Thermotolerance and molecular chaperone function of the small heat shock protein HSP20 from hyperthermophilic archaeon, Sulfolobus solfataricus P2

Small heat shock proteins are ubiquitous in all three domains (Archaea, Bacteria and Eukarya) and possess molecular chaperone activity by binding to unfolded polypeptides and preventing aggregation of proteins in vitro. The functions of a small heat shock protein (S.so-HSP20) from the hyperthermophilic archaeon, Sulfolobus solfataricus P2 have not been described. In the present study, we used real-time polymerase chain reaction analysis to measure mRNA expression of S.so-HSP20 in S. solfataricus P2 and found that it was induced by temperatures that were substantially lower (60°C) or higher (80°C) than the optimal temperature for S. solfataricus P2 (75°C). The expression of S.so-HSP20 mRNA was also up-regulated by cold shock (4°C). Escherichia coli cells expressing S.so-HSP20 showed greater thermotolerance in response to temperature shock (50°C, 4°C). By assaying enzyme activities, S.so-HSP20 was found to promote the proper folding of thermo-denatured citrate synthase and insulin B chain. These results suggest that S.so-HSP20 promotes thermotolerance and engages in chaperone-like activity during the stress response

Specific prebiotics modulate gut microbiota and immune activation in HAART-naive HIV-infected adults: results of the “COPA” pilot randomized trial

Intestinal mucosal immune system is an early target for human immunodeficiency virus type 1 (HIV-1) infection, resulting in CD4+ T-cell depletion, deterioration of gut lining, and fecal microbiota composition. We evaluated the effects of a prebiotic oligosaccharide mixture in highly active antiretroviral therapy (HAART)-naive HIV-1-infected adults. In a pilot double-blind, randomized, placebo-controlled study, 57 HAART-naive HIV-1-infected patients received a unique oligosaccharide mixture (15 or 30 g short chain galactooligosaccharides/long chain fructooligosaccharides/pectin hydrolysate-derived acidic oligosaccharides (scGOS/lcFOS/pAOS) daily) or a placebo for 12 weeks. Microbiota composition improved significantly with increased bifidobacteria, decreased Clostridium coccoides/Eubacterium rectale cluster, and decreased pathogenic Clostridium lituseburense/Clostridium histolyticum group levels upon prebiotic supplementation. In addition, a reduction of soluble CD14 (sCD14), activated CD4+/CD25+ T cells, and significantly increased natural killer (NK) cell activity when compared with control group were seen in the treatment group. The results of this pilot trial highly significantly show that dietary supplementation with a prebiotic oligosaccharide mixture results in improvement of the gut microbiota composition, reduction of sCD14, CD4+ T-cell activation (CD25), and improved NK cell activity in HAART-naive HIV-infected individuals

Recovery of aprotinin from insulin industrial process effluent by affinity adsorption

Aprotinin is a protease inhibitor found in bovine organs and used as a valuable human therapeutic compound. In this work, a process for the recovery of aprotinin from insulin industrial process effluent via affinity adsorption on immobilized trypsin and chymotrypsin was developed. First, process conditions were set as a result of a study of the effects of pH and ionic strength on pure aprotinin adsorption and desorption utilizing an experimental design methodology. The best conditions obtained with immobilized trypsin as the ligand were adsorption at 0.018 M NaCl and pH 8.7 and desorption at 0.018 M NaCl and pH 2.1. For immobilized chymotrypsin, the best conditions were adsorption at 0.582 M NaCl and pH 8.0 and desorption at 0.582 M NaCl and pH 2.1. Recovery of the inhibitor from the effluent was carried out utilizing a two-step process: trypsin agarose adsorption followed by chymotrypsin-agarose adsorption. Analysis of the chromatographic fractions by trypsin and chymotrypsin inhibition and capillary electrophoresis assays strongly suggested that the recovered inhibitor is aprotinin.21655356

Recombinant aprotinin produced transgenic corn seed: Extraction and purification studies

Expression in transgenic plants is potentially one of the most economical systems for large-scale production of valuable peptide and protein products. However, the downstream processing of recombinant proteins produced in plants has not been extensively studied. In this work, we studied the extraction and purification of recombinant aprotinin, a protease inhibitor used as a therapeutic compound, produced in transgenic corn seed. Conditions for extraction from transgenic corn meal that maximize aprotinin concentration and its fraction of the total soluble protein in the extract were found: pH 3.0 and 200 mM NaCl. Aprotinin, together with a native corn trypsin inhibitor (CTI), was captured using a tryspin-agarose column. These two inhibitors were separated using an agarose-IDA-Cu2+ column that proved to efficiently absorb the CTI while the recombinant aprotinin was collected in the flowthrough with purity of at least 79%. The high purity of the recombinant aprotinin was verified by SDS-PAGE and N-terminal sequencing. The overall recombinant aprotinin recovery yield and purification factor were 49% and 280, respectively. Because CTI was also purified, the recovery and purification process studied has the advantage of possible CTI co-production. Finally, the work presented here introduces additional information on the recovery and purification of recombinant proteins produced in plants and corroborates with past research on the potential use of plants as biorreactors. (C) 2002 Wiley Periodicals, Inc.80326827

Microfluidic devices for continuous production of pDNA/cationic liposome complexes for gene delivery and vaccine therapy

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)To evaluate the process parameters for the production of plasmid DNA/cationic liposome (pDNA/CL) complexes in microfluidic systems, we studied two microfluidic devices: one with simple straight hydrodynamic flow focusing (SMD) and a second one with barriers in the mixing microchannel (patterned walls, PMD). A conventional bulk mixing method was used as a comparison to microfluidic mixing. The CL and the pDNA were combined at a molar positive/negative charge ratio of 6. The results showed that incorporating pDNA into the liposomal structures was different for the two microfluidic devices and that the temperature influenced the average size of complexes produced by the simple microfluidic device, while it did not influence the average complex size in the patterned wall device. Differences were also observed in pDNA probe accessibility in the complexes. The SMD yielded a similar quantity of non-electrostatic bound pDNA as that provided by the bulk mixing method. The complexes produced by the PMD had their pDNA probe accessibility decreased in 40% and achieved lower in vitro transfection levels in HeLa cells than the bulk mixing and simple microfluidic complexation methods. These differences are most likely due to different degrees of association between pDNA and CL, as controlled by the microfluidic devices. This study contributes to the development of rational strategies for controlling the formation of pDNA/CL complexes for further applications in gene and vaccine therapy. (C) 2013 Elsevier B.V. All rights reserved.111203210Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Universidade Estadual de Campinas - UNI-CAMP (Campinas, Brazil)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP

Aprotinin recovery: Comparison between biospecific and peudobiospecific affinity adsorptions

Two adsorption techniques were studied as potential methods for the recovery of aprotinin: a biospecific adsorption (using immobilized trypsin and chymotrypsin as ligants) and a pseudobiospecific adsorption of aprotinin-trypsin complex onto IMAC matrix. These studies indicated that ionic strength has an important effect on aprotinin adsorption on immobilized trypsin, and the pH was the most significant variable in aprotinin desorption from both immobilized enzymes. The aprotinin-trypsin complex adsorption onto the IMAC matrix was not as significantly affected by changes in pH as it was for changes in ionic strength. For the desorption step, both variables significantly affected the complex recovery. However, the effect of ionic strength was markedly stronger for this desorption step.16211912

Recovery and purification of aprotinin from industrial insulin-processing effluent by immobilized chymotrypsin and negative IMAC chromatographies

Aprotinin, a bovine protease inhibitor currently also produced in recombinant bacteria, yeast, and corn, has valuable applications as a human therapeutic and in tissue culture. The objective of this work was to develop the basis of a large-scale aprotinin purification process centered on immobilized metal ion affinity chromatography (IMAC). This technique uses ligands-metal ions-of a lower cost and higher stability than those traditionally used in affinity chromatography. Since aprotinin does not interact with IMAC ligands, collection is from the nonretained fractions (negative chromatography). Stirred-tank batch IMAC adsorption experiments indicated that one-step aprotinin purification could not be successful. Immobilized chymotrypsin chromatography was then used as a prepurification step, yielding a suitable feed for IMAC (with purification factors as high as 476). IMAC column fed with these prepurified materials produced purified aprotinin in the nonretained fractions with purification factors as high as 952. (C) 2002 Elsevier Science Ltd. All rights reserved.37121413142

Sodium citrate and potassium phosphate as alternative adsorption buffers in hydrophobic and aromatic thiophilic chromatographic purification of plasmid DNA from neutralized lysate

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)The number of studies on gene therapy using plasmid vectors (pDNA) has increased in recent years. As a result, the demand for preparations of pDNA in compliance with recommendations of regulatory agencies (EMEA, FDA) has also increased. Plasmid DNA is often obtained through fermentation of transformed Escherichia coli and purification by a series of unit operations, including chromatography. Hydrophobic interaction chromatography (HIC) and thiophilic aromatic chromatography (TAC), both using ammonium sulfate buffers, are commonly employed with success. This work was aimed at studying the feasibility of utilizing alternative salts in the purification of pDNA from neutralized lysate with phenyl-agarose (HIC) and mercaptopyrimidine-agarose (TAC) adsorbents. Their selectivity toward sc pDNA was evaluated through adsorption studies using 1.5 mol/L sodium citrate and 2.0 mol/L potassium phosphate as adsorption buffers. Chromatography with mercaptopyrimidine-agarose adsorbent and 1.5 mol/L sodium citrate was able to recover 91.1% of the pDNA with over 99.0% removal of gDNA and endotoxin. This represents a potential alternative for the primary recovery of sc pDNA. However, the most promising result was obtained using 2.0 mol/L potassium phosphate buffer and a mercaptopyrimidine-agarose column. In a single chromatographic step, this latter buffer/adsorbent system recovered 68.5% of the pDNA with 98.8% purity in accordance with the recommendations of regulatory agencies with regard to RNA and endotoxin impurity. (C) 2013 Elsevier B.V. All rights reserved.9196774Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq

Cloning, expression, and purification of the virulence-associated protein D from Xylella fastidiosa

in this study, an efficient expression system, based on the pET32Xa/LIC vector, for producing a Xylella fastidiosa virulence-associated protein D, found to have a strong similarity to Riemerella anatipestifer and Actinobacillus actinomycetencomitans VapD protein, is presented. The protein has a molecular mass of 17.637 Da and a calculated pI of 5.49. The selected XFa0052 gene was cloned in the pET32Xa/LIC vector and the plasmid was transformed into Escherichia coli BL21 (DE3) strain at 37degreesC. with an induction time of 2 h and 1 mM IPTG concentration. The protein present in the soluble fraction was purified by immobilized metal affinity chromatography (IMAC), and had its identity determined by mass spectrometry (MALDI-TOF) and N-terminal sequencing. The purified protein was found as a single band on SDS-PAGE and its correct folding was verified by circular dichroism spectroscopy. (C) 2004 Elsevier Inc. All rights reserved.37232032

Structural characterization of the H-NS protein from Xylella fastidiosa and its interaction with DNA

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)The nucleoid-associated protein H-NS is a major component of the bacterial nucleoid involved in DNA compaction and transcription regulation. The NMR solution structure of the Xylella fastidiosa H-NS C-terminal domain (residues 56-134) is presented here and consists of two beta-strands and two alpha helices, with one loop connecting the two beta-strands and a second loop connecting the second beta strand and the first helix. The amide H-1 and N-15 chemical shift signals for a sample of XfH-NS56-134 were monitored in the course of a titration series with a 14-bp DNA duplex. Most of the residues involved in contacts to DNA are located around the first and second loops and in the first helix at a positively charged side of the protein surface. The overall structure of the Xylella H-NS C-terminal domain differ significantly from Escherichia coil and Salmonella enterica H-NS proteins, even though the DNA binding motif in loop 2 adopt similar conformation, as well as beta-strand 2 and loop 1. Interestingly, we have also found that the DNA binding site is expanded to include helix 1, which is not seen in the other structures. (C) 2012 Elsevier Inc. All rights reserved.52612228Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)FAPESP [07/50573-6, 07/55128-0, 02/02772-6