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United States Patent 19 11 Patent Number: 5,418,243 Angerbauer Et Al
USOO5418243A United States Patent 19 11 Patent Number: 5,418,243 Angerbauer et al. 45 Date of Patent: May 23, 1995 54 SUBSTITUTED 4-PHENYL-PYRIDONES 4,215,126 7/1980. Durant et al........................ 514/345 AND 4-PHENYL-3-ALKOXYPYRIDNES 4,684,477 8/1987 Sugimori et al. ... 546/290 4,916,239 4/1990 Treiber ................. ... 549/292 75 Inventors: Rolf Angerbauer; Peter Fey; Walter 4,988,711 1/1991 Angerbauer et al. ... 514/326 Hibsch, all of Wuppertal; Thomas 5,032,602 7/1991 Fey et al. ................. ... 54/345 Philipps, Cologne; Hilmar Bischoff, 5,064,841 11/1991 Angerbauer et al. ... 514/336 Wuppertal; Hans-Peter Krause, 5,138,090 8/1992 Fey et al. .............................. 560/59 Schwelm; Jörg Peterson-von Gehr, Bochum; Delf Schmidt, Wuppertal, FOREIGN PATENT DOCUMENTS all of Germany 0373423 6/1990 European Pat. Off. 73 Assignee: Bayer Aktiengesellschaft, OTHER PUBLICATIONS Leverkusen, Germany J. Med. Chem., 1990, vol. 33, pp. 52-60; “Synthesis and 21) Appl. No.: 166,775 Biological Activity of New HGM-CoA Reductase 22 Filed: Dec. 14, 1993 Inhibitors ... ', G. Beck. Primary Examiner-C. Warren Ivy (30) Foreign Application Priority Data Assistant Examiner-A. A. Owens Dec. 21, 1992 DE Germany ........................ 4243 278.2 Attorney, Agent, or Firm-Sprung, Horn, Kramer & Jun. 28, 1993 DE Germany ........................ 43 21421.5 Woods 511 Int. Cl...................... A61K 31/44; C07D 213/64 57 ABSTRACT 52 U.S. C. ...................................... 514/345; 546/24; 546/290; 514/89 Substituted 4-phenyl-pyridones and 4-phenyl-2-alkox 58 Field of Search .................. 546/290, 24; 514/345, ypyridines are prepared by reducing corresponding 514/89 4-phenyl-pyridone and 4-phenyl-2-alkoxypyridine de rivatives. -
SAFETY DATA SHEET Electrolyte Licl 1 Mol/L in Ethanol
SAFETY DATA SHEET according to Regulation (EU) No. 453/2010 Electrolyte LiCl 1 mol/l in ethanol 1. Identification of the substance/mixture and of the company/undertaking 1.1. Product identifier Product code 51350088, 51343183 Synonyms None. 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the Laboratory chemicals Substance/Preparation 1.3. Details of the supplier of the safety data sheet Company/Undertaking Mettler-Toledo AG Identification ANALYTICAL Sonnenbergstrasse 74 CH-8603 Schwerzenbach Schweiz Tel: +41-44-806-77-11 Fax: +41-44-806-73-50 Email: [email protected] 1.4. Emergency telephone +41-44-251 51 51 (Tox Center) number Revision Date 07.03.2014 Version GHS 1 2. Hazards identification 2.1. Classification of the substance or mixture Electrolyte LiCl 1 mol/l in ethanol (9830) V. GHS 1 / 07.03.2014 Print Date 28.03.2014 Page 1/10 Classification according to Flammable liquids, Cat. 2, H225 Regulation (EC) No. 1272/2008 (GHS/CLP) The product is classified and labelled according to Regulation (EC) No. 1272/2008 (GHS/CLP). Classification according to EU F; R11 Directives 67/548/EEC or 1999/45/EC Additional information For the full text of the phrases mentioned in this Section, see Section 16. 2.2. Label elements F Signal Word Danger Hazard Statements H225: Highly flammable liquid and vapour. Precautionary statements P210b: Keep away from heat, hot surfaces, sparks, open flames and other ignition sources. No smoking. P243: Take precautionary measures against static discharge. P280: Wear protective gloves/ protective clothing/ eye protection/ face protection. -
Separation of Water out of Highly Concentrated Electrolyte Solutions Using Multistage Vacuum Membrane Distillation
Separation of water out of highly concentrated electrolyte solutions using multistage vacuum membrane distillation Bin Jiang Master of Science Thesis KTH School of Industrial Engineering and Management Energy Technology EGI-2013-082MSC EKV967 Division of Heat and Power SE-100 44 STOCKHOLM Master of Science Thesis EGI-2013-082MSC EKV967 Separation of water out of highly concentrated electrolyte solutions using multistage vacuum membrane distillation Bin Jiang Approved Examiner Supervisor 26.09.2013 Andrew Martin Daniel Minilu Woldemariam Commissioner Contact person Abstract Absorption dehumidification requires regeneration system to regenerate diluted desiccant solutions, which are still highly concentrated. A novel multi-stage vacuum membrane distillation system was applied for separating water out of the highly concentrated solution. The performance of this novel membrane distillation system with high concentration solution is studied, as well as the effect of solution concentration, heating temperature and feed flow rate on concentration increase, permeate flux and specific energy consumption was studied. Feed solutions are LiCl solution (22-30 wt%) and CH3COOK solution (50-60 wt%).Other experimental parameters studied were: heating temperature, 70-80 °C, feed flow rate, 1.2-2.0 l/min. Response surface method is applied for model building, in order to provide a better understanding of the interactions between different parameters. Compared with pure water, high concentration solution has lower vapor pressure, which leads to lower permeate flux. The highest concentration the system can reach is 36.5 wt% for LiCl solution and over 70 wt% for CH3COOK solution, when the heating temperature is 80 °C. Lower concentration and higher heating temperature will result in larger increase in concentration, higher permeate flux and also lower specific energy consumption. -
A Study of Lithium Precursors on Nanoparticle Quality
Electronic Supplementary Material (ESI) for Nanoscale. This journal is © The Royal Society of Chemistry 2021 Electronic Supplementary Information Elucidating the role of precursors in synthesizing single crystalline lithium niobate nanomaterials: A study of lithium precursors on nanoparticle quality Rana Faryad Ali, Byron D. Gates* Department of Chemistry and 4D LABS, Simon Fraser University, 8888 University Drive Burnaby, BC, V5A 1S6, Canada * E-mail: [email protected] This work was supported in part by the Natural Sciences and Engineering Research Council of Canada (NSERC; Grant No. RGPIN-2020-06522), and through the Collaborative Health Research Projects (CHRP) Partnership Program supported in part by the Canadian Institutes of Health Research (Grant No. 134742) and the Natural Science Engineering Research Council of Canada (Grant No. CHRP 462260), the Canada Research Chairs Program (B.D. Gates, Grant No. 950-215846), CMC Microsystems (MNT Grant No. 6345), and a Graduate Fellowship (Rana Faryad Ali) from Simon Fraser University. This work made use of 4D LABS (www.4dlabs.com) and the Center for Soft Materials shared facilities supported by the Canada Foundation for Innovation (CFI), British Columbia Knowledge Development Fund (BCKDF), Western Economic Diversification Canada, and Simon Fraser University. S1 Experimental Materials and supplies All chemicals were of analytical grade and were used as received without further purification. Niobium ethoxide [Nb(OC2H5)5, >90%] was obtained from Gelest Inc., and benzyl alcohol (C7H7OH, 99%) and triethylamine [N(C2H5)3, 99.0%] were purchased from Acros Organics and Anachemia, respectively. Lithium chloride (LiCl, ~99.0%) was obtained from BDH Chemicals, and lithium bromide (LiBr, ≥99.0%), lithium fluoride (LiF, ~99.9%), and lithium iodide (LiI, 99.0%) were purchased from Sigma Aldrich. -
Introduction Part I. Electrolysis of Lithium Chloride in Pyridine
DECOMPOSITION CURVES OF LITHIUM CHLORIDE IN PYRIDINE AND IN ACETONE-.'I"E EFFECT OF WATER BY HARRISON EASTMAN PATTEN AND WILLIAM ROY MOTV Introduction Lithium chloride is soluble in a number of organic liquids, and thus affords ready means for studying the effect of change in solvent upon the process of electrolysis. In the deposition of lithium from its chloride in a series of alcohols' we have considered only a simple solvent. This paper takes account of the influence of moisture on the electrolysis of lithium chloride in pyridine and in acetone, starting with the anhy- drous solvents. Part I. Electrolysis of Lithium Chloride in Pyridine During the electrolysis of a pyridine solution of lithium chloride in an open cell,s there is a marked increase in the cell resistance. Thus, in a series of decomposition-curve determinations, polarization values for the total cell ranged from 4.00' volts4 to 2.70 volts, and in sonie instances a rise of ten to a hundred fold was observed in the cell resistance. A preliminary attempt to take anode and cathode curves gave a polarization of 1.6 volts at the anode, and $0.4 volt at the cathode. As these solutions were not strictly anhydrous, it seemed advisable to study the effect of water. So several solutions were made up with great care to exclude moisture, This work was carried out in the laboratories of physical chemistry and of applied electrochemistry at the University of Wisconsin, and the authors wish to express their appreciation of the courtesy extended to them by Professor I,. -
Vapor-Liquid Equilibrium Data for the System Acetone-Methanol Saturated with Salts"
VAPOR-LIQUID EQUILIBRIUM DATA FOR THE SYSTEM ACETONE-METHANOL SATURATED WITH SALTS" SHUZO OHE, KIMIHIKO YOKOYAMA, AND SHOICHI NAKAMURA Ishikazvajima-Harima Heavy Industries Co., Ltd. Research Institute, Yokohama Vapor-liquid equilibrium data at atmospheric pressure of the system : acetone-methanol-salt are studied. The Salts, Kl, NaCI, MgCI2, CaCI2/ LiCI, and CaBr2 are examined to observe the salt effect on the acetone-methanol system. Effective salts are CaQ2, LiC! and CaBr2, which are more soluble in methanol than Kl, NaCI and MgCh. CaCI2, LiCI and CaBr2 are observed to shift the azeotropic composition from 8O.I to 88.6, 9I-O and 94.O mole /# of acetone, respectively. The salt effect at each infinite dilute concentration of acetone and methanol increases with the increasing solubility of each salt in the rich concentration component. In general, salts shift azeotropic compositions or 2) Experimental method eliminate azeotropes. For example, sodium chloride The salt, being completely non-volatile, appears only saturated in ethanol-water system shifts the azeotropic in the liquid, hence yielding a system consisting of composition from 87 to over 90 mole %ethanol45 and a two-componentvapor phase and a three-component calcium chloride saturated in the ethanol-water system liquid phase. The concentrations of acetone and eliminates the azeotrope25. This salt effect may be used for the separation of azeotropic mixtures. Systems which contain water as one component have been well studied5>9>10), but studies on non-aqueous systems are scarce from the point of salt effect. L. Belcku studied the effect of calcium chloride on the acetone-methanol system and reported on a constant concentration of 2.3 moles of salt/mole of solution. -
POLAROGRAPHIC S'ludies of LEAD in METHANOL SOLUTIONS
POLAROGRAPHIC S'lUDI ES OF LEAD IN METHANOL SOLUTIONS ii By BIH'I' i\LLIE30N., JB.. Bachelor of. Science r:;;:u:rt. Ce:ntral State College Ada, Oltlahvrna 1947 Subiui.tted to the Depa.rfa:i1r.mt of Che11ri.stry Oklahoma. 11.g:dcultural and 1°Iecharrlcal College In Partial F'ulfilh1e:nt of the Requirements F'or '/:.he Degree of 1950 iii OKLAHOMA AGRICULTURAL & MECHANICAL COLLEGI APPRov:o;n BY: LIBRARY APR 241950 Chair.nan, Thesis Committee r-iember of the Thesis Committee 250906 iv 'l'he author ·,-s;ishes to acl.:nmdodge the 1:.dvice and gu:l.d<2.nce of Dr. Paul Acknowledgment is also made of the unn;y helpful sugg0stions and cordial coope:raticn of tho other faculty nombors of tho i;l10w.istr;y :;.,ovu:ctment. '£he author &\ih,h,:;s to express his sincere apr,rcciatiun tu the Che.wistry Deparl.imant. of Oklaho;m l:,.r:;r.lcult,,~i.rnl and 1-~echaniciol.l Colle,G;e f0r finru,d.al this invest:1gatiou. V TABLE CF COW'fI3IJTS HISTORICAL • • .. l '.EE'l'.i'iDDUCTION ·•. 4 . ·-· • • • 15 .. • 17 Instrumental Procedure • • • • 17 Reagents • 17 Results and Conclusions • • 19 Appearance B.nd Interpreta.tiot, of a Second Lead 't"Jave 33 SU]}IARY • • 44 BIBLIOG;tAPHY • .. • 47 BIOGRAPHY •. • • • • • • • l~9 l HISTO CAL In 1903 Kucer 1 constructed a dropping ercury electr for the pur se of studying the el ctroc pillary curve of ereury in various electrolyte solutions, this typ of electrode being especialJ.y convenient for the termination of the surface tension of rcury under various conditions. -
Beryllium Chloride Apparatus. Figure M
Durham E-Theses Organic and hydride chemistry of beryllium Bell, N.A How to cite: Bell, N.A (1964) Organic and hydride chemistry of beryllium, Durham theses, Durham University. Available at Durham E-Theses Online: http://etheses.dur.ac.uk/8894/ Use policy The full-text may be used and/or reproduced, and given to third parties in any format or medium, without prior permission or charge, for personal research or study, educational, or not-for-prot purposes provided that: • a full bibliographic reference is made to the original source • a link is made to the metadata record in Durham E-Theses • the full-text is not changed in any way The full-text must not be sold in any format or medium without the formal permission of the copyright holders. Please consult the full Durham E-Theses policy for further details. Academic Support Oce, Durham University, University Oce, Old Elvet, Durham DH1 3HP e-mail: [email protected] Tel: +44 0191 334 6107 http://etheses.dur.ac.uk ORGANIC AND HYDRIDE CHEMISTRY OF BERYLLIUM oy N.A. BELL. A thesis.submitted for the Degree of Doctor of Philosophy in the University- of Durham. June 196^-. I Acknowledgements. The author wishes to express his sincere thanks to Professor G-.E. Coates, M.A., D.Sc., F.R.I.C., under whose direction this research was carried out, for his constant encouragement and extremely valuable advice. ' The author is also indebted to the Department of Scien• tific and Industrial Research for a Research StudiSntshrp. I I Memorandum. The work described in this thesis was carried out in the University of Durham between September 19b1 and May 196A-. -
Purification of REPLI-G® Amplified DNA by Licl/Etoh Precipitation
QIAGEN Supplementary Protocol Purification of REPLI-g® amplified DNA by LiCl/EtOH precipitation This protocol is designed for the purification of 5–40 μg DNA amplified using the REPLI-g Single Cell Kit (cat. nos. 150343 and 150345), REPLI-g WTA Single Cell Kit (cat. nos. 150063 and 150065), or the REPLI-g Cell WGA & WTA Kit (cat. nos. 150052 and 150054) by lithium chloride/ethanol precipitation. Product use limitations REPLI-g Kits are intended for molecular biology applications. These products are not intended for the diagnosis, prevention, or treatment of a disease. All due care and attention should be exercised in the handling of the products. We recommend all ® users of QIAGEN products to adhere to the NIH guidelines that have been developed for recombinant DNA experiments, or to other applicable guidelines. Equipment and reagents to be supplied by user When working with chemicals, always wear a suitable lab coat, disposable gloves, and protective goggles. For more information, consult the appropriate safety data sheets (SDSs), available from the product supplier. 1.5 or 2 ml microcentrifuge tubes Microcentrifuge Pipet tips (pipet tips with aerosol barriers for preventing cross-contamination are recommended) TE buffer (10 mM Tris·Cl; 1 mM EDTA, pH 8.0) Ethanol (96–100%) Ethanol (70%) Lithium chloride (7.5 M) EDTA (0.5 M, pH 8.0) Sample & Assay Technologies Important points before starting All centrifugation steps should be performed at room temperature (15–25°C). Wear gloves throughout the entire procedure. In case of contact between gloves and sample, change gloves immediately. Procedure 1. After the REPLI-g reaction, equilibrate REPLI-g amplified DNA to room temperature (15–25°C) for no longer than 10 min. -
Sodium Aluminum Hydride
Sodium aluminum hydride sc-251007 Material Safety Data Sheet Hazard Alert Code Key: EXTREME HIGH MODERATE LOW Section 1 - CHEMICAL PRODUCT AND COMPANY IDENTIFICATION PRODUCT NAME Sodium aluminum hydride STATEMENT OF HAZARDOUS NATURE CONSIDERED A HAZARDOUS SUBSTANCE ACCORDING TO OSHA 29 CFR 1910.1200. NFPA FLAMMABILITY3 HEALTH3 HAZARD INSTABILITY1 W SUPPLIER Santa Cruz Biotechnology, Inc. 2145 Delaware Avenue Santa Cruz, California 95060 800.457.3801 or 831.457.3800 EMERGENCY: ChemWatch Within the US & Canada: 877-715-9305 Outside the US & Canada: +800 2436 2255 (1-800-CHEMCALL) or call +613 9573 3112 SYNONYMS Al-H4.Na, "aluminate (1-), tetrahydro-, sodium", "aluminum sodium hydride", "sodium aluminium tetrahydride", "sodium tetrahydroaluminate (1-)" Section 2 - HAZARDS IDENTIFICATION CHEMWATCH HAZARD RATINGS Min Max Flammability: 3 Toxicity: 2 Body Contact: 3 Min/Nil=0 Low=1 Reactivity: 1 Moderate=2 High=3 Chronic: 2 Extreme=4 CANADIAN WHMIS SYMBOLS 1 of 7 EMERGENCY OVERVIEW RISK Contact with water liberates extremely flammable gases. Harmful if swallowed. Causes burns. Risk of serious damage to eyes. Highly flammable. POTENTIAL HEALTH EFFECTS ACUTE HEALTH EFFECTS SWALLOWED ! The material can produce chemical burns within the oral cavity and gastrointestinal tract following ingestion. ! Accidental ingestion of the material may be harmful; animal experiments indicate that ingestion of less than 150 gram may be fatal or may produce serious damage to the health of the individual. EYE ! The material can produce chemical burns to the eye following direct contact. Vapors or mists may be extremely irritating. ! If applied to the eyes, this material causes severe eye damage. SKIN ! The material can produce chemical burns following direct contactwith the skin. -
Experimental Setup for Determining Ammonia-Salt Adsorption And
Experimental setup for determining ammonia-salt adsorption and desorption behaviour under typical heat pump conditions: a description of the setup and experimental results Michel van der Pal Robert de Boer Jakobert Veldhuis Simon Smeding This paper will be presented at the ISHPC conference 2011, April 5-7 2011, Padua, Italy ECN-M--11-030 MARCH 2011 EXPERIMENTAL SETUP FOR DETERMINING AMMONIA- SALT ADSORPTION AND DESORPTION BEHAVIOR UNDER TYPICAL HEAT PUMP CONDITIONS: A DESCRIPTION OF THE SETUP AND EXPERIMENTAL RESULTS Michel van der Pala, Robert de Boera, Jakobert Veldhuisa, Simon Smedinga a Energy research Centre of the Netherlands (ECN), P.O. Box 1, 1755 ZG, Petten, [email protected] ABSTRACT Heat-driven heat pumps based on the principle of chemisorption have been researched worldwide. Such research typically focuses either on fundamental materials properties such as sorption isotherms, thermal conductivity and heat of sorption, or on the development and performance of complete systems. Also at ECN the research shows this typical pattern with publications on the fundamental thermodynamic properties on ammonia reactions of lithium chloride and magnesium chloride (Bevers et al., 2006; Bevers et al., 2007) together with results on complete systems (Haije et al., 2007; van der Pal et al., 2009). However, when trying to connect the material properties to the system’s performance, for example by using model calculations, various uncertainties on heat exchanger/sorption reactor level remain. These uncertainties, such as reaction kinetics, heat and mass transfer limitations for given specific geometries and conditions but also effects due to repeated sorption, pose a considerable problem for further development, improvement and scaling up of the system. -
A Review on the Separation of Lithium Ion from Leach Liquors of Primary and Secondary Resources by Solvent Extraction with Commercial Extractants
processes Article A Review on the Separation of Lithium Ion from Leach Liquors of Primary and Secondary Resources by Solvent Extraction with Commercial Extractants Thi Hong Nguyen 1,2 and Man Seung Lee 1,* 1 Department of Advanced Materials Science & Engineering, Institute of Rare Metal, Mokpo National University, Jeollanamdo 534-729, Korea; [email protected] 2 College of Natural Sciences, Can Tho University, Can Tho City 900000, Viet Nam * Correspondence: [email protected]; Tel.: +82-61-450-2492 Received: 10 April 2018; Accepted: 9 May 2018; Published: 12 May 2018 Abstract: The growing demand for lithium necessitates the development of an efficient process to recover it from three kinds of solutions, namely brines as well as acid and alkaline leach liquors of primary and secondary resources. Therefore, the separation of lithium(I) from these solutions by solvent extraction was reviewed in this paper. Lithium ions in brines are concentrated by removing other metal salts by crystallization with solar evaporation. In the case of ores and secondary resources, roasting followed by acid/alkaline leaching is generally employed to dissolve the lithium. Since the compositions of brines, alkaline and acid solutions are different, different commercial extractants are employed to separate and recover lithium. The selective extraction of Li(I) over other metals from brines or alkaline solutions is accomplished using acidic extractants, their mixture with neutral extractants, and neutral extractants mixed with chelating extractants in the presence of ferric chloride (FeCl3). Among these systems, tri-n-butyl phosphate (TBP)- methyl isobutyl ketone (MIBK)-FeCl3 and tri-n-octyl phosphine oxide (TOPO)- benzoyltrifluoroacetone (HBTA) are considered to be promising for the selective extraction and recovery of Li(I) from brines and alkaline solutions.