Advance in toxic and pathogenic mechanisms of bacterial hemolysins / 中国人兽共患病学报

Many bacterial pathogens can produce hemolysins to lyse erythrocytes,but recent studies revealed that bacterial hemolysins could cause injury and death of many nucleated cells and platelets.According to the difference of molecular structure,cell-binding manner and membrane pore-forming mechanism,most of bacterial hemolysins are classified into the toxins belonging to either repeats in toxin family (RTX) or cholesterol-dependent cytolysin family (CDC).Bacterial hemolysins play important pathogenic roles during infection of bacteria through membrane damage,cell lysis or disruption,ion disequilibriumassociated pathological changes,cell apoptosis or cell necroptosis as well as through TLR2/4-mediated NF-κB,p38MAPK,JNK signaling pathways and NLRs-mediated NLRP3 inflammasomes to cause powerful inflammatory reaction and inflammatory tissue injury.

Enhancement of pigment extraction from B. braunii pretreated using CO2 rapid depressurization

Abstract Extraction of compounds from microalgae requires cell disruption as a pretreatment to increase extraction yield. Botryococcus braunii is a microalga with a significant content of carotenoids and other antioxidant compounds, such as chlorophylls. Cell disruption of B. braunii using CO2 rapid depressurization was studied as a pretreatment for the extraction of carotenoid and chlorophyll pigments. We studied the effect of temperature (21–49 °C) and pressure (6–13 MPa) during static compression on pigment recovery with supercritical CO2 at 40 °C, 30 MPa and solvent flow of 4.7 L NPT/min. Within the experimental region, the extraction yield of carotenoids and chlorophylls increased by 2.4- and 2.2-fold respectively. Static compression conditions of high pressure and low temperature increased the extraction of carotenoids and especially chlorophylls. We selected 21 °C and 13 MPa as the cell disruption condition, which produced 1.91 g/kg d.s. of carotenoids and 14.03 mg/kg d.s. of chlorophylls. Pretreated microalga gave a 10-fold higher chlorophyll extraction yield compared to the untreated sample. While for carotenoids and tocopherols were 1.25 and 1.14-fold higher, respectively. Additionally, antioxidant activity of pretreated microalga (33.22 mmol TE/kg oil) was significantly higher than the value for the untreated samples (29.11 mmol TE/kg oil) (p ≤ 0.05). Confocal microscopy images showed morphological differences between micro-colonies with and without disruption treatment, suggesting that partial cell disruption by rapid depressurization improved the extraction of microalga compounds.

A comparative study on cell disruption methods for release of aspartase from E. coli K-12.

Applicability of different mechanical cell disruption techniques namely sonication, bead milling and French press for the release of aspartase from E. coli K-12 was compared. Various operating parameters of each technique were optimized to obtain maximum aspartase release. The efficiency of aspartase release and cell disruption by all the methods was also compared under optimal conditions. The maximum release of aspartase (98.22%) and maximum cell breakage (84.25%) was observed using French press, while 92% of aspartase release was obtained by both sonication and bead milling. The order of cell disruption constant (k) for aspartase release by these methods was French press > bead milling > sonication. Disruption of cells using French press also demonstrated maximum protein release (14.12 mg/mL). The crude enzyme preparations can be further used for purification and its applications.

Production of antibody fragment (Fab) throughout Escherichia coli fed-batch fermentation process: Changes in titre, location and form of product

Background: Recombinant proteins, including antibodies and antibody fragments, often contain disulfide bond bridges that are necessary for their folding, stability and function. Production of disulfide-bond-containing proteins in the periplasm of Escherichia coli has been very useful, due to unique characteristics of the periplasm, for obtaining fully active and correctly folded products and for alleviating downstream processing. Results: In this study, fed-batch cultivation of Escherichia coli (E. coli) for production of Fab D1.3, which is an anti-hen egg white lysozyme (HEWL) antibody fragment was carried out at 37ºC, and the bacterial cells were induced by adding 0.1 mM IPTG to the culture medium. Fermentor was sampled over the course of fermentation; the bacterial cells were centrifugally separated from the culture broth and subjected to osmotic shock (with excluding HEWL) and sonication procedures. The resulting fractions were analysed for Fab using a combination of ELISA, SDS-PAGE and Western blotting and changes in product titre, location, and form was assessed throughout growth. It was shown that osmotic shock released the Fab from the periplasm very efficiently and its efficacy was 20-45% more than sonication. This study demonstrates that, at high cell density cultivation in fermentor, target product can appear inside and outside the cells, depending on the time of induction. The maximum amount of Fab (47 mg/l) in the periplasm was reached at 14 hrs cultivation (4 hrs post induction), being suitable time for cell harvest, selective periplasmic extraction and downstream capture. The Fab increasingly leaked into the culture medium, and reached its maximum culture medium titre of ~78 mg/l after 6 hrs post induction. After 16 hrs cultivation (6 hrs post induction) the amount of Fab remained constant in different locations within and outside the cells. Western blot analysis of cell fractions showed that certain amount of the Fab was also produced in the cells as insoluble form. Conclusions: In this work we showed that the production of Fab in the periplasm during high cell density cultivation of E. coli in fermentor can be challenging as the product may appear in various locations within and outside the cells. To exploit the advantages of the periplasmic expression systems for purification in downstream processing, bacterial cells should be harvested when they maintain the majority of the target protein in their periplasmic space (i.e. 4 hrs post induction).