Ultrafiltration Method for Plasma Protein Binding Studies and Its
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Platform for a Technological Leap in Antibiotics
Columns CHIMIA 2015, 69, No. 12 809 doi:10.2533/chimia.2015.809 Chimia 69 (2015) 809–811 © Schweizerische Chemische Gesellschaft biotechnet Switzerland Hot from the press! Platform for a Technological Leap in Antibiotics as the microbiologist Stewart Thomas Cole, Head of the Cole Laboratory at EPFL – are working on the development of drugs Elsbeth Heinzelmann, science + technology journalist to treat MDR-TB. In a joint start-up meeting in Bern in early au- tumn 2015, partners from academia and industry explained their Abstract: NTN Swiss Biotech™ brings together the Swiss views and objectives in forging plans for a common Antibiotics Biotech Association SBA, which is involved in regulatory, finan- Platform. cial and legal issues, and biotechnet Switzerland, which is ac- tive in translational R&D, to provide a technology base for joint projects. Biotechnet aims to push promising domains by creat- Everyone Contributes Individual Excellence ing topic-oriented platforms that enable academia and industry to work together to produce R&D results of major importance to The Center of Organic and Medicinal Chemistry (ZHW Wae- society and the economy. The first activity initiated by biotech- denswil) places particular emphasis on the design and synthesis net is the Antibiotics Platform that has now been launched. part of the drug discovery process. In order to improve the po- Keywords: Antimicrobial-resistant organisms · Gram-negative tency, selectivity and pharmacokinetic profiles of modulators of bacteria · Klebsiella pneumoniae · Multidrug-resistant strains · validated drug targets, the group rationally designs and synthe- Pathogenesis of tuberculosis sizes novel scaffolds and focused libraries based on X-ray data of co-crystal structures. -
Crystallization of Oxytetracycline from Fermentation Waste Liquor: Influence of Biopolymer Impurities
Journal of Colloid and Interface Science 279 (2004) 100–108 www.elsevier.com/locate/jcis Crystallization of oxytetracycline from fermentation waste liquor: influence of biopolymer impurities Shi-zhong Li a,1, Xiao-yan Li a,∗, Dianzuo Wang b a Environmental Engineering Research Centre, Department of Civil Engineering, The University of Hong Kong, Hong Kong, China b Chinese Academy of Engineering, Beijing 100038, China Received 28 January 2004; accepted 17 June 2004 Available online 29 July 2004 Abstract Organic impurities in the fermentation broth of antibiotic production impose great difficulties in the crystallization and recovery of antibi- otics from the concentrated waste liquor. In the present laboratory study, the inhibitory effect of biopolymers on antibiotic crystallization was investigated using oxytetracycline (OTC) as the model antibiotic. Organic impurities separated from actual OTC fermentation waste liquor by ultrafiltration were dosed into a pure OTC solution at various concentrations. The results demonstrated that small organic molecules with an apparent molecular weight (AMW) of below 10,000 Da did not affect OTC crystallization significantly. However, large biopolymers, especially polysaccharides, in the fermentation waste caused severe retardation of crystal growth and considerable deterioration in the pu- rity of the OTC crystallized. Atomic force microscopy (AFM) revealed that OTC nuclei formed in the solution attached to the surfaces of large organic molecules, probably polysaccharides, instead of being surrounded by proteins as previously thought. It is proposed that the attachment of OTC nuclei to biopolymers would prevent OTC from rapid crystallization, resulting in a high OTC residue in the aqueous phase. In addition, the adsorption of OTC clusters onto biopolymers would destabilize the colloidal system of organic macromolecules and promote particle flocculation. -
Review and Cost Analysis of Reverse Osmosis and Ultrafiltration
Review and cost analysis of reverse osmosis and ultrafiltration A Senior Project presented to Dr. Bruce Golden of Dairy Science California Polytechnic State University, San Luis Obispo In Partial Fulfillment of the Requirements for the Degree Bachelor of Dairy Science by Jared De Groot March, 2013 © 2013 Abstract The aim in this study was to determine whether implementing an on farm ultrafiltration system was profitable. Ultrafiltration was researched to reduce the amount of milk hauled from producer to processor. An ultrafiltration system involved milk that flowed through a semi-permeable membrane. Through this process water and small amounts of calcium and ash were pressured through the semi-permeable membrane. This permeate would then be able to feed heifers. The protein, fat, solids nonfat, and small amounts of calcium and ash were retained by the membrane. Through the process of ultrafiltration, raw milk was concentrated to three times its original concentration. With the use of ultrafiltration, the dairyman would need to one load of ultrafiltration milk instead of three loads of raw milk. The reduction in the cost of milk hauled and the feed presented to the heifers were the advantages in ultrafiltration. With the saved money on hauling and feeding of heifers, the initial costs of the system and the annual maintenance cost of the system exceed the benefits if implemented on De Groot Dairies. For the on farm ultrafiltration system to break even in ten years, the producer would need to be paid an additional $1.05 /cwt of retentate. This price included the reduced hauling cost and the money saved on the heifer ration. -
Sartorius Ultrafiltration and Protein Purification Products Brochure
Ultrafiltration & Protein Purification Products Fisher Scientific Contents General Information General Information Protein Purification Major Uses for Ultrafiltration 4 Vivapure® Ion Exchange Protein Purification Products 52 Process Alternatives 5 Vivawell Vac Vacuum Manifold Membrane Characteristics 6 Systems 55 Membrane Selection 7 Vivawell Vac 8-strip plate 57 Protein Concentration Vivapure® mini & maxiprep Purification Kits 59 Centrifugal Filtration Protein Concentration Vivapure® mini|maxiprep Protein Vivaspin 500 8 A & G Spin Columns 60 24-Well Ultrafiltration Frame 10 Vivapure® mini|maxiprep MC Spin Vivaspin 2 12 Columns 62 Centrisart I 15 Vivaspin 4 18 Vivapure Anti-HSA/IgG Kits 64 Vivaspin 6 20 Vivapure C18 65 Vivaspin 15 22 Vivaspin 15R 24 Virus Purification and Concentration Vivaspin 20 26 Vivaclear 29 Vivapure® Virus Purification and Concentration Kits 66 Pressure-Fugation DNA Concentration Vivacell 70 30 Adenovirus Purification with Vivacell 100 33 AdenoPACK Kits 67 Vivapure® AdenoPACK 20 68 Gas Pressure Filtration Vivapure® AdenoPACK 100 69 Vivacell 250 36 Vivapure® AdenoPACK 500 71 Tangential Flow Filtration Lentivirus Purification with Vivaflow 50 38 LentiSELECT Kit 73 Vivaflow 200 40 Vivapure® LentiSELECT 40 74 Solvent Adsorption Vivapore 2, 5, 10|20 43 Vivapure® LentiSELECT 500 75 Protein Purification Ultrafiltration Membrane Discs 45 Vivapure® LentiSELECT 1000 76 DNA Concentration Application Notes 77 Vivacon® 500 47 1. Desalting and Buffer Exchange with Vivaspin Centrifugal Concentrators 79 Vivacon® 250 2. Treatment -
Stability of Zopiclone in Whole Blood Studies from a Forensic Perspective
Linköping Studies in Health Sciences, Thesis No. 113 Stability of zopiclone in whole blood ‐ Studies from a forensic perspective Gunnel Nilsson Division of Drug Research Department of Medical and Health Sciences Linköping University, Sweden Linköping 2010 Supervisors Robert Kronstrand, Associate Professor Department of Medical and Health Sciences, Faculty of Health Sciences, Linköping University, Sweden Johan Ahlner, Professor Department of Medical and Health Sciences, Faculty of Health Sciences, Linköping University, Sweden Fredrik C. Kugelberg, Associate Professor Department of Medical and Health Sciences, Faculty of Health Sciences, Linköping University, Sweden Gunnel Nilsson, 2010 Published article has been reprinted with permission of the copyright holder. Paper I © 2010 Elsevier, Forensic Science International Printed in Sweden by LiU‐Tryck, Linköping, Sweden, 2010 ISBN 978‐91‐7393‐339‐1 ISSN 1100‐6013 Dala‐Gård Ring the bells that still can ring Forget your perfect offering There is a crack in everything That’s how the light gets in Anthem by Leonard Cohen Contents CONTENTS ABSTRACT ............................................................................................................................. 1 POPULÄRVETENSKAPLIG SAMMANFATTNING..................................................... 3 LIST OF PAPERS ................................................................................................................... 5 ABBREVIATIONS ................................................................................................................ -
Pharmacology Part 2: Introduction to Pharmacokinetics
J of Nuclear Medicine Technology, first published online May 3, 2018 as doi:10.2967/jnmt.117.199638 PHARMACOLOGY PART 2: INTRODUCTION TO PHARMACOKINETICS. Geoffrey M Currie Faculty of Science, Charles Sturt University, Wagga Wagga, Australia. Regis University, Boston, USA. Correspondence: Geoff Currie Faculty of Science Locked Bag 588 Charles Sturt University Wagga Wagga 2678 Australia Telephone: 02 69332822 Facsimile: 02 69332588 Email: [email protected] Foot line: Introduction to Pharmacokinetics 1 Abstract Pharmacology principles provide key understanding that underpins the clinical and research roles of nuclear medicine practitioners. This article is the second in a series of articles that aims to enhance the understanding of pharmacological principles relevant to nuclear medicine. This article will build on the introductory concepts, terminology and principles of pharmacodynamics explored in the first article in the series. Specifically, this article will focus on the basic principles associated with pharmacokinetics. Article 3 will outline pharmacology relevant to pharmaceutical interventions and adjunctive medications employed in general nuclear medicine, the fourth pharmacology relevant to pharmaceutical interventions and adjunctive medications employed in nuclear cardiology, the fifth the pharmacology related to contrast media associated with computed tomography (CT) and magnetic resonance imaging (MRI), and the final article will address drugs in the emergency trolley. 2 Introduction As previously outlined (1), pharmacology is the scientific study of the action and effects of drugs on living systems and the interaction of drugs with living systems (1-7). For general purposes, pharmacology is divided into pharmacodynamics and pharmacokinetics (Figure 1). The principle of pharmacokinetics is captured by philosophy of Paracelsus (medieval alchemist); “only the dose makes a thing not a poison” (1,8,9). -
Ontogeny of Plasma Proteins, Albumin and Binding of Diazepam, Cyclosporine, and Deltamethrin
nature publishing group Basic Science Investigation Articles Ontogeny of plasma proteins, albumin and binding of diazepam, cyclosporine, and deltamethrin Pankaj K. Sethi1,2, Catherine A. White1, Brian S. Cummings1, Ronald N. Hines3–5, Srinivasa Muralidhara1 and James V. Bruckner1 BACKGROUND: To characterize the ontogeny of plasma for example, have been attributed to significant elevations albumin and total proteins, due to the lack of a comprehensive in serum concentrations of unbound parent compound and pediatric database. Secondly, to establish the magnitude and N-desmethyldiazepam, its major active metabolite (7). duration of maturational changes in binding of highly-bound There are number of factors that influence plasma binding of drugs/chemicals. drugs and other chemicals, some of which can be age-related. METHODS: Anonymized plasma samples from 296 donors These include the drug and its concentration, the presence of were pooled in 6 age brackets from birth to adolescence. Total binding competitors, the type and quantity of plasma protein, protein and albumin levels were measured in each age group, and the proteins’ affinity for the drug. Nau et al. (7) observed a as was the age-dependency of plasma binding of diazepam twofold increase in the free fraction of diazepam in the serum (DZP), cyclosporine (CYC), and deltamethrin (DLM), a pyre- of neonates that accompanied marked increases in free fatty throid insecticide. acids and bilirubin, competitors for albumin-binding sites. RESULTS: Plasma levels of albumin and total proteins steadily Albumin levels progressively rose during a 6-d postgestation increased for the first 1–3 y of life. Unbound DZP and CYC monitoring period, but remained significantly lower than in fractions were elevated three- to fourfold in neonates, but adults. -
S-Layer Ultrafiltration Membranes
membranes Review S-Layer Ultrafiltration Membranes Bernhard Schuster * and Uwe B. Sleytr * Institute for Synthetic Bioarchitectures, Department of NanoBiotechnology, BOKU—University of Natural Resources and Life Sciences, Vienna, Muthgasse 11, 1190 Vienna, Austria * Correspondence: [email protected] (B.S.); [email protected] (U.B.S.) Abstract: Monomolecular arrays of protein subunits forming surface layers (S-layers) are the most common outermost cell envelope components of prokaryotic organisms (bacteria and archaea). Since S-layers are periodic structures, they exhibit identical physicochemical properties for each constituent molecular unit down to the sub-nanometer level. Pores passing through S-layers show identical size and morphology and are in the range of ultrafiltration membranes. The functional groups on the surface and in the pores of the S-layer protein lattice are accessible for chemical modifications and for binding functional molecules in very precise fashion. S-layer ultrafiltration membranes (SUMs) can be produced by depositing S-layer fragments as a coherent (multi)layer on microfiltration membranes. After inter- and intramolecular crosslinking of the composite structure, the chemical and thermal resistance of these membranes was shown to be comparable to polyamide membranes. Chemical modification and/or specific binding of differently sized molecules allow the tuning of the surface properties and molecular sieving characteristics of SUMs. SUMs can be utilized as matrices for the controlled immobilization of functional biomolecules (e.g., ligands, enzymes, antibodies, and antigens) as required for many applications (e.g., biosensors, diagnostics, enzyme- and affinity- membranes). Finally, SUM represent unique supporting structures for stabilizing functional lipid membranes at meso- and macroscopic scale. -
Membrane Filtration
Membrane Filtration A membrane is a thin layer of semi-permeable material that separates substances when a driving force is applied across the membrane. Membrane processes are increasingly used for removal of bacteria, microorganisms, particulates, and natural organic material, which can impart color, tastes, and odors to water and react with disinfectants to form disinfection byproducts. As advancements are made in membrane production and module design, capital and operating costs continue to decline. The membrane processes discussed here are microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO). MICROFILTRATION Microfiltration is loosely defined as a membrane separation process using membranes with a pore size of approximately 0.03 to 10 micronas (1 micron = 0.0001 millimeter), a molecular weight cut-off (MWCO) of greater than 1000,000 daltons and a relatively low feed water operating pressure of approximately 100 to 400 kPa (15 to 60psi) Materials removed by MF include sand, silt, clays, Giardia lamblia and Crypotosporidium cysts, algae, and some bacterial species. MF is not an absolute barrier to viruses. However, when used in combination with disinfection, MF appears to control these microorganisms in water. There is a growing emphasis on limiting the concentrations and number of chemicals that are applied during water treatment. By physically removing the pathogens, membrane filtration can significantly reduce chemical addition, such as chlorination. Another application for the technology is for removal of natural synthetic organic matter to reduce fouling potential. In its normal operation, MF removes little or no organic matter; however, when pretreatment is applied, increased removal of organic material can occur. -
Novel Antibiotics for Multidrug-Resistant Gram- Positive Microorganisms
Review Novel Antibiotics for Multidrug-Resistant Gram- Positive Microorganisms Despoina Koulenti 1,2,*, Elena Xu 1, Isaac Yin Sum Mok 1,†, Andrew Song 1,†, Drosos E. Karageorgopoulos 3, Apostolos Armaganidis 2, Jeffrey Lipman 1,4,5,‡ and SotiriosTsiodras 3,‡ 1 UQ Centre for Clinical Research, Faculty of Medicine, The University of Queensland, Brisbane, QLD 4072, Australia 2 2nd Critical Care Department, Attikon University Hospital, 12462 Athens, Greece 3 4th Department of Internal Medicine, Attikon University Hospital, 12462 Athens, Greece 4 Department of Intensive Care Medicine, Royal Brisbane and Women’s Hospital, 4029 Brisbane, Australia 5 Anesthesiology and Critical Care, Centre Hospitalier Universitaire De Nîmes (CHU), University of Montpellier, 30029 Nîmes, France * Correspondence: [email protected] † Equal contribution-both 3rd authors. ‡ They are joint senior authors. Received: 13 July 2019; Accepted: 15 August 2019; Published: 18 August 2019 Abstract: Increasing multidrug-resistance to Gram-positive pathogens, particularly to staphylococci, enterococci and streptococci, is a major problem, resulting in significant morbidity, mortality and healthcare costs. In recent years, only a small number of novel antibiotics effective against Gram-positive bacteria has been approved. This review will discuss the current evidence for novel branded antibiotics that are highly effective in the treatment of multidrug-resistant infections by Gram-positive pathogens, namely ceftobiprole, ceftaroline, telavancin, oritavancin, dalbavancin, tedizolid, besifloxacin, delafloxacin, ozenoxacin, and omadacycline. The mechanism of action, pharmacokinetics, microbiological spectrum, efficacy and safety profile will be concisely presented. As for any emerging antibiotic agent, resistance is likely to develop against these highly effective antibiotics. Only through appropriate dosing, utilization and careful resistance development monitoring will these novel antibiotics continue to treat Gram-positive pathogens in the future. -
Ultrafiltration 1 Basic Ideas
Ultrafiltration 1 Basic Ideas Ultrafiltration is a effective separation method for proteins Protein have two characteristics which are important for these separation Large molecules Conformation change with pH Osmotic Pressure Macromolecule is uncharged Macromolecule can not pass through the membrane Solvent flows from right to left, diluting the macromolecular sol’n As the dilution takes place, the sol’n vol. increases and the level in the capillary rises Figure 1. Osmosis pressure across a membrane. Solvent can diffuse across the membrane shown, but solute cannot. Ideal state μ = μ μ 0 : chemical potential in STP 2 ( pure) 2 (solution) 2 V : partial molar volume of solvent μ 0 + 0 = μ 0 + + 2 2 p V2 2 pV2 RT ln x2 x2 : mole fraction RT ΔΠ = − = − ΔΠ p p0 ln x2 : osmotic pressure V2 If the macromolecular sol’n is dilute, then we can expand the logarithm in term of x1 Dilute sol’n ΔΠ = − = − RT = − RT − p p0 ln x2 ~ ln(1 x1 ) V2 V2 RT ≅ − − − ≅ : Van’t Hoff’s Law ~ ( x1 ....) RTc1 V2 Side chain of Proteins Carboxylic acid ( - COOH ) : glutamic acid in basic sol’n to form carboxylate ( - COO- ) groups Amine ( - NH2 ) : lysine in acid sol’n to form ammonium ( - NH3+ ) groups A function of the pH of the sol’n : the relative amount of these positive and negative charges + - - Low pH : more -NH3 and -COOH, High pH : more -NH2 and -COO Figure 2. Charges on a protein. At low pH, amine side chains are protonated to give a positive charge ; at high pH, carboxylic side chain ionizeto give a negative charge. -
Lecture 10. Membrane Separation – Materials and Modules
Lecture 10. Membrane Separation – Materials and Modules • Membrane Separation • Types of Membrane • Membrane Separation Operations - Microporous membrane - Dense membrane • Membrane Materials • Asymmetric Polymer Membrane • Membrane Modules Membrane Separation • Separation by means of a semipermeable barrier (membrane) through which one or more species move faster than another or other species; rate-controlled separation • Characteristics - The two products are usually miscible - The separating agent is a semipermeable barrier - A sharp separation is often difficult to achieve History of Membrane Separation • Large-scale applications have only appeared in the past 60 years 235 238 - 1940s: separation of UF6 from UF6 (porous fluorocarbons) - 1960s: reverse osmosis for seawater desalinization (cellulose acetate), commercial ultrafiltration membranes - 1979: hollow-fiber membrane for gas separation (polysulfone) - 1980s: commercialization of alcohol dehydration by pervaporation • Replacement of more-common separations with membrane - Potential: save large amounts of energy - Requirements § production of high-mass-transfer-flux, defect-free, long-life membranes on a large scale § fabrication of the membrane into compact, economical modules of high surface area Characteristics of Membrane Separation • Distillation vs. gas permeation : energy of separation for distillation is usually heat, but for gas permeation is the shaft work of gas compression • Emerging (new) unit operation : important progress is still being made for efficient membrane