(S)-(-)-2-Methyl-1-butanol - CAS 1565-80-6

(S)-(-)-2-Methyl-1-butanol is a chiral resolution reagent to separate racemic compounds into different mirror isomers and is an important tool for the production of optically active drugs.

Product Information

Canonical SMILES
CC[C@H](C)CO
InChI
InChI=1S/C5H12O/c1-3-5(2)4-6/h5-6H,3-4H2,1-2H3/t5-/m0/s1
InChI Key
QPRQEDXDYOZYLA-YFKPBYRVSA-N
Purity
>98.0%(GC)
MDL
MFCD00064299
Physical State
Liquid
Appearance
Colorless liquid
Storage
Inert atmosphere. Room temperature.
Boiling Point
128 °C / 760 mmHg
Flash Point
42.5 °C(108.5 °F)
Density
0.81
Optical Activity
−5.8°( neat)
Refractive Index
1.41
Hazard Class
3
WGK Germany
3
Packing Groups
III

Safety Information

Signal Word
Warning
Precautionary Statement
P210 - P304+P340+P312
Hazard Statements
H226 - H332 - H335

Reference Reading

1. Enriching the production of 2-methyl-1-butanol in fermentation process using corynebacterium crenatum.
JiaFu Lin, HaiFeng Su, Hua Chen. Curr Microbiol. 2020 Aug; 77(8): 1699-1706. DOI: 10.1007/s00284-020-01961-0. PMID: 32300924.
Non-natural 2-methyl-1-butanol (2 MB) has been biosynthesized through the modification of metabolic pathways using Corynebacterium crenatum, a non-model host. However, its production capacity is not effectively improved. In this study, the fermentation process was strengthened through factor combination design (FCD) for enhancing the production of 2 MB. Our results showed that the highest production of 2 MB, 3-methyl-1-butanol (3 MB), ethanol, and total solvent was 4.87 ± 0.39 g/L, 3.57 ± 0.21 g/L, 5.74 ± 0.43 g/L, and 14.18 g/L, respectively, under the optimal fermentation conditions. The optimal fermentation conditions were determined through the FCD to be as follows: pH of 6.5, IPTG concentration of 1.2 mM, fermentation temperature of 32 °C, and fermentation time of 96 h. This study provides a significant guidance for the optimal control technology of the genetically engineered C. crenatum, and also a useful reference for the industrial production of 2 MB via the microbial fermentation approach.
2. Introduction of nadh-dependent nitrate assimilation in synechococcus sp. Pcc 7002 improves photosynthetic production of 2-methyl-1-butanol and isobutanol.
Hugh M Purdy, Brian F Pfleger, Jennifer L Reed. Metab Eng. 2021 Nov 10; 69: 87-97. DOI: 10.1016/j.ymben.2021.11.003. PMID: 34774761.
Cyanobacteria hold promise for renewable chemical production due to their photosynthetic nature, but engineered strains frequently display poor production characteristics. These difficulties likely arise in part due to the distinctive photoautotrophic metabolism of cyanobacteria. In this work, we apply a genome-scale metabolic model of the cyanobacteria Synechococus sp. PCC 7002 to identify strain designs accounting for this unique metabolism that are predicted to improve the production of various biofuel alcohols (e.g. 2-methyl-1-butanol, isobutanol, and 1-butanol) synthesized via an engineered biosynthesis pathway. Using the model, we identify that the introduction of a large, non-native NADH-demand into PCC 7002's metabolic network is predicted to enhance production of these alcohols by promoting NADH-generating reactions upstream of the production pathways. To test this, we construct strains of PCC 7002 that utilize a heterologous, NADH-dependent nitrite reductase in place of the native, ferredoxin-dependent enzyme to create an NADH-demand in the cells when grown on nitrate-containing media. We find that photosynthetic production of both isobutanol and 2-methyl-1-butanol is significantly improved in the engineered strain background relative to that in a wild-type background. We additionally identify that the use of high-nutrient media leads to a substantial prolongment of the production curve in our alcohol production strains. The metabolic engineering strategy identified and tested in this work presents a novel approach to engineer cyanobacterial production strains that takes advantage of a unique aspect of their metabolism and serves as a basis on which to further develop strains with improved production of these alcohols and related products.
The molarity calculator equation

Mass (g) = Concentration (mol/L) × Volume (L) × Molecular Weight (g/mol)

The dilution calculator equation

Concentration (start) × Volume (start) = Concentration (final) × Volume (final)

This equation is commonly abbreviated as: C1V1 = C2V2

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