PubMed Health⌕ Search
Home/Archive/PubMed

PubMed · 11916253

Microfluidic components for protein characterization.

T Laurell·G Marko-Varga·S Ekström·M Bengtsson·J Nilsson
View original source ↗Export metadata ↓

Abstract

The use of microfluidic components to create an analytical toolbox for the very rapidly growing field of proteomics is described. This toolbox provides novel generic analytical solutions that are highly adaptable for analysis of various biomolecules, ranging from high to low abundant. The components are fabricated using silicon micromachining and consist of a microchip immobilised enzyme reactor (microIMER), a piezoelectric microdispenser and high-density nanovial target plates. This microtechnology based platform interfaces matrix-assisted laser desorption/ionisation time-of-flight mass spectrometry (MALDI TOF-MS) to a wide range of upstream sample handling and/or analytical techniques. Examples of applications such as rapid on-line digestion (12 s) and sample preparation of proteins, interfacing to capillary liquid chromatography (100 attomol sensitivity), and in-vial chemistry on femtomol amounts of sample are presented.

Explore related subjects

BioreactorsBiotechnologyEquipment DesignMiniaturizationNanotechnologyProteinsProteomeSiliconSpectrometry, Mass, Matrix-Assisted Laser Desorption-IonizationJournal ArticleReview

Keep this discovery

Explore connections, maps & timelines

BibTeXRIS

T Laurell, G Marko-Varga, S Ekström, M Bengtsson, J Nilsson. 2001. Microfluidic components for protein characterization.. https://doi.org/10.1016/s1389-0352(01)00036-8

Cite the original work for its findings. Save a collection to share your selection of sources.

KEEP EXPLORING

Related citations

PubMed2025

Unraveling the ecological success of Iodidimonas in a bioreactor treating oil and gas produced water.

UNLABELLED: Iodidimonas sp., a bacterium found in bioreactors treating oil and gas produced water as well as iodide-rich brines, has garnered attention for its unique ability to oxidize iodine. However, little is known about the metabolic capabilities that enable Iodidimonas sp. to thrive in certain unique ecological niches. In this study, we isolated, characterized, and sequenced three strains belonging to the Iodidimonas genus from the sludge of a membrane bioreactor used for produced water treatment. We investigated the genomic features of these isolates and compared them with the four publicly available isolate genomes from this genus, as well as a metagenome-assembled genome from the source bioreactor. Our Iodidimonas isolates had several genes associated with mitigating salinity, heavy metal, and organic compound stress, which likely help these bacteria to survive in produced water. Phenotyping tests revealed that while the isolates could utilize a wide variety of simple carbon substrates, they failed to degrade aliphatic or aromatic hydrocarbons, consistent with the lack of genes associated with common hydrocarbon degradation pathways in their genomes. We hypothesize that these microbes may lead a scavenging lifestyle in the bioreactor and similar iodide-rich brines. IMPORTANCE: Occupying a niche habitat and having few representative isolates, the genus Iodidimonas is a relatively understudied alphaproteobacterial group. Its ability to corrode pipes in iodine production facilities has economic implications, and its ability to generate potentially carcinogenic iodinated organic compounds during treatment of oil and gas produced water may cause environmental and health concerns with the recycling of treated water. Therefore, detailed characterization of the metabolic potential of the Iodidimonas isolates in this study both sheds light on their adaptation to the environmental conditions they inhabit and has environmental and economic significance.

Bioreactors↗
PubMed2003

Integration of production and aqueous two-phase systems extraction of extracellular Fusarium solani pisi cutinase fusion proteins.

Genetic engineering was integrated with the production and purification of Fusarium solani pisi cutinases, in order to obtain the highest amount of enzyme activity units, after purification. An aqueous two-phase system (ATPS) of polyethylene glycol 3350, dipotassium phosphate and whole broth was used for the extraction of three extracellular cutinases expressed in Saccharomyces cerevisiae. The production/extraction process was evaluated regarding cutinases secretion in the medium, partition behaviour and extraction yields in the ATPS. The proteins studied were cutinase wild type and two fusion proteins of cutinase with the tryptophane-proline (WP) fusion tags, namely (WP)(2) and (WP)(4). The (WP)(4) fusion protein enabled a 300-fold increase of the cutinase partition coefficient when comparing to the wild type. However, the secretion of the fusion proteins was lower than of the wild type cutinase secretion. A batch extraction strategy was compared with a continuous extraction in a perforated rotating disc contactor (PRDC). The batch and continuous systems were loaded with as much as 60% (w/w) whole cultivation broth. The continuous extraction strategy provided a 2.5 higher separation capacity than the batch extraction strategy. Considering the integrated process, the cutinase-(WP)(2) proved to lead to the highest product activity, enabling five and six times more product activity than the wild type and the (WP)(4) fusion proteins, respectively.

Bioreactors↗
PubMed2002

Process control for enhanced L-phenylalanine production using different recombinant Escherichia coli strains.

A novel fed-batch approach for the production of L-phenylalanine (L-Phe) with recombinant E. coli is presented concerning the on-line control of the key fermentation parameters glucose and tyrosine. Two different production strains possessing either the tyrosine feedback resistant aroF(fbr) (encoding tyrosine feedback resistant DAHP-synthase (3-desoxy-D-arabino-heptusonate-7-phosphate)) or the wild-type aroF(wt) were used as model systems to elucidate the necessity of finding an individual process optimum for each genotype. With the aid of tyrosine control, wild-type aroF(wt) could be used for L-Phe production achieving higher final L-Phe titers (34 g/L) than the aroF(fbr) strain (28 g/L) and providing higher DAHP-synthase activities. With on-line glucose control, an optimum glucose concentration of 5 g/L could be identified that allowed a sufficient carbon supply for L-Phe production while at the same time an overflow metabolism leading to acetate by-product formation was avoided. The process approach is suitable for other production strains not only in lab-scale but also in pilot-scale bioreactors.

Bioreactors↗