bacteria. In this review, we describe Mdhs, including in terms of their enzyme properties and engineering for desired activity. In addition, we specifically focus on the application of various Mdhs for synthetic methylotrophy.Entities:
Keywords: C1 gas; assimilation; formaldehyde; methanol dehydrogenase; synthetic methylotrophy
Year: 2021 PMID: 35004648 PMCID: PMC8741260 DOI: 10.3389/fbioe.2021.787791
Source DB: PubMed Journal: Front Bioeng Biotechnol ISSN: 2296-4185
FIGURE 1Natural methane and methanol utilization pathways in methylotrophs.
FIGURE 2Three classes of methanol dehydrogenases (Mdhs).
Enzyme properties of NAD+-Dependent Mdhs (EC number: 1.1.1.244) and PQQ-Dependent Mdhs (EC number: 1.1.2.7).
| Enzyme | Source | Optimum tem. (°C) | Optimum pH | Molecular weight (kDa) | Association form | Metal ion | Refs | |
|---|---|---|---|---|---|---|---|---|
| Subunit | Native | |||||||
| NAD+-Dependent Mdhs |
| 57–59 | 9.5 | 4.3 | 43 | Decamer | Mg2+ |
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|
| 37 | 7.4 | N.I. | 43 | Decamer | Mg2+ |
| |
| 45 | 9.5 | N.I. | N.I. | Decamer | Mg2+ |
| ||
| 50 | 9.5 | N.I. | 43 | Decamer | Mg2+ |
| ||
| 50 | 9.0 | N.I. | N.I. | Decamer | Mg2+ |
| ||
|
| 37 | 7.4 | N.I. | 43 | Decamer | Mg2+ |
| |
| 45 | 9.5 | N.I. | N.I. | Decamer | Mg2+ |
| ||
|
| 37 | 7.4 | N.I. | N.I. | N.I. | Mg2+ |
| |
|
| 55 | 9.5 | N.I. | 42.8 | N.I. | Mg2+ |
| |
|
| 30 | 9.5 | N.I. | 40.7 | N.I. | Ni2+ |
| |
| PQQ-Dependent Mdhs |
| N.I. | 9.0 | α: 62, β: N.I. | 120 | N.I. | N.I. |
|
|
| N.I. | 9.0 | α: 62, β: N.I. | 120 | N.I. | N.I. | ||
|
| 25 | 7.0 | α: 65, β: 9 | 148 | Heterotetramer | N.I. |
| |
|
| N.I. | 7.0 | α: 66, β: 8.5 | 149 | Heterotetramer | Ca2+ |
| |
|
| N.I. | 9.0 | α: 62, β: 7.5 | 139 | Heterotetramer | Ca2+ |
| |
| 30 | 8.0 | N.I. | 117 | Homodimer | La3+ |
| ||
| N.I. | 8.0 | N.I. | N.I. | N.I. | La3+, Nd3+ |
| ||
| N.I. | 8.0 | N.I. | N.I. | N.I. | Gd3+ |
| ||
|
| 22 | 7.5 | α: 65, β: N.I. | N.I. | Monomer | N.I. |
| |
|
| 22 | 7.5 | α: 65, β: N.I. | N.I. | Monomer | N.I. |
| |
|
| R.T | 8.8 | α: 65, β: N.I. | N.I. | Monomer | N.I. |
| |
|
| R.T | 8.8 | α: 65, β: N.I. | N.I. | Monomer | N.I. | ||
|
| 30 | 8.0 | α: 65.98, β: 7.58 | 147.12 | Tetramer | Ca2+ | ||
|
| N.I. | N.I. | α: 65, β: 7.5 | 145 | Heterotetramer | Mg2+ |
| |
|
| 50 | 9–10 | α: 60, β: 6.5 | 70 | Heterodimer | No metal |
| |
|
| N.I. | N.I. | α: 62, β: 8 | 140 | Heterotetramer | Ca2+ |
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|
| N.I. | N.I. | α: 67, β: 9.5 | 153 | Heterotetramer | Ca2+ |
| |
|
| N.I. | N.I. | α: 63, β: N.I. | 120 | Homodimer | La3+ |
| |
|
| N.I. | N.I. | α: 60, β: 10 | 114 | Heterotetramer | Ca2+ |
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|
| N.I. | N.I. | α: 68, β: N.I. | 108 | Homodimer | Ce3+ |
| |
|
| N.I. | N.I. | N.I. | N.I. | N.I. | La3+ |
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|
| N.I. | N.I. | α: 67.2, β: N.I. | N.I. | Homodimer | La3+ |
| |
|
| 45 | 7.2 | N.I. | 63.6 | Homodimer | Eu3+ |
| |
|
| N.I. | N.I. | α: 64, β: N.I. | 136 | N.I. | Ce3+ |
| |
R.T—Room temperature; N.I—No information.
Summary of substrate affinity for methanol by NAD+-Dependent Mdhs.
| Enzyme type | Strain | Type of enzyme |
|
|
| Evolution method | Refs |
|---|---|---|---|---|---|---|---|
|
|
|
| 0.06 ± 0.002 | N.I. | 170 ± 20 | WT |
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|
| 0.09 ± 0.003 | N.I. | 360 ± 30 | WT | |||
|
| 0.07 ± 0.005 | N.I. | 200 ± 70 | WT | |||
|
| 0.4 ± 0.02 | N.I. | 26 ± 7 | WT | |||
|
| 0.2 ± 0.008 | N.I. | 200 ± 20 | WT | |||
|
| 0.4 ± 0.008 | N.I. | 150 ± 10 | WT | |||
|
| 0.151 ± 0.008 | 0.11 ± N.I. | 150 ± 25 | WT |
| ||
|
| 0,151 ± 0.012 | 0.12 ± N.I. | 416 ± 97 | WT | |||
|
| 0.474 ± 0.032 | 0.32 ± N.I. | 9 ± 2 | WT | |||
|
| 0.394 ± 0.016 | 0.27 ± N.I. | 96 ± 12 | WT | |||
|
|
| 0.03 ± 0.001 | N.I. | 220 ± 30 | WT |
| |
|
| 0.015 ± 0.001 | N.I. | 170 ± 60 | WT | |||
|
| 0.08 ± 0.004 | N.I. | 330 ± 0.05 | WT | |||
|
| 0.2 ± 0.003 | N.I. | 10 ± 1 | WT | |||
|
| 0.05 ± 0.002 | N.I. | 5 ± 1 | WT | |||
|
| 0.38 ± 0.04 | N.I. | 110 ± 50 | WT | |||
|
|
| 0.32 ± N.I. | 0.22 ± 0.01 | 132 ± 15.4 | WT |
| |
|
|
| 2.1 ± N.I. | N.I. | 20 ± N.I. | WT |
| |
|
|
| 0.3027 ± 0.0169 | 0.21 ± 0.01 | 3.23 ± 1.05 | WT |
| |
|
|
|
| 0.44 ± 0.053 | 0.35 ± N.I. | 1,151 ± 274 | Rational approach |
|
|
|
| 0.819 ± 0.082 | 0.59 ± N.I. | 847 ± 190 | Rational approach | ||
|
|
| 0.29 ± N.I. | 0.20 ± 0.01 | 21.6 ± 1.5 | Directed evolution |
| |
|
|
| 0.3423 ± 0.02167 | 0.24 ± 0.01 | 10.35 ± 3.87 | Rational approach |
| |
|
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| 0.4629 ± 0.0576 | 0.33 ± 0.04 | 51.24 ± 23.95 | Rational approach | ||
|
|
| 0.4753 ± 0.05072 | 0.33 ± 0.03 | 36.83 ± 15.82 | Rational approach | ||
|
|
| N.I. | 0.020 ± 0.002 | 0.010 ± 0.003 | Directed evolution |
| |
|
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| N.I. | 0.027 ± 0.005 | 0.046 ± 0.072 | Directed evolution | ||
|
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| N.I | 0.022 ± 0.002 | 0.233 ± 0.107 | Directed evolution | ||
|
|
| 0.0365 ± 0.0017 | N.I. | 636 ± 74 | Directed evolution |
| |
|
|
| 0.0366 ± 0.0016 | N.I. | 615 ± 66 | Directed evolution | ||
|
|
| 0.055 ± 0.0031 | N.I. | 627 ± 89 | Directed evolution | ||
|
|
| 0.0754 ± 0.0023 | N.I. | 440 ± 39 | Directed evolution | ||
|
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| 0.127 ± 0.0033 | N.I. | 432 ± 32 | Directed evolution | ||
|
|
| 0.0885 ± 0.0023 | N.I. | 329 ± 28 | Directed evolution | ||
|
|
| Class I | 0.29 ± N.I. | 0.20 ± 0.01 | 97 ± 9.8 | WT |
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| N.I. | 0.0029 ± N.I. | N.I. | N.I. | WT |
| |
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| N.I. | 0.0038 ± N.I. | N.I. | N.I. | WT | ||
|
| N.I. | 0.0058 ± N.I. | N.I. | N.I. | WT | ||
|
| N.I. | 0.0018 ± N.I. | N.I. | N.I. | WT |
N.I.—No information.
Strategies and advancements in improving methanol bioconversion efficiency of synthetic methylotrophy in recent literature.
| Host | Carbon source/substrate | Used Mdh | Refs |
|---|---|---|---|
|
| 0.4% glucose and 1 M methanol | Mdh from |
|
| 5 mM sodium gluconate, 20 mM sodium pyruvate, 0.1 g/L yeast extract and 500 mM methanol | Mdh from |
| |
| 60 mM methanol and 1 g/L yeast extract | Mdh from |
| |
| 250 mM methanol, 10 g/L glucose |
| ||
| 60 mM methanol and 0.5 g/L yeast extract or 4 g/L glucose |
| ||
| 100 mM methanol and 0.5 g/L yeast extract |
| ||
| 6 g/L xylose and 250 mM methanol | Mdh 2 from |
| |
| 250 mM methanol, 50 mM ribose or xylose, 0.05% casamino acids | Mdh 2 CT4-1 from |
| |
| 400 mM methanol and 20 mM xylose |
| ||
| 500 mM methanol and 20 mM pyruvate |
| ||
|
| 120 mM methanol and 55 mM glucose | Mdh and MD3 from |
|
| 500 mM methanol and 20 mM co-substrates (ribose, xylose or gluconate) | Mdh from |
| |
| 96.90 mM methanol and 25.32 mM xylose | Mdh from |
| |
| Mdh 3 from | |||
| Mdh 2 CT4-1 from | |||
|
| 10 g/L methanol, 20 g/L glucose, 10 g/L yeast extract and 20 g/L peptone | Mdh from |
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