Aqueous Two-Phase Systems: Towards Novel and More Disruptive Applications
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Ultracentrifugation Techniques for the Ordering of Nanoparticles
nanomaterials Review Ultracentrifugation Techniques for the Ordering of Nanoparticles Xufeng Xu 1,† and Helmut Cölfen 2,* 1 Laboratory of Physical Chemistry, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612AE Eindhoven, The Netherlands; [email protected] 2 Physical Chemistry, University of Konstanz, Universitätsstraße 10, Box 714, 78457 Konstanz, Germany * Correspondence: [email protected] † Present address: Institute of Materials, École Polytechnique Fédérale de Lausanne, 1015 Lausanne, Switzerland. Abstract: A centrifugal field can provide an external force for the ordering of nanoparticles. Especially with the knowledge from in-situ characterization by analytical (ultra)centrifugation, nanoparticle ordering can be rationally realized in preparative (ultra)centrifugation. This review summarizes the work back to the 1990s, where intuitive use of centrifugation was achieved for the fabrication of colloidal crystals to the very recent work where analytical (ultra)centrifugation is employed to tailor-make concentration gradients for advanced materials. This review is divided into three main parts. In the introduction part, the history of ordering microbeads in gravity is discussed and with the size of particles reduced to nanometers, a centrifugal field is necessary. In the next part, the research on the ordering of nanoparticles in analytical and preparative centrifugation in recent decades is described. In the last part, the applications of the functional materials, fabricated from centrifugation-induced nanoparticle superstructures are briefly discussed. Keywords: centrifugation; sedimentation; nanoparticle; concentration gradient; non-equilibrium process; superstructure; functional material Citation: Xu, X.; Cölfen, H. Ultracentrifugation Techniques for 1. Introduction the Ordering of Nanoparticles. 1.1. The Era of Microbeads in Gravity Nanomaterials 2021, 11, 333. -
Continuous-Flow Centrifugation to Collect Suspended Sediment for Chemical Analysis
1 Table 6. Compounds detected in both equipment blank samples and not in corresponding source blank samples or at concentrations greater than two times the corresponding source blank sample concentration. Prepared in cooperation with the National Water Quality Monitoring Council and [Source data: Appendix A, table A1; Conn and Black (2014, table A4); and Conn and others (2015, table A11). CAS Registry Number: Chemical Abstracts Service Washington State Department of(CAS) Ecology Registry Number® (RN) is a registered trademark of the American Chemical Society. CAS recommends the verifi cation of CASRNs through CAS Client ServicesSM. Method: EPA, U.S. Environmental Protection Agency’s SW 846; SIM, select ion monitoring. Unit: µg/kg, microgram per kilogram; ng/kg, nanogram per kilogram. Sample type: River samples were from the Puyallup River, Washington. Q, qualifi er (blank cells indicate an unqualifi ed detection). J, estimated, result between the Continuous-Flow Centrifugationdetection level and reporting level; toNJ, result Collect did not meet all quantitation Suspended criteria (an estimated maxiumum possible concentration is reported in Result column) U, not detected above the reporting level (reported in the Result column); UJ, not detected above the detection level (reported in the Result column). Abbreviations: na, not Sediment for Chemicalapplicable; Analysis PCBs, polychlorinated biphenyls] Sample type Chapter 6 of CAS River River Commercial Commercial Section D, Water Quality Parameter name Registry Method Unit source equipment -
Hyphenating Chromatographic, Electrophoretic and On-Line Immobilized Enzymatic Strategies for Improved Oligonucleotide Analysis
Hyphenating chromatographic, electrophoretic and on-line immobilized enzymatic strategies for improved oligonucleotide analysis Thesis submitted to the Faculty of Science in fulfilment of the requirements for the degree of Doctor in Science (Chemistry) PIOTR WIKTOR ALVAREZ POREBSKI Promotor Prof. Dr. Frederic Lynen 2016 Table of contents Table of Contents TABLE OF CONTENTS…………………………………………….………………………………………….……………………………… I I GENERAL INTRODUCTION AND SCOPE ............................................................................................. 1 INTRODUCTION .................................................................................................................................. 1 SCOPE .............................................................................................................................................. 3 REFERENCES ...................................................................................................................................... 4 II PRINCIPLES OF THE SEPARATION TECHNIQUES USED IN OLIGONUCLEOTIDE ANALYSIS ................ 7 SUMMARY ............................................................................................................................................. 7 PRINCIPLES OF HIGH PERFORMANCE LIQUID CHROMATOGRAPHY (HPLC) ...................................................... 8 Ion exchange chromatography ........................................................................................... 10 Ion pair chromatography ................................................................................................... -
Nanosep® Centrifugal Devices - Protocols for Use Nanosep® Centrifugal Devices - Protocols for Use
Contact Us: www.pall.com/contact Nanosep® Centrifugal Devices - Protocols for Use Nanosep® Centrifugal Devices - Protocols for Use Ultrafiltration Fundamentals Purification and Handling of DNA Fragments PCR: Before and After Protein Purification and Handling Miscellaneous Protocols Appendices References Ordering Information Ultrafiltration Fundamentals Background Ultrafiltration (UF) is a membrane separation technique used to separate extremely small particles and dissolved molecules in fluids. The primary basis for separation is molecular size, although other factors such as molecule shape and charge can also play a role. Molecules larger than the membrane pores will be retained at the surface of the membrane (not in the polymer matrix as they are retained in microporous membranes) and concentrated during the ultrafiltration process. Compared to non-membrane processes (chromatography, dialysis, solvent extraction, or centrifugation), ultrafiltration: Is far gentler to the molecules being processed. Does not require an organic extraction which may denature labile proteins. Maintains the ionic and pH milieu. Is fast and relatively inexpensive. Can be performed at low temperatures (for example, in the cold room). Is very efficient and can simultaneously concentrate and purify molecules. The retention properties of ultrafiltration membranes are expressed as Molecular Weight Cutoff (MWCO). This value refers to the approximate molecular weight (MW) of a dilute globular solute (i.e., a typical protein) which is 90% retained by the membrane. However, a molecule’s shape can have a direct effect on its retention by a membrane. For example, linear molecules like DNA may find their way through pores that will retain a globular species of the same molecular weight. There are three generic applications for ultrafiltration: 1. -
Centrifugal Hyperfiltration
TO: Technology Innovation Program Mail Stop 4750 National Institute of Standards and Technology 100 Bureau Drive Gaithersburg, MD 20899-4750 FM: Dirk Forman 125 S. St. Louis Lafayette Louisiana 70506 [email protected] Centrifugal Hyperfiltration A means to economically recover resources from saltwater and wastewater streams with lower the energy cost of producing freshwater and potable water from marginalized water resources. Introduction Reverse Osmosis (RO) is a filtration process for the removal of ionic and organic pollutants from wastewater. Today’s technology of utilization of this filtration process is by large array of high-pressure piping and pressure pumps. This process yields low volumes of filtrated output (permeate), utilizes large areas for pipe array and components and the concentration polarization and membrane fouling hinders the wide application of RO filtration process. Utilizing centrifugal forces and cross flow membranes has potential to change the standard (RO) process to one of portable and high volume water purification. AN AREA OF CRITICAL NATIONAL NEED Ensuring Future Water Supply: As the Nation’s population and economy grow, greater demands are being placed on freshwater resources. At the same time, temporary or permanent drought conditions and water access rights affect regional freshwater availability. Water needs threaten to outstrip available freshwater, now and in the future. Emerging contaminants that must either be removed from distributed water or converted to harmless forms of waste is also pressuring water quality, both in terms of decontamination and disinfection of water supplies. Food contaminations are often traced back to water contaminations, either in the field or in processing. Municipal waste streams and irrigation runoff waste resources that are not recovered.1 Over 97 percent of the Earth's water -- seawater and brackish groundwater -- is too salty to use for drinking water or agriculture. -
Coagulation-Flocculation As a Submerged Biological Filter Pre-Treatment with Landfill Leachate
Coagulation-flocculation as a submerged biological filter pre-treatment with landfill leachate A. Gálvez Perez1,2, A. Ramos1,2,3, B. Moreno1,2,3 & M. Zamorano Toro1,2 1Department of Civil Engineering, Granada University, Spain 2MITA Research Group 3Institute of Water Research Abstract Landfill leachate may cause environmental problems if it is not properly managed and treated. An appropriate treatment process of landfill leachate often involves a combination of physical, chemical and biological methods to obtain satisfactory results. In this study, coagulation-flocculation was proposed as a pre- treatment stage of partially stabilized landfill leachate prior to submerged biological filters. Several coagulants (ferric, aluminium or organic) and flocculants (cationic, anionic or non-ionic) were assayed in jar-test experiments in order to determine optimum conditions for the removal of COD and total solids. Among the cationic flocculants, that of highest molecular weight and cationicity (CV/850) showed highest removal efficiencies (15% COD and 8% TS). Organic and aluminium coagulants showed better results than ferric coagulants. Coagulant removal efficiencies were between 9% and 17% for COD and between 10% and 15% for TS. Doses of 1 ml/l of coagulant were preferred. Some combinations of coagulant and flocculant enhanced the process. The best combinations obtained were FeCl3+A30.L, Ferriclar+A20.L, SAL8.2+A30.L and PAX-18+A30.L, which presented COD removal efficiencies between 24% and 37% with doses between 10 and 18 ml/l. Keywords: landfill leachate, coagulation-flocculation, submerged biological filter pre-treatment. Waste Management and the Environment II, V. Popov, H. Itoh, C.A. Brebbia & S. -
404 Sedimentation Handout
Sedimentation for Analysis and Separation of Macromolecules A ‘centrifugal force’ as experienced by particles in a centrifuge actually reflects the natural tendency of the particle to move in a straight line in the absence of external forces. If we view the experiment in the (fixed) reference frame of the laboratory, we observe that the particle is deflected from a linear trajectory by a centripetal force (directed toward the central axis of the rotor). However, when we consider the motion of the particle with respect to the (rotating) reference frame of the rotor, it appears that at any instant the particle experiences an outward or centrifugal force: Instantaneous Velocity (vtang) Centrifugal Acceleration Centripetal Acceleration As seen in laboratory As seen in (rotating) reference frame reference frame of rotor Ignoring buoyancy effects for the moment, the magnitude of the centrifugal force (which, in the rotating reference frame of the rotor, is as real as any other force) is m ⋅ v2 F = objecttan g =⋅mrω 2 centrif r object [1] where r is the distance from the axis of rotation, vtang is the linear velocity at any instant (in the direction perpendicular to the radial axis) and ω is the angular velocity (in radians sec-1 – note that 1 rpm = 2π///60 rad sec-1). The magnitude of this force can be compared to that of the gravitational force at the earth’s surface: Gm⋅()⋅() m = earth object Fgrav 2 re [2] -8 -1 3 -2 where G is the universal gravitational constant (= 6.67 x 10 g cm sec ) and re and me are the earth’s radius (= 6.37 x 108 cm) and mass (5.976 x 1027 g), respectively. -
Guide to Gel Filtration Or Size Exclusion Chromatography
Guide to Gel Filtration or Size Exclusion Chromatography www.harvardapparatus.com Table of Contents Introduction ........................................................................ 2-4 Size Fractionation .................................................................... 5 Buffer Sample Selection ........................................................ 6-7 Selection of Media and Size .................................................... 8 Gel Filtration SpinColumns .................................................... 9 Spehadex P-25 Applications .................................................. 10 Desalting Columns Applications ............................................ 11 P-2, P-6 and P-30 SpinColumns .......................................... 12 Ordering Information ............................................................ 13 Contact Information .............................................................. 14 Guide to Gel Filtration or Size Exclusion Chromatography 1 Introduction Gel Filtration Gel Filtration also called size-exclusion chromatography can be used for protein DNA purification, buffer exchange, desalting, or for group separation in which the sample is separated in two major groups. Gel Filtration is an easy to use method for separation of molecules with different molecular sizes, using mild conditions. Gel Filtration uses the size of molecules in solution to determine separation. SpinColumns have short media packing so the samples are separated by size, the large molecules travel out of the column with the void -
PROTEIN a CHROMATOGRAPHY – the PROCESS ECONOMICS DRIVER in Mab MANUFACTURING
PROCESS Application Note PROTEIN A CHROMATOGRAPHY – THE PROCESS ECONOMICS DRIVER IN mAb MANUFACTURING THE OPTIMIZATION OF THE PROTEIN A CAPTURE STEP IN DOWNSTREAM PROCESSING PLATFORMS CAN CONSIDER- ABLY IMPROVE PROCESS EFFICIENCY AND ECONOMICS OF INDUSTRIAL ANTIBODY MANUFACTURING. PARAMETERS LIKE RESIN REUSE AND ITS CAPACITY CONTRIBUTE CONSIDERABLY TO THE PRODUCTION COSTS. THE USE OF A HIGH CAPACITY PROTEIN A RESIN CAN IMPROVE THE PROCESS EFFICIENCY AND ECONOMICS. THIS PAPER PRESENTS THE KEY FEATURES OF A NEW CAUSTIC STABLE PROTEIN A RESIN PROVIDING EXTREMELY HIGH IgG BINDING CAPACITIES. Biopharmaceuticals represent an ever growing important Protein A affinity resins are dominating the Cost of Goods part of the pharmaceutical industry. The market for recom- (COGs) of mAb manufacturing. Bioreactors at the 10.000 L binant proteins exceeded $ 100 billion in 2011 with a scale operating at a titer of about 1g/L typically generate contribution of 45% sales by monoclonal antibodies (mAbs) costs of $ 4-5 million (2). Therefore the Protein A capturing (1). The introduction of the first mAb biosimilars in Europe step is the key driver to improve process economics. Besides raised the competitive pressure in an increasingly crowded the capacity of the resin, life time and cycle numbers market place. The industry faces challenges, such as patent significantly contribute to the production costs in mAb expirations accompanied by approvals of corresponding manufacturing. biosimilars, failures in clinical trials/rejections or the refusal of health insurers to pay for new drugs. Today, the IgG binding capacities of most Protein A resins are in the range of 30-50 g/L, offering significant advantages These challenges force the industry to minimize risk and time- for the processing of high-titer feedstreams when compared to-market and to proceed more cautiously. -
Integrated Leaching and Separation of Metals Using Mixtures of Organic Acids and Ionic Liquids
molecules Article Integrated Leaching and Separation of Metals Using Mixtures of Organic Acids and Ionic Liquids Silvia J. R. Vargas, Helena Passos , Nicolas Schaeffer * and João A. P. Coutinho CICECO-Aveiro Institute of Materials, Department of Chemistry, University of Aveiro, 3810-193 Aveiro, Portugal; [email protected] (S.J.R.V.); [email protected] (H.P.); [email protected] (J.A.P.C.) * Correspondence: nicolas.schaeff[email protected] Academic Editors: Magdalena Regel-Rosocka and Isabelle Billard Received: 4 November 2020; Accepted: 25 November 2020; Published: 27 November 2020 Abstract: In this work, the aqueous phase diagram for the mixture of the hydrophilic tributyltetradecyl phosphonium ([P44414]Cl) ionic liquid with acetic acid (CH3COOH) is determined, and the temperature dependency of the biphasic region established. Molecular dynamic simulations of the [P44414]Cl + CH3COOH + H2O system indicate that the occurrence of a closed “type 0” biphasic regime is due to a “washing-out” phenomenon upon addition of water, resulting in solvophobic segregation of the [P44414]Cl. The solubility of various metal oxides in the anhydrous [P44414]Cl + CH3COOH system was determined, with the system presenting a good selectivity for CoO. Integration of the separation step was demonstrated through the addition of water, yielding a biphasic regime. Finally, the [P44414]Cl + CH3COOH system was applied to the treatment of real waste, NiMH battery black mass, being shown that it allows an efficient separation of Co(II) from Ni(II), Fe(III) and the lanthanides in a single leaching and separation step. Keywords: critical metals; process intensification; metal leaching; solvent extraction; solvometallurgy 1. Introduction Solvometallurgy, the extraction of metals from primary and secondary sources using solutions containing less than 50 vol. -
(12) United States Patent (10) Patent No.: US 8,685,240 B2 Malik Et Al
USOO8685240B2 (12) United States Patent (10) Patent No.: US 8,685,240 B2 Malik et al. (45) Date of Patent: Apr. 1, 2014 (54) HIGH EFFICIENCY SOL-GEL GAS (56) References Cited CHROMATOGRAPHY COLUMN (75) Inventors: Abdul Malik, Tampa, FL (US); Abuzar U.S. PATENT DOCUMENTS Kabir, Tampa, FL (US); Chetan 3,722,181 A 3/1973 Kirkland et al. Shende, Vernon, CT (US) 3,954,651 A 5, 1976 Donike (73) Assignee: University of South Florida, Tampa, FL (Continued) (US) (*) Notice: Subject to any disclaimer, the term of this FOREIGN PATENT DOCUMENTS patent is extended or adjusted under 35 EP O315633 B1 10, 1991 U.S.C. 154(b) by 1875 days. EP O537851. B1 3/1996 (21) Appl. No.: 11/599,497 (Continued) (22) Filed: Nov. 13, 2006 OTHER PUBLICATIONS (65) Prior Publication Data Aichholz, R., “Preparation of Glass Capillary Columns Coated with US 2007/OO62874 A1 Mar. 22, 2007 OH-Terminated (3,3,3-Trifluoropropyl) Methyl Polysiloxane (PS Related U.S. Application Data 184.5), Journal of High Resolution Chromatography, 13, 71-73 1990). (63) Continuation of application No. 10/471.388, filed as ( ) application No. PCT/US02/07163 on Mar. 8, 2002, (Continued) now abandoned. (60) Provisional application No. 60/274,886, filed on Mar. Primary Examiner — Ernest G. Therkorn 9, 2001. (74) Attorney, Agent, or Firm — Saliwanchik, Lloyd & (51) Int. Cl. Eisenschenk BOI 20/285 (2006.01) BOI 20/28 (2006.01) (57) ABSTRACT BOLD 5/26 (2006.01) A capillary column (10)includes a tube structure having inner GOIN3/56 (2006.01) walls (14) and a sol-gel Substrate (16) coated on a portion of GOIN3O/60 (2006.01) inner walls (14) to form a stationary phase coating (18) on (52) U.S. -
A Basic Chloride Method for Extracting Aluminum from Clay
(k Bureau of Mines Report of investigations/l984 A Basic Chloride Method for Extracting Aluminum From Clay By P. R. Bremner, L. J. Nicks, and D. J, Bauer UNITED STATES DEPARTMENT OF THE INTERIOR Report of Investigations 8866 A Basic Chloride Method for Extracting Aluminum From Clay By P. R. Bremner, L. J. Nicks, and D. J. Bauer UNITED STATES DEPARTMERIT OF THE INTERIOR William P. Clark, Secretary BUREAU OF MINES Robert C. Worton, Director Library of Congress Cataloging in Publication Data: Bremner, P, R. (Paul R,) A basic chloride method for extracting aluminum from clay. (Bureau of Mines report of investigations ; 8866) Bibliography: p. 8. Supt. of Docs. no.: I 28.23:8866. 1. Alumit~urn-Metallurgy. 2. Leaching. 3. Chlorides. 4, Kao- linite, I. Nicks, 1;. J. (Larry J.), 11. Bauer, D. J. (Donald J,). 111. Title. IV. Series: Report of investigations (United States. Bureau of TN23.U43 [TN776] 622s [669'.722] 84-600004 CONTENTS .Page Abstract ....................................................................... 1 Introduction ................................................................... 2 Materials. equipment. and procedures .......O.O...........,............... 3 Results and discussion........................................................b 3 Effects of calcination time and temperature .................................. 3 Single-stage leaching and crystallization... ................................. 4 Countercurrent leaching and crystallization.................................. 5 Purification and solubility studies ........................*................