The Extraction of Iron, Cobalt, and Nickel Sulfates

Total Page:16

File Type:pdf, Size:1020Kb

The Extraction of Iron, Cobalt, and Nickel Sulfates THE EXTRACTION OF IRON, COBALT, AND NICKEL SULFATES Dissertation Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By CARL SOLOMON SCHLEA, B.Ch.E., M.Sc. The Ohio State University 1955-- Approved by • \ C , Dr. C. J. Geankoplis, Adviser Chemical Engineering Department i Acknowledgement The author would like to express his appreciation to his adviser, Dr. C. J. Geankoplis, for his very generous assistance and helpful advice. Grateful acknowledgement is made to the Battelle Memorial Institute for their financial assistance by means of a fellowship for the years 1952-1955. TABLE OP CONTENTS Page ABSTRACT................ 1 INTRODUCTION ....................................... 4 LITERATURE R E V I E W .................................. 10 1. The Extraction of Metal Halides .......... 10 2. The Extraction of Metal Nitrates ........ 18 3. The Extraction of Thiocyanates............... 24- 4-. The Extraction of Metal Sulfates ......... 26 5. The Extraction of Cobalt and Nickel Acetates and. 28 the Separation of Chromium and Vanadium 6. The Extraction of Chelate Compounds ........ 28. STATEMENT OF THE PROBLEM............................. 30 THEORY...................... 32 ANALYTICAL METHODS.................................. 36 1. Aqueous-Phase Analyses .......... ....... 36 2. Organic-Phase A n a lyses................. 4& EXPERIMENTAL PROCEDURE .............................. 62 1. Equipment.................. 62 2. Extraction Procedure.................. 65 3. Phase Diagram Determination ................ 71 4-. Materials Used................... 72 EXPERIMENTAL D A T A ............. 77 1. Solvent and Additive Search D a t a ......... 77 2. Extractions With Normal Butyl Alcohol..... 94. 3. Solubility Determinations With Normal Butyl Alcohol 94. TREATMENT AND DISCUSSION OF D A T A .................... 106 1. Calculations ................... 106 2. Discussion of Solvent Search and Additive Search. 108 Data iii TABLE OF CONTENTS (Continued) Page a. Solvent Search ................ 10S b. Additive S e a r c h ............. 113 c. Selection of the Solvent......... 114 3. Correlation and Discussion of Distribution Data . 115 a. Effect of Sulfuric A c i d ............... 116 b. Effect of Metal and Metal Composition .... 120 c. Effect of Temperature................. 126 d. The Distribution of Sulfuric Acid............ 129 e. Distribution in Mixtures................... 132 f. Density Correlations ............. I36 4» Solubility Determinations....................... 136 CONCLUSIONS. .................................... 144 SUGGESTIONS FOR FURTHER INVESTIGATIONS .................. 147 NOMENCLATURE.......... ............... ............149 autobiography:........................................ 151 iv LIST OF TABLES Page TABLE 1. ERRORS IN COLORIMETRIC ANALYSES.............. 51 TABLE 2. MATERIALS U S E D .......... .......... 74 TABLE 3. SOLVENT SEARCH DATA AT 25.0°C................ 78 TABLE A. DISTRIBUTION IN SYSTEMS: METAL SULFATE - . 90 WATER - SOLVENT - ADDITIVE AT 25.0°C. TABLE 5. DISTRIBUTION IN SYSTEMS: NICKEL SULFATE - . , ; 95 SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL - AT 25.0°C. TABLE 6. DISTRIBUTION IN THE SYSTEM: COBALT SULFATE - i . 96 SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL AT 25.0°C. TABLE 7. DISTRIBUTION IN THE SYSTEM: FERRIC SULFATE - . ♦ 97 SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL AT 25.0°C. TABLE 8. DISTRIBUTION IN THE SYSTEM: SULFURIC ACID - . 98 . WATER - NORMAL BUTYL ALCOHOL AT 25.0°C. TABLE 9. DISTRIBUTION IN THE SYSTEM: NICKEL SULFATE - . 99 SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL AT VARIOUS TEMPERATURES TABLE 1C . DISTRIBUTION IN THE SYSTEM: COBALT SULFATE - . 100 SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL AT VARIOUS TEMPERATURES TABLE 13 . DISTRIBUTION IN THE SYSTEM: FERRIC SULFATE - . ”101 SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL AT VARIOUS TEMPERATURES TABLE 12.. DISTRIBUTION IN THE SYSTEM: NICKEL SULFATE - . 102 COBALT SULFATE - FERRIC SULFATE - SULFURIC ACID - WATER - NORMAL BUTYL ALCOHOL AT 25.0°C. TABLE 13. SOLUBILITY ENVELOPE FOR THE SYSTEM: SULFURIC . 103 ACID - WATER - NORMAL BUTYL ALCOHOL AT 25.0°C. V LIST OP TABLES (Continued) Page TABLE 14. THE EFFECT OF METAL SULFATES ON T H E .............104 SOLUBILITY OF NORMAL BUTYL ALCOHOL IN AQUEOUS SULFURIC ACID SOLUTIONS AT 25.0°C. TABLE 15. THE EFFECT OF NICKEL SULFATE ON T H E .............105 SOLUBILITY OF WATER IN SULFURIC ACID SOLUTIONS OF NORMAL BUTYL ALCOHOL AT 25.0°C. TABLE 16. SEPARATION FACTORS AT 25.0°C....................121 TABLE 17. EXTRACTION IN MIXTURES COMPARED TO T H A T ...... 134 WHEN SALTS EQUILIBRATED SEPARATELY AT 25.0°C. TABLE IS. TIE LINE DATA FOR THE SYSTEM: SULFURIC..... 140 ACID - WATER - NORMAL BUTYL ALCOHOL AT 25.0°C. vi LIST OF FIGURES Page FIGURE 10. THE DISTRIBUTION OF CHROMIC SULFATE AND .... 27 SULFATE BETWEEN NORMAL BUTYL ALCOHOL AND AQUEOUS SULFURIC ACID FIGURE 2„ THE EFFECT OF METAL SULFATES AND NORMAL BUTYL . 1(3 ALCOHOL ON SULFURIC ACID NEUTRALIZATION * ’ ' FIGURE 3o ERRORS IN COLORIMETRIC ANALYTICAL PROCEDURES . h9 FIGURE lw THE DISTRIBUTION OF NICKEL SULFATE BETWEEN. 0H 7 NORMAL BUTYL ALCOHOL AND AQUEOUS SULFURIC ACID FIGURE 5. THE DISTRIBUTION OF COBALT SULFATE BETWEEN. • .118 NOMAL BUTYL ALCOHOL AND AQUEOUS SULFURIC ACID FIGURE 6*. THE DISTRIBUTION OF FERRIC SULFATE BETWEEN. .119 NORMAL BUTYL ALCOHOL AND AQUEOUS SULFURIC ACID FIGURE 7* THE EFFECT OF SULFURIC ACID ON THE. ..... .122 SEPARATION FACTOR BETWEEN IRON AND NICKEL AT 25.0°C. FIGURE 8 ,. THE EFFECT OF SULFURIC ACID ON THE. ..... ,123 SEPARATION FACTOR BETWEEN IRON AND COBALT AT 25.0°C. FIGURE 9o THE EFFECT OF SULFURIC ACID ON THE........ .121* SEPARATION FACTOR BETWEEN COBALT AND NICKEL AT 25.0°C* FIGURE 10* THE EFFECT OF METAL CONCENTRATION ON. .125 DISTRIBUTION AT CONSTANT ACID CONCENTRATIONS FIGURE 11*. THE EFFECT OF TEMPERATURE ON DISTRIBUTION . 0127 FIGURE 12 o. THE EFFECT OF TEMPERATURE ON DISTRIBUTION , . ,128 vii LI SI’ OF FIGURES (Continued) FIGURE 13. THE DISTRIBUTION OF SULFURIC ACID BETWEEN . , * 130 • WATER AND NOMAL BUTIL ALCOHOL AT 25.0°C., FERRIC SULFATE PRESENT FIGURE lUo THE DISTRIBUTION OF SULFURIC ACID BETWEEN o . o 131 WATER AND NORMAL BUTYL ALCOHOL AT 25a0°Co, COBALT SULFATE AND NICKEL SULFATE PRESENT FIGURE 1$. DISTRIBUTION IN MIXTURES AT 2$.0°C, 133 FIGURE 160 EXTRACTION IN MIXTURES COMPARED TO THAT WHEN. ,13$ EACH SALT EQUILIBRATED SEPARATELY FIGURE 17* DENSITY OF THE WATER PHASE IN THE SYSTEM. 0 • » 137 HgSOj^ - NiSO^ - HgO - nC^HpOH AT 2S.0°C» FIGURE 18*. DENSITY OF THE WATER PHASE IN THE SYSTEM* , . 0 138 HgSO^ - NiSO^ - HgO - n C ^ O H AT 20.0°C* FIGURE 19+ DENSITY OF THE N-BUTYL ALCOHOL PHASE IN THE „ * 139 SYSTEM* H2SO^ - NiSO^ - HgO - n C ^ O H AT 20 .0 °C*. FIGURE 20* PHASE DIAGRAM FOR THE SfSTEM:' SULFURIC ACID lUl WATER - NORMAL BUTYL ALCOHOL AT 25,0°C„ FIGURE 21, THE EFFECT OF METAL SULFATES ON THE , , . „ 1^2 SOLUBILITY OF NORMAL BUTYL ALCOHOL IN WATER AT 25bO°C. 1 ABSTRACT The separation of iron, cobalt, and nickel has long been of commercial and academic importance. In recent years, interest has been shown in the use of liquid-liquid extraction to separate compon­ ents of mixtures of inorganic compounds. Some cobalt and nickel recovery processes involve the use of sulfuric acid solutions of the metals* This investigation was carried out to thoroughly study the use of liquid-liquid extraction as a method of separating iron, cobalt, and nickel sulfates from aqueous solutions. The first series of tests were made to determine distri­ bution data for the pure metal sulfates between water and a large number of organic solvents at 2£.Q°C. when each metal was equilibrated separately. The effects of sulfuric acid, sodium sulfate, and ammoni­ um sulfate on the distribution characteristics were determined for each metal. Distribution runs were then carried out with the best solvent* The alkyl acid phosphates were found to be the best series of compounds for extraction purposes* Supplementary experimental work showed that a chemical reaction took place and the sulfate ion was not extracted. These compounds were thus eliminated as possible extraction media. Most non-acidic organic compounds did not extract iron, cobalt, and nickel sulfates to any measurable degree. Of these non-acidic organic solvents, the lower alcohols were found to be the best series of compounds to extract the metal sulfates. Sulfuric acid increased distribution coefficients markedly, while sodium sulfate and ammonium sulfate had detrimental effects on extraction. 2 Electrostatic considerations of ions in solution could not explain the extraction,* Solvents with high dielectric constants ex­ tracted less than some with considerably lower dielectric constants# Also, extraction could not be correlated with the degree of water solubility in the organic phase# Although no quantitative information of the strength of hydrogen bonds is available, the relative order of magnitude of distribution coefficients changed in much the same manner as relative strengths of hydrogen bonding characteristics of the organic solvents# Normal butyl alcohol was chosen in conjunction with sulfuric acid to determine extraction characteristics with iron, cobalt, and mickel sulfates# Distribution coefficients, when each metal was equilibrated separately, were on the order of magnitude of 0.0001 at 25#0°C# By adding up to 250 grams sulfuric acid per liter of the water phase, these distribution coefficients increased over 100 times, values over 0.01 being obtained* Separation factors were
Recommended publications
  • Developing a Solvent Extraction Process for the Separation of Cobalt and Iron from Nickel Sulfate Solutions
    Abstract DEVELOPING A SOLVENT EXTRACTION PROCESS FOR THE SEPARATION OF COBALT AND IRON FROM NICKEL SULFATE SOLUTIONS By Michiel Casparus Olivier Thesis presented in partial fulfilment of the requirements for the Degree of MASTER OF SCIENCE IN ENGINEERING (EXTRACTIVE METALLURGICAL ENGINEERING) In the faculty of Engineering at Stellenbosch University Supervised by Christie Dorfling December 2011 i Stellenbosch University http://scholar.sun.ac.za DeclarationAbstract DECLARATION By submitting this thesis electronically, I declare that the entirety of the work contained therein is my own, original work, that I am the sole author thereof (save to the extent explicitly otherwise stated), that reproduction and publication thereof by Stellenbosch University will not infringe any third party rights and that I have not previously in its entirety or in part submitted it for obtaining any qualification. …………………………… ………………. Signature Date Copyright © 2011 Stellenbosch University All rights reserved i Stellenbosch University http://scholar.sun.ac.za Abstract ABSTRACT Crude NiSO4 solutions are often produced as a product of Sherrit based matte leach processes leading to iron and cobalt contaminated solutions of NiSO4. To upgrade the quality of these solutions for either, the production of NiSO4 crystals or cathode/precipitated nickel, the iron and cobalt must be removed. Conventional processes use either pure or saponified Cyanex 272 in solvent extraction to extract iron and cobalt from pregnant nickel leach solutions. These processes require the addition of an alkali like NaOH to neutralise the protons being exchanged for the different metal species since extraction is a strong function of pH. Hence, while removing iron and cobalt from the solution, sodium is added instead.
    [Show full text]
  • Sudibyo S, Et Al. Optimization of Electrometal-Elektrowinning Cobalt Process from the Slag Copyright© Sudibyo S, Et Al
    Physical Science & Biophysics Journal MEDWIN PUBLISHERS ISSN: 2641-9165 Committed to Create Value for Researchers Optimization of Electrometal-Elektrowinning Cobalt Process from the Slag of Nickel Pig Iron (NPI) Hermida L1, Sudibyo S2*, Supriyatna YI2, Herlina U2, Handoko AS2, Prasetyo E2, Almutaqii M2 and Reswari PA1 Research Article Volume 4 Issue 2 1Department of Chemical Engineering, Engineering Faculty, Lampung University, Indonesia Received Date: October 09, 2020 2Research Unit for Mineral Technology, Indonesian Institute of Sciences (LIPI), Indonesia Published Date: October 27, 2020 *Corresponding author: Sudibyo Sudibyo, Research Unit for Mineral Technology, Indonesian Institute of Sciences (LIPI), Ir. Sutami street Km. 15, Tanjung Bintang, South Lampung district, Lampung Province, Indonesia, Tel: +6285881020870; Email: [email protected] Abstract Slag from the manufacturing of nickel pig iron (NPI) from laterite soil is still containing 823.7 ppm of cobalt. In this research, the separation process is carried out from slag NPI by using the Response Surface Method (RSM). This method is to determine the optimum conditional process of Electrometal Electrowinning (EMEW) and get an equation model to see the correlation isbetween leach the a variable slag using and acetic know acid,the most and significantthen extracted interfactor in two interaction.steps by versatic This research acid 10 andwas thenconducted with cyanex using three 272. parameters,The organic phaseconsists from of duration this extraction of operation, then stripped potential using voltage, 6 M and sulphuric variable acid of boric so obtained acid. The aqueous first step phase in electro-metal at pH 5.5 with electrowinning the highest cobalt content. The best condition of electro-metal electrowinning is obtained at 4.5 V, 2 hours, and 0.5 M of boric acid with 45.8273% of cobalt recovery.
    [Show full text]
  • Heats of Formation of Certain Nickel-Pyridine Complex Salts
    HEATS OF FORFATION OF CERTAIN NICKEL-PYRIDINE COLPLEX SALTS DAVID CLAIR BUSH A THESIS submitted to OREGON STATE COLLEGE in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE June l9O [4CKNOWLEDGMENT The writer wishes to acknowledge his indebtedness and gratitude to Dr. [4. V. Logan for his help and encour- agement during this investigation. The writer also wishes to express his appreciation to Dr. E. C. Gilbert for helpful suggestions on the con- struction of the calortheter, and to Lee F. Tiller for his excellent drafting and photostating of the figures and graphs. APPROVED: In Charge of ?ajor Head of Department of Chemistry Chairrian of School Graduate Comrittee Dean of Graduate School Date thesis is presented /11 ' Typed by Norma Bush TABLE OF CONTENTS HISTORICAL BACKGROUND i INTRODUCTION 2 EXPERIMENTAL 5 Preparation of the Compounds 5 Analyses of the Compounds 7 The Calorimeter Determination of the Heat Capacity 19 Determination of the Heat of Formation 22 DISCUSSION 39 41 LITERATURE CITED 42 TABLES I Analyses of the Compounds 8 II Heat Capacity of the Calorimeter 23 III Heat of Reaction of Pyridine 26 IV Sample Run and Calculation 27 V Heat of Reaction of Nickel Cyanate 30 VI Heat of Reaction of Nickel Thiocyanate 31 VII Heat of Reaction of Hexapyridinated Nickel Cyanate 32 VIII Heat of Reaction of Tetrapyridinated Nickel Thiocyanate 33 IX Heat of Formation of the Pyridine Complexes 34 FI GURES i The Calorimeter 10 2 Sample Ijector (solids) 14 2A Sample Ejector (liquids) 15 3 Heater Circuit Wiring Diagram 17 4 heat Capacity of the Calorimeter 24 5 Heat of Reaction of Pyridine 28 6 Heat of Reaction of Hexapyridinated Nickel Cyanate 35 7 Heat of Reaction of Tetrapyridinated Nickel Thiocyanate 36 8 Heat of Reaction of Nickel Cyanate 37 9 Heat of Reaction of Nickel Thiocyanate 38 HEATS OF FOW ATION OF CERTAIN NICKEL-PYRIDINE COMPLEX SALTS HISTORICAL BACKGROUND Compounds of pyridine with inorganic salts have been prepared since 1970.
    [Show full text]
  • United States Patent Office Patented Jan
    3,071,593 United States Patent Office Patented Jan. 1, 1963 2 3,071,593 O PREPARATION OF AELKENE SULFES Paul F. Warner, Philips, Tex., assignor to Philips Petroleum Company, a corporation of Delaware wherein each R is selected from the group consisting of No Drawing. Filed July 27, 1959, Ser. No. 829,518 5 hydrogen, alkyl, aryl, alkaryl, aralkyl and cycloalkyl 8 Claims. (C. 260-327) groups having 1 to 8 carbon atoms, the combined R groups having up to 12 carbon atoms. Examples of Suit This invention relates to a method of preparing alkene able compounds are ethylene oxide, propylene oxide, iso sulfides. Another aspect relates to a method of convert butylene oxide, a-amylene oxide, styrene oxide, isopropyl ing an alkene oxide to the corresponding sulfide at rela O ethylene oxide, methylethylethylene oxide, 3-phenyl-1, tively high yields without refrigeration. 2-propylene oxide, (3-methylphenyl) ethylene oxide, By the term "alkene sulfide' as used in this specifica cyclohexylethylene oxide, 1-phenyl-3,4-epoxyhexane, and tion and in the claims, I mean to include not only un the like. substituted alkene sulfides such as ethylene sulfide, propyl The salts of thiocyanic acid which I prefer to use are ene sulfide, isobutylene sulfide, and the like, but also 5 the salts of the alkali metals or ammonium. I especially hydrocarbon-substituted alkene sulfides such as styrene prefer ammonium thiocyanate, sodium thiocyanate, and oxide, and in general all compounds conforming to the potassium thiocyanate. These compounds can be reacted formula with ethylene oxide in a cycloparaffin diluent to produce 20 substantial yields of ethylene sulfide and with little or S no polymer formation.
    [Show full text]
  • Development of the New Method for Oxidized Nickel Ore Processing
    NIOKR-2018 Theoretical and practical conference with international participation and School KnE Materials Science for young scientists «FERROALLOYS: Development prospects of metallurgy and machine building based on completed Research and Development» Volume 2019 Conference Paper Development of the New Method for Oxidized Nickel Ore Processing Boris Dmitrievich Khalezov, Oleg Vadimovich Zayakin, Alexey Sergeevich Gavrilov, and Vladimir Ivanovich Zhuchkov IMET UB RAS, Ekaterinburg, Russia Abstract In modern conditions of sharp fluctuations in nickel prices on world markets, the problem of profitability of processing Russian poor oxidized nickel ores (ONO) has arisen. As an alternative to the previously existing in Russia, a sulphidation-reducing smelting on a matte, a hydro-pyrometallurgical method has been proposed for the preparation of complex nickel-, chromium-, manganese-containing ferroalloys. At the first stage, hydrolytic precipitation (with sodium hydroxide) is considered as a method of processing production solutions from heap leaching of ONO. It is established that Corresponding Author: at pH = 5.5, Al is completely removed in the precipitate as hydroxide. After washing Oleg Vadimovich Zayakin from impurities and calcining, a concentrate containing 50 wt.% Al was obtained. At the [email protected] second stage, at pH = 9.5, more than 99% of nickel and cobalt oxides, as well as 92% Received: 5 February 2019 MnO and 46% MgO, are precipitated. Obtained after washing and calcination at 700∘C Accepted: 6 March 2019 oxide concentrate contains, by weight. %: 67 NiO; 3 CoO; 20 MnO; 9 MgO; 0,2 S. At the Published: 17 March 2019 third stage, a pyrometallurgical method for smelting complex ferroalloys of the Fe-Ni-Cr- Publishing services provided by Mn-Si system using refractory ferrosilicochrome as a reducing agent is proposed for the Knowledge E processing of nickel-containing concentrate.
    [Show full text]
  • Study on the Extraction and Separation of Zinc, Cobalt, and Nickel Using Ionquest 801, Cyanex 272, and Their Mixtures
    metals Article Study on the Extraction and Separation of Zinc, Cobalt, and Nickel Using Ionquest 801, Cyanex 272, and Their Mixtures Wensen Liu 1,2,3, Jian Zhang 3,4,5, Zhenya Xu 6, Jie Liang 1,* and Zhaowu Zhu 2,3,4,* 1 School of Chemical and Environmental Engineering, China University of Mining and Technology (Beijing), Beijing 100083, China; [email protected] 2 Innovation Academy for Green Manufacture, Chinese Academy of Sciences, Beijing 100190, China 3 National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Beijing 100190, China; [email protected] 4 Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China 5 School of Chemistry and Chemical Engineering, University of Chinese Academy of Sciences, Beijing 100049, China 6 The College of Chemical Engineering, Beijing University of Chemical Technology, Beijing 100028, China; [email protected] * Correspondence: [email protected] (J.L.); [email protected] (Z.Z.) Abstract: Both Cyanex 272 (bis (2,4,4-trimethylpentyl) phosphinic acid) and Ionquest 801 (2-ethylhexyl phosphonic acid mono-2-ethylhexyl ester) are commonly used for metal extraction and separation, particularly for zinc, cobalt, and nickel, which are often found together in processing solutions. Detailed metal extractions of zinc, cobalt, and nickel were studied in this paper using Cya-nex 272, Ionquest 801, and their mixtures. It was found that they performed very similarly in zinc selectivity over cobalt. Cyanex 272 performed much better than Ionquest 801 in cobalt separation from nickel. Citation: Liu, W.; Zhang, J.; Xu, Z.; However, very good separation of them was also obtained with Ionquest 801 at its low concentration Liang, J.; Zhu, Z.
    [Show full text]
  • House Fly Attractants and Arrestante: Screening of Chemicals Possessing Cyanide, Thiocyanate, Or Isothiocyanate Radicals
    House Fly Attractants and Arrestante: Screening of Chemicals Possessing Cyanide, Thiocyanate, or Isothiocyanate Radicals Agriculture Handbook No. 403 Agricultural Research Service UNITED STATES DEPARTMENT OF AGRICULTURE Contents Page Methods 1 Results and discussion 3 Thiocyanic acid esters 8 Straight-chain nitriles 10 Propionitrile derivatives 10 Conclusions 24 Summary 25 Literature cited 26 This publication reports research involving pesticides. It does not contain recommendations for their use, nor does it imply that the uses discussed here have been registered. All uses of pesticides must be registered by appropriate State and Federal agencies before they can be recommended. CAUTION: Pesticides can be injurious to humans, domestic animals, desirable plants, and fish or other wildlife—if they are not handled or applied properly. Use all pesticides selectively and carefully. Follow recommended practices for the disposal of surplus pesticides and pesticide containers. ¿/áepé4áaUÁí^a¡eé —' ■ -"" TMK LABIL Mention of a proprietary product in this publication does not constitute a guarantee or warranty by the U.S. Department of Agriculture over other products not mentioned. Washington, D.C. Issued July 1971 For sale by the Superintendent of Documents, U.S. Government Printing Office Washington, D.C. 20402 - Price 25 cents House Fly Attractants and Arrestants: Screening of Chemicals Possessing Cyanide, Thiocyanate, or Isothiocyanate Radicals BY M. S. MAYER, Entomology Research Division, Agricultural Research Service ^ Few chemicals possessing cyanide (-CN), thio- cyanate was slightly attractive to Musca domes- eyanate (-SCN), or isothiocyanate (~NCS) radi- tica, but it was considered to be one of the better cals have been tested as attractants for the house repellents for Phormia regina (Meigen).
    [Show full text]
  • Thiocyanate Pyridine Complexes
    W&M ScholarWorks Undergraduate Honors Theses Theses, Dissertations, & Master Projects 5-2017 Structural Comparison of Copper(II) Thiocyanate Pyridine Complexes Joseph V. Handy College of WIlliam & Mary Follow this and additional works at: https://scholarworks.wm.edu/honorstheses Part of the Inorganic Chemistry Commons Recommended Citation Handy, Joseph V., "Structural Comparison of Copper(II) Thiocyanate Pyridine Complexes" (2017). Undergraduate Honors Theses. Paper 1100. https://scholarworks.wm.edu/honorstheses/1100 This Honors Thesis is brought to you for free and open access by the Theses, Dissertations, & Master Projects at W&M ScholarWorks. It has been accepted for inclusion in Undergraduate Honors Theses by an authorized administrator of W&M ScholarWorks. For more information, please contact [email protected]. Structural Comparison of Copper(II) Thiocyanate Pyridine Complexes A thesis submitted in partial fulfillment of the requirement for the degree of Bachelor of Science in Chemistry from The College of William & Mary by Joseph Viau Handy Accepted for ____________________________ ________________________________ Professor Robert D. Pike ________________________________ Professor Deborah C. Bebout ________________________________ Professor David F. Grandis ________________________________ Professor William R. McNamara Williamsburg, VA May 3, 2017 1 Table of Contents Table of Contents…………………………………………………...……………………………2 List of Figures, Tables, and Charts………………………………………...…………………...4 Acknowledgements….…………………...………………………………………………………6
    [Show full text]
  • Cobalt: Demand-Supply Balances in the Transition to Electric Mobility
    Cobalt: demand-supply balances in the transition to electric mobility Alves Dias P., Blagoeva D., Pavel C., Arvanitidis N. 2018 EUR 29381 EN This publication is a Technical report by the Joint Research Centre (JRC), the European Commission’s science and knowledge service. It aims to provide evidence-based scientific support to the European policymaking process. The scientific output expressed does not imply a policy position of the European Commission. Neither the European Commission nor any person acting on behalf of the Commission is responsible for the use that might be made of this publication. Contact information Name: Patrícia Alves Dias & Darina Blagoeva Address European Commission, Joint Research Centre, P.O. Box 2, NL-1755 ZG Petten, The Netherlands Email: [email protected] & [email protected] Tel.: +31 22456-5054 / +31 22456-5030 JRC Science Hub https://ec.europa.eu/jrc JRC112285 EUR 29381 EN PDF ISBN 978-92-79-94311-9 ISSN 1831-9424 doi:10.2760/97710 Luxembourg: Publications Office of the European Union, 2018 © European Union/European Atomic Energy Community, 2018 The reuse policy of the European Commission is implemented by Commission Decision 2011/833/EU of 12 December 2011 on the reuse of Commission documents (OJ L 330, 14.12.2011, p. 39). Reuse is authorised, provided the source of the document is acknowledged and its original meaning or message is not distorted. The European Commission shall not be liable for any consequence stemming from the reuse. For any use or reproduction of photos or other material that is not owned by the EU, permission must be sought directly from the copyright holders.
    [Show full text]
  • First Cobalt Refinery Engineering Report
    First Cobalt Refinery Project Ontario, Canada Association for the Advancement of Cost Engineering (AACE) Class 3 Feasibility Study July 9, 2020 Prepared for: First Cobalt Corporation 401 Bay St., 6th Floor, Toronto, ON, M5H 2Y4 Prepared by: Ausenco Engineering Canada 855 Homer St., Vancouver, BC, V6C 2X8 This report was prepared to summarise the results of the feasibility study related to the First Cobalt Refinery Project. This report does not constitute a feasibility study within the definition employed by the Canadian Institute of Mining, Metallurgy and Petroleum (CIM), as it relates to a stand-along industrial project and does not concern a mineral project of First Cobalt. As a result, disclosure standards prescribed by National Instrument 43-101 – Standards of Disclosure for Mineral Projects (NI 43-101) are not applicable to the scientific and technical disclosure in this report. Any references to scoping study, prefeasibility study or feasibility study by First Cobalt, in relation to the Refinery Project, are not the same as terms defined by the CIM Definition Standards and used in NI 43-101. First Cobalt Refinery Project AACE Class 3 Feasibility Study 1 Executive Summary ....................................................................................................................... 1 1.1 Property Description & Location ............................................................................................................... 1 1.2 Infrastructure & Physiography .................................................................................................................
    [Show full text]
  • Flotation of Mixed Oxide Sulphide Copper-Cobalt Minerals Using Xanthate, Dithiophosphate, Thiocarbamate and Blended Collectors
    ORE Open Research Exeter TITLE Flotation of mixed oxide sulphide copper-cobalt minerals using xanthate, dithiophosphate, thiocarbamate and blended collectors AUTHORS Tijsseling, L; Dehaine, Q; Rollinson, G; et al. JOURNAL Minerals Engineering DEPOSITED IN ORE 03 June 2019 This version available at http://hdl.handle.net/10871/37358 COPYRIGHT AND REUSE Open Research Exeter makes this work available in accordance with publisher policies. A NOTE ON VERSIONS The version presented here may differ from the published version. If citing, you are advised to consult the published version for pagination, volume/issue and date of publication Minerals Engineering 138 (2019) 246–256 Contents lists available at ScienceDirect Minerals Engineering journal homepage: www.elsevier.com/locate/mineng Flotation of mixed oxide sulphide copper-cobalt minerals using xanthate, T dithiophosphate, thiocarbamate and blended collectors ⁎ L.T. Tijsseling, Q. Dehaine, G.K. Rollinson, H.J. Glass University of Exeter, Camborne School of Mines, Penryn, Cornwall TR10 9FE, United Kingdom ARTICLE INFO ABSTRACT Keywords: More than half of the global cobalt supply from primary sources is currently produced in the Democratic Mixed oxide sulphide ore Republic of Congo (DRC) from ores containing copper-cobalt oxides or copper-cobalt sulphides. Where oxide and Flotation sulphide cobalt-bearing copper minerals occur together, efficient recovery of copper and cobalt is known tobe Copper extremely difficult. This study investigates the flotation behaviour of a mixed oxide-sulphide ore wherecopperis Cobalt hosted in sulphides phases such as bornite, chalcopyrite and chalcocite, and oxide phases such as malachite and QEMSCAN to a lesser extent chrysocolla. Three cobalt-bearing oxide minerals are observed in the mixed ore, i.e.
    [Show full text]
  • Energy Consumption and Greenhouse Gas Emissions of Nickel Products
    energies Article Energy Consumption and Greenhouse Gas Emissions of Nickel Products Wenjing Wei 1,2,*, Peter B. Samuelsson 1 , Anders Tilliander 1, Rutger Gyllenram 1,2 and Pär G. Jönsson 1 1 Department of Materials Science and Engineering, Royal Institute of Technology, 114 28 Stockholm, Sweden; [email protected] (P.B.S.); [email protected] (A.T.); [email protected] (R.G.); [email protected] (P.G.J.) 2 Kobolde &Partners AB, Ringvägen 100, 118 60 Stockholm, Sweden * Correspondence: [email protected] Received: 25 September 2020; Accepted: 26 October 2020; Published: 29 October 2020 Abstract: The primary energy consumption and greenhouse gas emissions from nickel smelting products have been assessed through case studies using a process model based on mass and energy balance. The required primary energy for producing nickel metal, nickel oxide, ferronickel, and nickel pig iron is 174 GJ/t alloy (174 GJ/t contained Ni), 369 GJ/t alloy (485 GJ/t contained Ni), 110 GJ/t alloy (309 GJ/t contained Ni), and 60 GJ/t alloy (598 GJ/t contained Ni), respectively. Furthermore, the associated GHG emissions are 14 tCO2-eq/t alloy (14 tCO2-eq/t contained Ni), 30 t CO2-eq/t alloy (40 t CO2-eq/t contained Ni), 6 t CO2-eq/t alloy (18 t CO2-eq/t contained Ni), and 7 t CO2-eq/t alloy (69 t CO2-eq/t contained Ni). A possible carbon emission reduction can be observed by comparing ore type, ore grade, and electricity source, as well as allocation strategy. The suggested process model overcomes the limitation of a conventional life cycle assessment study which considers the process as a ‘black box’ and allows for an identification of further possibilities to implement sustainable nickel production.
    [Show full text]