RESUMO
Modern beer production is a complex industrial process. However, some of its biochemical details remain unclear. Using mass spectrometry proteomics, we have performed a global untargeted analysis of the proteins present across time during nanoscale beer production. Samples included sweet wort produced by a high temperature infusion mash, hopped wort, and bright beer. This analysis identified over 200 unique proteins from barley and yeast, emphasizing the complexity of the process and product. We then used data independent SWATH-MS to quantitatively compare the relative abundance of these proteins throughout the process. This identified large and significant changes in the proteome at each process step. These changes described enrichment of proteins by their biophysical properties, and identified the appearance of dominant yeast proteins during fermentation. Altered levels of malt modification also quantitatively changed the proteomes throughout the process. Detailed inspection of the proteomic data revealed that many proteins were modified by protease digestion, glycation, or oxidation during the processing steps. This work demonstrates the opportunities offered by modern mass spectrometry proteomics in understanding the ancient process of beer production.
Assuntos
Cerveja/análise , Proteínas/análise , Proteômica/métodos , Manipulação de Alimentos , Proteínas Fúngicas/análise , Hordeum/química , Oxirredução , Peptídeo Hidrolases/metabolismo , Polissacarídeos/metabolismo , Proteínas/metabolismoRESUMO
One of the main challenges for the 21st century is to balance the increasing demand for high-quality proteins while mitigating environmental impacts. In particular, cropland-based production of protein-rich animal feed for livestock rearing results in large-scale agricultural land-expansion, nitrogen pollution, and greenhouse gas emissions. Here we propose and analyze the long-term potential of alternative animal feed supply routes based on industrial production of microbial proteins (MP). Our analysis reveals that by 2050, MP can replace, depending on socio-economic development and MP production pathways, between 10-19% of conventional crop-based animal feed protein demand. As a result, global cropland area, global nitrogen losses from croplands and agricultural greenhouse gas emissions can be decreased by 6% (0-13%), 8% (-3-8%), and 7% (-6-9%), respectively. Interestingly, the technology to industrially produce MP at competitive costs is directly accessible for implementation and has the potential to cause a major structural change in the agro-food system.
Assuntos
Gases de Efeito Estufa , Gado , Agricultura , Ração Animal , Animais , IndústriasRESUMO
BACKGROUND: Peptides are increasingly used in industry as highly functional materials. Bacterial production of recombinant peptides has the potential to provide large amounts of renewable and low cost peptides, however, achieving high product titers from Chemically Defined Media (CDM) supplemented with simple sugars remains challenging. RESULTS: In this work, the short peptide surfactant, DAMP4, was used as a model peptide to investigate production in Escherichia coli BL21(DE3), a classical strain used for protein production. Under the same fermentation conditions, switching production of DAMP4 from rich complex media to CDM resulted in a reduction in yield that could be attributed to the reduction in final cell density more so than a significant reduction in specific productivity. To maximize product titer, cell density at induction was maximized using a fed-batch approach. In fed-batch DAMP4 product titer increased 9-fold compared to batch, while maintaining 60% specific productivity. Under the fed-batch conditions, the final product titer of DAMP4 reached more than 7 g/L which is the highest titer of DAMP4 reported to date. To investigate production from sucrose, sucrose metabolism was engineered into BL21(DE3) using a simple plasmid approach. Using this strain, growth and DAMP4 production characteristics obtained from CDM supplemented with sucrose were similar to those obtained when culturing the parent strain on CDM supplemented with glucose. CONCLUSIONS: Production of a model peptide was increased to several grams per liter using a CDM medium with either glucose or sucrose feedstock. It is hoped that this work will contribute cost reduction for production of designer peptide surfactants to facilitate their commercial application.
Assuntos
Escherichia coli/citologia , Escherichia coli/crescimento & desenvolvimento , Glucose/metabolismo , Peptídeos/metabolismo , Sacarose/metabolismo , Tensoativos/metabolismo , Sequência de Aminoácidos , Técnicas de Cultura Celular por Lotes , Reatores Biológicos/microbiologia , Meios de Cultura , Escherichia coli/metabolismo , Metaboloma , Dados de Sequência Molecular , Peptídeos/química , Proteínas Recombinantes/metabolismoRESUMO
Sucrose has economic and environmental advantages over glucose as a feedstock for bioprocesses. E. coli is widely used in industry, but the majority of current industrial E. coli strains cannot utilize sucrose. Previous attempts to transfer sucrose catabolic capabilities into non-sucrose-utilizing strains have met with limited success due to low growth rates on sucrose and phenotypic instability of the engineered strains. To address these problems, we developed a transferrable sucrose utilization cassette which confers efficient sucrose catabolism when integrated onto the E. coli chromosome. The cassette was based on the csc genes from E. coli W, a strain which grows very quickly on sucrose. Both plasmid-borne expression and chromosomal integration of a repressor-less sucrose utilizing cassette were investigated in E. coli strains K-12, B and C. In contrast to previous studies, strains harboring chromosomal cassettes could grow at the same rate as they do on glucose. Interestingly, we also discovered that spontaneous chromosomal integration of the csc genes was required to allow efficient growth from plasmid-transformed strains. The ability to engineer industrial strains for efficient sucrose utilization will allow substitution of sucrose for glucose in industrial fermentations. This will encourage the use of sucrose as a carbon source and assist in transition of our petrochemical-based economy to a bio-based economy.