Calcium Chloride
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1 the Volumetric Determination of Hydroxylamine
VOLUMETRIC DETERMINATION OF HYDROXYLAMINE. I363 [CONTRIBUTION FROM THE CHEMICAL LABORATORYOF THE UNIVERSITY OF CALIFORNIA.1 THE VOLUMETRIC DETERMINATION OF HYDROXYLAMINE. BY WILLIAMC. BRAY,MIBUM E. SIMPSONAND ANNA A. MACKENZIE. Received July 17, 1919 In the present investigation 3 volumetric methods of determining hydroxylamine in aqueous solution have been studied : The titanous salt method,' in which the hydroxylamine is reduced by excess titanous salt in acid solution with exclusion of air, and the excess titrated with permanganate. 2NH20H + Ti2(S04)3 = (NH4)2S04 + 4TiOS04 + HzS04. (I) The ferric salt method,2 in which the hydroxylamine is oxidized in an acid solution by excess of a ferric salt, the mixture is boiled and the fer- rous salt formed titrated with permanganate. 2NH20H + 2Fe@04)3 = N2O + 4FeS04 + 2H2S04 + H20. (2) The iodine method,3 in which the hydroxylamine is oxidized by iodine in a neutral solution, e. g., in the presence of disodium phosphate. 2NH20H + 212 = N2O + 4HI + H2O (3) or 2NH20H + 213- = N20 + 61- + 4H+ + HzO. Our first experiments, with the iodine method, yielded irregular results which could not be interpreted until the concentration of the hydroxyl- amine solution was accurately determined. An examination of the literature showed a rather unsatisfactory state of affairs. The advocates of the ferric sulfate method furnish evidence that it is perfectly reliable, but Leuba4 gives detailed experimental data to prove the contrary, and Adams5 states that he could not obtain reproducible results with it. The investigators who have used the iodine method consider it to be fairly satisfactory, but some of them state that it is not very accurate, and Rupp and Maeder6 have recently concluded that correct results are obtained only by a compensation of errors. -
A Fundamental Evaluation of the Atmospheric Pre-Leaching Section of the Nickel-Copper Matte Treatment Process
A FUNDAMENTAL EVALUATION OF THE ATMOSPHERIC PRE-LEACHING SECTION OF THE NICKEL-COPPER MATTE TREATMENT PROCESS by RODRICK MULENGA LAMYA Dissertation presented for the Degree of DOCTOR OF PHILOSOPHY (Extractive Metallurgical Engineering) in the Department of Process Engineering at the University of Stellenbosch, South Africa Promoter Prof. L. Lorenzen STELLENBOSCH March 2007 DECLARATION I the undersigned, hereby declare that the work contained in this dissertation is my own original work and that I have not previously in its entirety or in part submitted it at any university for a degree. Signature: ............................................... Date: ....................................................... Copyright © 2007 Stellenbosch University All rights reserved i SYNOPSIS Nickel-Copper sulphide ores are the most important Platinum Group Metal bearing ores. The South African deposits are exceptionally rich in the platinum group metals (PGMs) and production of the PGMs is the primary purpose of treating these ores. The methods used in the recovery of the PGMs from the nickel-copper ores generally consists of ore concentration by physical techniques, pyrometallurgical concentration and hydrometallurgical extraction of the base metals followed by the PGMs. Pyrometallurgical concentration produces Ni-Cu matte, which is treated by hydrometallurgical processes to recover the nickel, copper, cobalt and the precious metals. In this study, the leaching behaviour of a Ni–Cu matte in CuSO4–H2SO4 solution during the repulping (pre-leach) stage at Impala Platinum Refineries was studied. The repulping stage is basically a non–oxidative atmospheric leach stage, in which nickel, iron and cobalt are partially dissolved, while the copper is precipitated. To understand the nature of the leaching process during this stage of the base metal refining operation, the effects of variations in the key process variables such as temperature, stirring rate, particle size, pulp density, residence time, initial copper and acid concentrations were investigated. -
1 Abietic Acid R Abrasive Silica for Polishing DR Acenaphthene M (LC
1 abietic acid R abrasive silica for polishing DR acenaphthene M (LC) acenaphthene quinone R acenaphthylene R acetal (see 1,1-diethoxyethane) acetaldehyde M (FC) acetaldehyde-d (CH3CDO) R acetaldehyde dimethyl acetal CH acetaldoxime R acetamide M (LC) acetamidinium chloride R acetamidoacrylic acid 2- NB acetamidobenzaldehyde p- R acetamidobenzenesulfonyl chloride 4- R acetamidodeoxythioglucopyranose triacetate 2- -2- -1- -β-D- 3,4,6- AB acetamidomethylthiazole 2- -4- PB acetanilide M (LC) acetazolamide R acetdimethylamide see dimethylacetamide, N,N- acethydrazide R acetic acid M (solv) acetic anhydride M (FC) acetmethylamide see methylacetamide, N- acetoacetamide R acetoacetanilide R acetoacetic acid, lithium salt R acetobromoglucose -α-D- NB acetohydroxamic acid R acetoin R acetol (hydroxyacetone) R acetonaphthalide (α)R acetone M (solv) acetone ,A.R. M (solv) acetone-d6 RM acetone cyanohydrin R acetonedicarboxylic acid ,dimethyl ester R acetonedicarboxylic acid -1,3- R acetone dimethyl acetal see dimethoxypropane 2,2- acetonitrile M (solv) acetonitrile-d3 RM acetonylacetone see hexanedione 2,5- acetonylbenzylhydroxycoumarin (3-(α- -4- R acetophenone M (LC) acetophenone oxime R acetophenone trimethylsilyl enol ether see phenyltrimethylsilyl... acetoxyacetone (oxopropyl acetate 2-) R acetoxybenzoic acid 4- DS acetoxynaphthoic acid 6- -2- R 2 acetylacetaldehyde dimethylacetal R acetylacetone (pentanedione -2,4-) M (C) acetylbenzonitrile p- R acetylbiphenyl 4- see phenylacetophenone, p- acetyl bromide M (FC) acetylbromothiophene 2- -5- -
Federal LCA Commons Elementary Flow List: Background, Approach, Description and Recommendations for Use
EPA/600/R-19/092 | September 2019 | www.epa.gov/research The Federal LCA Commons Elementary Flow List: Background, Approach, Description and Recommendations for Use 0 Federal LCA Commons Elementary Flow List: Background, Approach, Description and Recommendations for Use by Ashley Edelen, Troy Hottle, Sarah Cashman Eastern Research Group Wesley Ingwersen U.S. EPA/National Risk Management Research Laboratory/ Land and Materials Management Division ii Notice/Disclaimer Although the U.S. Environmental Protection Agency, through its Office of Research and Development, funded and conducted the research described herein under an approved Quality Assurance Project Plan (Quality Assurance Identification Number G-LMMD-0031522-QP-1-0), with the support of Eastern Research Group, Inc. through EPA Contract Number EP-C-16-015, it does not necessarily reflect the views of the Agency, and no official endorsement should be inferred. Mention of trade names or commercial products does not constitute endorsement or recommendation for use. iii Foreword The U.S. Environmental Protection Agency (U.S. EPA) is charged by Congress with protecting the Nation's land, air, and water resources. Under a mandate of national environmental laws, the Agency strives to formulate and implement actions leading to a compatible balance between human activities and the ability of natural systems to support and nurture life. To meet this mandate, U.S. EPA's research program is providing data and technical support for solving environmental problems today and building a science knowledge base necessary to manage our ecological resources wisely, understand how pollutants affect our health, and prevent or reduce environmental risks in the future. -
APPENDIX G Acid Dissociation Constants
harxxxxx_App-G.qxd 3/8/10 1:34 PM Page AP11 APPENDIX G Acid Dissociation Constants § ϭ 0.1 M 0 ؍ (Ionic strength ( † ‡ † Name Structure* pKa Ka pKa ϫ Ϫ5 Acetic acid CH3CO2H 4.756 1.75 10 4.56 (ethanoic acid) N ϩ H3 ϫ Ϫ3 Alanine CHCH3 2.344 (CO2H) 4.53 10 2.33 ϫ Ϫ10 9.868 (NH3) 1.36 10 9.71 CO2H ϩ Ϫ5 Aminobenzene NH3 4.601 2.51 ϫ 10 4.64 (aniline) ϪO SNϩ Ϫ4 4-Aminobenzenesulfonic acid 3 H3 3.232 5.86 ϫ 10 3.01 (sulfanilic acid) ϩ NH3 ϫ Ϫ3 2-Aminobenzoic acid 2.08 (CO2H) 8.3 10 2.01 ϫ Ϫ5 (anthranilic acid) 4.96 (NH3) 1.10 10 4.78 CO2H ϩ 2-Aminoethanethiol HSCH2CH2NH3 —— 8.21 (SH) (2-mercaptoethylamine) —— 10.73 (NH3) ϩ ϫ Ϫ10 2-Aminoethanol HOCH2CH2NH3 9.498 3.18 10 9.52 (ethanolamine) O H ϫ Ϫ5 4.70 (NH3) (20°) 2.0 10 4.74 2-Aminophenol Ϫ 9.97 (OH) (20°) 1.05 ϫ 10 10 9.87 ϩ NH3 ϩ ϫ Ϫ10 Ammonia NH4 9.245 5.69 10 9.26 N ϩ H3 N ϩ H2 ϫ Ϫ2 1.823 (CO2H) 1.50 10 2.03 CHCH CH CH NHC ϫ Ϫ9 Arginine 2 2 2 8.991 (NH3) 1.02 10 9.00 NH —— (NH2) —— (12.1) CO2H 2 O Ϫ 2.24 5.8 ϫ 10 3 2.15 Ϫ Arsenic acid HO As OH 6.96 1.10 ϫ 10 7 6.65 Ϫ (hydrogen arsenate) (11.50) 3.2 ϫ 10 12 (11.18) OH ϫ Ϫ10 Arsenious acid As(OH)3 9.29 5.1 10 9.14 (hydrogen arsenite) N ϩ O H3 Asparagine CHCH2CNH2 —— —— 2.16 (CO2H) —— —— 8.73 (NH3) CO2H *Each acid is written in its protonated form. -
Kalenga Tite Mwepu a Dissertation Submitted in Partial Fulfillment of The
LITHIUM EXTRACTION FROM ZIMBABWEAN PETALITE WITH AMMONIUM BIFLUORIDE DIGESTION Kalenga Tite Mwepu A dissertation submitted in partial fulfillment of the requirements for the degree Master of Science in Applied Science (Chemical Technology) in the Department of Chemical Engineering, Faculty of Engineering, Built Environment and Information Technology. Supervisor: Prof. Philip Crouse Co-supervisor: Dr Salmon Lubbe February 2020 Declaration I, Kalenga Tite Mwepu, student No. 15261043, do hereby declare that this research is my original work and that it has not previously, in its entirety or in part, been submitted and is not currently being submitted, either in whole or in part, at any other university for a degree or diploma, and that all references are acknowledged. SIGNED on this ________________________ day of_____12/02______________ 2020. __________________ Kalenga Tite Mwepu ii Synopsis Lithium carbonate is the precursor for most other lithium compounds. The market demand for lithium is increasing because it is used for many applications such as the preparation of electrode material and electrolyte for lithium-ion batteries, for treatment of manic depression, production of electronic grade crystals of lithium niobate and tantalite, and preparation of battery-grade lithium metal. Previously reported methods of lithium extraction require high temperature calcination for phase transformation from α-spodumene into β-spodumene, that is energy consuming and costly. This step is required because of the higher chemical reactivity of β-spodumene. The objectives of this research were to investigate the viability of ammonium bifluoride digestion of the petalite concentrate from the Bikita deposits without the initial thermal conversion to β- spodumene, in order to produce a high purity lithium carbonate in a cost efficient way, and optimising the remaining process parameters of the full process. -
Global Lithium Sources—Industrial Use and Future in the Electric Vehicle Industry: a Review
resources Review Global Lithium Sources—Industrial Use and Future in the Electric Vehicle Industry: A Review Laurence Kavanagh * , Jerome Keohane, Guiomar Garcia Cabellos, Andrew Lloyd and John Cleary EnviroCORE, Department of Science and Health, Institute of Technology Carlow, Kilkenny, Road, Co., R93-V960 Carlow, Ireland; [email protected] (J.K.); [email protected] (G.G.C.); [email protected] (A.L.); [email protected] (J.C.) * Correspondence: [email protected] Received: 28 July 2018; Accepted: 11 September 2018; Published: 17 September 2018 Abstract: Lithium is a key component in green energy storage technologies and is rapidly becoming a metal of crucial importance to the European Union. The different industrial uses of lithium are discussed in this review along with a compilation of the locations of the main geological sources of lithium. An emphasis is placed on lithium’s use in lithium ion batteries and their use in the electric vehicle industry. The electric vehicle market is driving new demand for lithium resources. The expected scale-up in this sector will put pressure on current lithium supplies. The European Union has a burgeoning demand for lithium and is the second largest consumer of lithium resources. Currently, only 1–2% of worldwide lithium is produced in the European Union (Portugal). There are several lithium mineralisations scattered across Europe, the majority of which are currently undergoing mining feasibility studies. The increasing cost of lithium is driving a new global mining boom and should see many of Europe’s mineralisation’s becoming economic. The information given in this paper is a source of contextual information that can be used to support the European Union’s drive towards a low carbon economy and to develop the field of research. -
Why Nature Chose Selenium Hans J
Reviews pubs.acs.org/acschemicalbiology Why Nature Chose Selenium Hans J. Reich*, ‡ and Robert J. Hondal*,† † University of Vermont, Department of Biochemistry, 89 Beaumont Ave, Given Laboratory, Room B413, Burlington, Vermont 05405, United States ‡ University of WisconsinMadison, Department of Chemistry, 1101 University Avenue, Madison, Wisconsin 53706, United States ABSTRACT: The authors were asked by the Editors of ACS Chemical Biology to write an article titled “Why Nature Chose Selenium” for the occasion of the upcoming bicentennial of the discovery of selenium by the Swedish chemist Jöns Jacob Berzelius in 1817 and styled after the famous work of Frank Westheimer on the biological chemistry of phosphate [Westheimer, F. H. (1987) Why Nature Chose Phosphates, Science 235, 1173−1178]. This work gives a history of the important discoveries of the biological processes that selenium participates in, and a point-by-point comparison of the chemistry of selenium with the atom it replaces in biology, sulfur. This analysis shows that redox chemistry is the largest chemical difference between the two chalcogens. This difference is very large for both one-electron and two-electron redox reactions. Much of this difference is due to the inability of selenium to form π bonds of all types. The outer valence electrons of selenium are also more loosely held than those of sulfur. As a result, selenium is a better nucleophile and will react with reactive oxygen species faster than sulfur, but the resulting lack of π-bond character in the Se−O bond means that the Se-oxide can be much more readily reduced in comparison to S-oxides. -
High Purity Inorganics
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Sodium Sulfate - Wikipedia, the Free Encyclopedia Page 1 of 7
Sodium sulfate - Wikipedia, the free encyclopedia Page 1 of 7 Sodium sulfate From Wikipedia, the free encyclopedia Sodium sulfate is the sodium salt of Sodium sulfate sulfuric acid. When anhydrous, it is a white crystalline solid of formula Na2SO4 known as the mineral thenardite; the decahydrate Na2SO4·10H2O has been known as Glauber's salt or, historically, sal mirabilis since the 17th century. Another Other names solid is the heptahydrate, which transforms Thenardite (mineral) to mirabilite when cooled. With an annual Glauber's salt (decahydrate) production of 6 million tonnes, it is a major Sal mirabilis (decahydrate) commodity chemical and one of the most Mirabilite (decahydrate) damaging salts in structure conservation: when it grows in the pores of stones it can Identifiers achieve high levels of pressure, causing CAS number 7757-82-6 , structures to crack. 7727-73-3 (decahydrate) Sodium sulfate is mainly used for the PubChem 24436 manufacture of detergents and in the Kraft ChemSpider 22844 process of paper pulping. About two-thirds UNII 36KCS0R750 of the world's production is from mirabilite, the natural mineral form of the decahydrate, RTECS number WE1650000 and the remainder from by-products of Jmol-3D images Image 1 chemical processes such as hydrochloric (http://chemapps.stolaf.edu/jmol/jmol.php? acid production. model=%5BNa%2B%5D.%5BNa%2B% 5D.%5BO-%5DS%28%5BO-%5D%29% 28%3DO%29%3DO) Contents SMILES InChI ■ 1History ■ 2 Physical and chemical properties Properties ■ 3 Production Molecular Na2SO4 ■ 3.1 Natural sources formula -
Lithium Resources and Requirements by the Year 2000
Lithium Resources and Requirements by the Year 2000 GEOLOGICAL SURVEY PROFESSIONAL PAPER 1005 Lithium Resources and Requirements by the Year 2000 JAMES D. VINE, Editor GEOLOGICAL SURVEY PROFESSIONAL PAPER 1005 A collection of papers presented at a symposium held in Golden, Colorado, January 22-24, 1976 UNITED STATES GOVERNMENT PRINTING OFFICE, WASHINGTON : 1976 UNITED STATES DEPARTMENT OF THE INTERIOR THOMAS S. KLEPPE, Secretary GEOLOGICAL SURVEY V. E. McKelvey, Director First printing 1976 Second printing 1977 Library of Congress Cataloging in Publication Data Vine, James David, 1921- Lithium resources and requirements by the year 2000. (Geological Survey Professional Paper 1005) 1. Lithium ores-United States-Congresses. 2. Lithium-Congresses. I. Vine, James David, 1921- II. Title. HI. Series: United States Geological Survey Professional Paper 1005. TN490.L5L57 553'.499 76-608206 For sale by the Superintendent of Documents, U.S. Government Printing Office Washington, D.C. 20402 Stock Number 024-001-02887-5 CONTENTS Page 1. Introduction, by James D. Vine, U.S. Geological Survey, Denver, Colo ______________-_______-_-- — ------- —— —— ——— ---- 1 2. Battery research sponsored by the U.S. Energy Research and Development Administration, by Albert Landgrebe, Energy Research and De velopment Administration, Washington, D.C., and Paul A. Nelson, Argonne National Laboratory, Argonne, Ill-__- —— -____.—————— 2 3. Battery systems for load-leveling and electric-vehicle application, near-term and advanced technology (abstract), by N. P. Yao and W. J. Walsh, Argonne National Laboratory, Argonne, 111___.__________________________________-___-_________ — ________ 5 4. Lithium requirements for high-energy lithium-aluminum/iron-sulfide batteries for load-leveling and electric-vehicle applications, by A. -
Chemical Names and CAS Numbers Final
Chemical Abstract Chemical Formula Chemical Name Service (CAS) Number C3H8O 1‐propanol C4H7BrO2 2‐bromobutyric acid 80‐58‐0 GeH3COOH 2‐germaacetic acid C4H10 2‐methylpropane 75‐28‐5 C3H8O 2‐propanol 67‐63‐0 C6H10O3 4‐acetylbutyric acid 448671 C4H7BrO2 4‐bromobutyric acid 2623‐87‐2 CH3CHO acetaldehyde CH3CONH2 acetamide C8H9NO2 acetaminophen 103‐90‐2 − C2H3O2 acetate ion − CH3COO acetate ion C2H4O2 acetic acid 64‐19‐7 CH3COOH acetic acid (CH3)2CO acetone CH3COCl acetyl chloride C2H2 acetylene 74‐86‐2 HCCH acetylene C9H8O4 acetylsalicylic acid 50‐78‐2 H2C(CH)CN acrylonitrile C3H7NO2 Ala C3H7NO2 alanine 56‐41‐7 NaAlSi3O3 albite AlSb aluminium antimonide 25152‐52‐7 AlAs aluminium arsenide 22831‐42‐1 AlBO2 aluminium borate 61279‐70‐7 AlBO aluminium boron oxide 12041‐48‐4 AlBr3 aluminium bromide 7727‐15‐3 AlBr3•6H2O aluminium bromide hexahydrate 2149397 AlCl4Cs aluminium caesium tetrachloride 17992‐03‐9 AlCl3 aluminium chloride (anhydrous) 7446‐70‐0 AlCl3•6H2O aluminium chloride hexahydrate 7784‐13‐6 AlClO aluminium chloride oxide 13596‐11‐7 AlB2 aluminium diboride 12041‐50‐8 AlF2 aluminium difluoride 13569‐23‐8 AlF2O aluminium difluoride oxide 38344‐66‐0 AlB12 aluminium dodecaboride 12041‐54‐2 Al2F6 aluminium fluoride 17949‐86‐9 AlF3 aluminium fluoride 7784‐18‐1 Al(CHO2)3 aluminium formate 7360‐53‐4 1 of 75 Chemical Abstract Chemical Formula Chemical Name Service (CAS) Number Al(OH)3 aluminium hydroxide 21645‐51‐2 Al2I6 aluminium iodide 18898‐35‐6 AlI3 aluminium iodide 7784‐23‐8 AlBr aluminium monobromide 22359‐97‐3 AlCl aluminium monochloride