Electrochemical Studies of Catalysed Aqueous Sulphide Oxidation

Total Page:16

File Type:pdf, Size:1020Kb

Electrochemical Studies of Catalysed Aqueous Sulphide Oxidation 1 Electrochemical Studies of Catalysed Aqueous Sulphide Oxidation A thesis submitted for the degree of Doctor of Philosophy of the University of London and The Diploma of Imperial College by Ian Thompson Department of Mineral Resources Engineering Sept. 1987 Imperial College of Science and Technology University of London LONDON SW7 2BP But it's all right now, In fact it's a Gas Gas Gas! Mick Jagger (1968) Abstract 3 Abstract Electrochemical Studies of Catalysed Aqueous Sulphide Oxidation This thesis concerns the mechanism of oxidation of aqueous sulphide solutions in the British Gas Stretford Process, which uses atmospheric oxygen to achieve the partial oxidation of hydrogen sulphide, producing elemental sulphur and water. Hydrogen sulphide is absorbed in an alkaline solution (pH 8.5-9.5) containing vanadium (V) salts and anthraquinone derivatives which act as oxidation catalysts. The important methods of removing hydrogen sulphide from fuel gases were reviewed, and a detailed description of the Stretford Process was provided. The thermodynamic data on sulphur species were presented in the form of Eh/pH diagrams, and the literature relating to the oxidation of sulphide solutions was surveyed. The redox behaviour of sulphide and polysulphide solutions were investigated using electrochemical techniques such as cyclic and pulse voltammetry at gold ring-disc electrodes. It was shown that polysulphide species were important intermediates in the oxidation of HS" ions. The aqueous chemistry of vanadium was described and the electrochemical behaviour of vanadium (V) and (IV) solutions at pH 9.2 were investigated at mercury, carbon and gold electrodes. The electrochemical reduction of vanadium (V) was shown to be irreversible and to lead to vanadium oxide films, rather than to solution species. The redox chemistry of anthraquinone was reviewed and electrochemical studies were made of the compound anthraquinone 2,7-disulphonate. The reduced species and intermediates were identified using UV-visible spectrophotometry and ESR spectroscopy. The reduction pathways of oxygen in alkaline solution were reviewed, and the role of hydrogen peroxide as a possible reactive intermediate was investigated. The Stretford Process chemistry was examined using stopped-flow spectroscopic methods; these enabled the courses of the redox reactions between sulphide solutions and solutions containing the catalysts to be followed. A mechanism was proposed for the Stretford Process, and possible process improvements were discussed. Acknowledgements 4 Acknowledgements I would like to thank Dr. G. H. Kelsall for his supervision during the course of this work. Thanks must also go to Dr. T. Ritter from the British Gas London Research Station and to the other staff there who have given me help; Dr. D. Keene, Dr R. Mounce, Dr R. Gibbons, Roy Lowry, Lucien Anthony, and Susan Mahony. From Imperial College I would particularly like to thank Gordon "the glass" as well as the other technical and academic staff in the Mineral Resources Engineering and the Chemistry Departments. Research is not carried out alone. The present and past members of the research group have both aided my studies and, through their company, made them more enjoyable. Thank you. I would also like to acknowledge the financial help of British Gas, the Science and Engineering Research Council and last but definitely not least, Corina Thompson. Contents 5 Contents Abstract 3 Acknowledgements 4 Contents 5 List of Figures 9 List of Tables 12 1. Introduction: The Importance of Sulphide Oxidation 14 1.1 The Removal of Hydrogen Sulphide 14 1.1.1 Absorption by liquids 15 1.1.2 Adsorption by solids 16 1.1.3 Electrochemical oxidation of hydrogen sulphide 17 1.1.4 Aqueous oxidation of hydrogen sulphide 18 1.2 The Stretford Process 19 1.2.1 Historical development 2 0 1.2.2 Operational Problems 21 1.2.3 Mechanistic studies 23 1.3 Objectives of the Present Study 25 1.3.1. Research Approach 2 5 2. Review of Sulphide Oxidation 2 6 2 .1 The Oxidation States of Sulphur 2 9 2.1.1 Sulphide (-II) 2 9 2.1.2 Poly sulphides (-1 to 0) 3 0 2.1.3 Elemental Sulphur (0) 3 2 2.1.4 Polythionates (0 to IV) 3 3 2.1.5 Thiosulphate (II) 33 2.1.6 Sulphite (IV) 3 4 2.1.7 Sulphate (VI) 3 4 2.2 Electrochemical Studies of Sulphide Oxidation 3 4 2.3 Chemical Oxidation of Sulphide using Oxygen 3 7 2.3.1 Rate of Reaction of Sulphide Solutions with Oxygen 3 8 2.3.2 Effect of Temperature and pH on Reaction Rate 3 9 2.3.3 Catalysis of Sulphide Oxidation 3 9 2.3.4 B acterial Action in S ulphide Oxidation 4 0 2.4 The Production of Elemental Sulphur 4 0 Contents 6 3. Sulphide Electrochemistry 41 3.1 Thermodynamic Calculations 43 3.2 Experimental 44 3.2.1 Solution Preparation 45 3.2.2 Electrochemical Instrumentation 46 3.2.3 Electrode Pretreatment 47 3.2.4 Experimental: Ion chromatography 4 8 3.3 Sulphide Voltammetry: Results and Discussion 5 0 3.4 Thiosulphate Voltammetry: Results and Discussion 51 3.5 Polysulphide Voltammetry: Results and Discussion 53 3.6 Ring-Disc Studies: Results and Discussion 56 3.7 Calculated Polysulphide Concentrations vs. Potential 62 3.8 Detection of Polysulphides Using Ion Chromatography 64 3.8.1 Ion Chromatography: Results and Discussion 6 4 3.9 Summary 65 4. Vanadium 66 4.1 Vanadium (V) 67 4.2 Vanadium (IV) 7 0 4.3 Vanadium (V)/(IV) Compounds 72 4.4 Vanadium (III) 74 4.5 Vanadium (II) 7 4 4.6 Vanadium Electrochemistry 75 4.6.1 The Vanadium (V)/(IV) Couple 7 5 4.6.2 Vanadium (TV) reduction 76 4.6.3 The Vanadium (ffl)/(II) Couple 76 4.7 Oxidation of Vanadium (IV) solutions using Oxygen 76 4.8 Vanadium Sulphides 7 7 4.8.1 V3S,V5S4,VS 77 4.8.2 V2S5 78 4.8.3 VS2andVS4 78 4.9 Vanadium-Sulphur Complexes 7 8 4.10 Summary 80 5. Vanadium Electrochemistry 82 5.1 Vanadium Electrochemistry: Experimental 82 5.1.1 Solution Preparation 83 5.2 Vanadium (V) Voltammetry: Results and Discussion 84 5.3 Summary 91 Contents 7 6. Review of Anthraquinone Redox Chemistry 9 2 6.1 Anthraquinone Reduction 9 2 6.1.1 Substituent effects 9 4 6.1.2 Photo-reduction 9 5 6.2 Anthraquinones in the Production of Hydrogen Peroxide 9 6 7. Redox Chemistry of Anthraquinone 2,7-disulphonate 9 7 7.1 Purification of Anthraquinone 2,7-disulphonate 9 7 7.1.1 Analysis of the Purified Material 9 7 7.2 Experimental: Voltammetry 9 8 7.3 Experimental: Exhaustive Electrolysis 9 9 7.3.1 Calculations: Exhaustive Electrolysis 100 7.3.2 Calibration of Exhaustive Electrolysis Apparatus 101 7.4 Voltammetry: Results and Discussion 103 7.5 Exhaustive Electrolysis: Results and Discussion 108 7.6 UV-Visible Spectrophotometry: Experimental 111 7.7 Results and Discussion: UV-Visible Spectrophotometry 113 7.7.1 Spectral Assignments 114 7 .8 ESR Spectroscopy: Experimental 116 7 .9 ESR Spectroscopy: Results and Discussion 117 7 .1 0 ESR Spectral Structure 119 7.11 Summary 120 8. Oxygen Reduction 122 8.1 The Oxygen / Water Couple 124 8.1.1 The Evolution of Oxygen 126 8.2 Hydrogen Peroxide 127 8.3 Superoxides 129 8.4 Experimental 129 8.5 Oxygen Reduction: Results and Discussion 130 8.6 Summary 132 Contents 8 9. The Redox Chemistry of the Stretford Process 133 9.1 Experimental 133 9.1.1 S topped Flow Apparatus 134 9.1.2 Experimental: Measurement of Solution Potential 135 9.1.3 Experimental: Preparation o f51V NMR Samples 136 9.2 Reaction of AQ27DS and HS“: Stopped Flow Results 137 9.2.1 Rate Studies 138 9.2.2 S olution Potential Measurements 140 9.3 Reaction of V(V) and HS“: Stopped Flow Results 142 9.3.1 Vanadium (V) Reduction 144 9.4 Interaction of AQ27DH" ions with Oxygen 147 9.5 Stretford Solution Chemistry: Electrochemical Results 148 9.6 The Stretford Process: Possible Mechanism 150 10. Conclusions 152 10.1 The S(-II)/S(0) Redox Couple 152 10.2 The V(V)/V(IV) Redox Couple 152 10.3 The Anthraquinone/Anthraquinol Redox Couple 153 10.4 The C^/OH- Redox Couple 154 10.5 The Redox Chemistry of the Stretford Process 154 10.6 The Mechanism of the Stretford Process 155 10.7 Concluding Remarks 156 Appendix: Thermodynamic Data Used in Eh-pH Diagrams 158 References 161 Figures 9 List of Figures 1 .1 The Stretford Process. 19 2 .1 Possible valence states of sulphur in aqueous media. 2 6 2 .2 Efo-pH diagram for the sulphur/water system at 298 K. 27 2 .3 . Efo-pH diagram for metastable sulphur system at 298 K. 2 8 2 .4 E^-pH diagram for the sulphur/water system at 298 K. 2 9 (Oxy-sulphur anions not considered.) 3 .1 Eh-pH Diagram for the Au/Cl/S System. 4 2 3 .2 Eh-pH diagram for the sulphur/water system at 298 K. 43 3 .3 Metastable Eh-pH diagram for the S/H20 system at 298 K. 44 3 .4 A Rotating Ring Disc Electrode. 4 4 3 .5 Ion Chromatography Apparatus. 4 9 3 .6 Voltammogram of HS~ on Gold Plated Disc Electrode. 5 0 ([HS_] = 10 mol m-3, pH = 9.2, nth. cycle, 20 mV s_1.) 3 .7 Cyclic Voltammograms of Sodium Thiosulphate. 5 2 ([Na2S2C>3] = 10 mol m~3. 1st Scans. 100 mV s-1. pH = 8.2.) 3 .8 Voltammograms of Polysulphide Solution at a Gold Disc. 5 3 ([Sx] = 1 mol m-3.
Recommended publications
  • ANTHRAQUINONE and ANTHRONE SERIES Part IX
    ANTHRAQUINONE AND ANTHRONE SERIES Part IX. Chromatographic Adsorption of Aminoanthraquinones on Alumina BY N. R. RAo, K. H. SHAH AND K. VENKATARAMAN, F.A.Sc. (Department of Chemical Technology. University of Bombay, Bombay) Received November 10, 1951 CORRELATIONS between chemical constitution and chromatograpl~c behaviour can only be attempted in molecales of the same or similar types and under specified conditions of chromatographic treatment, since complex solvent- adsorbent, solute-solvent and solute-adsorbent relationships are involved. Changes in the sequence of adsorption of the constituents in a mixture have been observed, ooth when the adsorbent is changed and when the deve- loping solvent is changed. Thus Strain was able tc separate some ternary mixtures in four of the six pessible sequences by changing the solvent1; and LeRosen found that cryptoxanthin is aloove lycopene on alumina and on calcium carbonate columns, but the order is inverted on a column of calcium hydroxide, using benzene as developer with all the three adsoroents. 2 An inversion of the sequence of adsorption of N-ethyl-N, N'-diphenylurea and 4-nitro-N-ethylaniline was observed by Schroeder when a slight alteration in the composition of the developer (2 or 5~o of ethyl acetate in light petro- leum) was made. 3 LeRosen has defined the adsorption affinity R as the rate of movement of the adsorptive zone (mm./min.) divided by the rate of flow of developing solvent. 2 R values have been used for standardizing adsorbents and for determining the efficiency of developers; using the same adsorbent and solvent, R values provide a quantitative measure of the adsorption affinities of a series of compounds which can then be correlated with their chemical constitution.
    [Show full text]
  • Opinion on the SCCNFP on Disperse Violet 1 Impurified with Disperse Red
    SCCNFP/0504/01, final OPINION OF THE SCIENTIFIC COMMITTEE ON COSMETIC PRODUCTS AND NON-FOOD PRODUCTS INTENDED FOR CONSUMERS CONCERNING DISPERSE VIOLET 1 IMPURIFIED WITH DISPERSE RED 15 Colipa n° C64 & C61 adopted by the SCCNFP during the 19th Plenary meeting of 27 February 2002 SCCNFP/0504/01, final Evaluation and opinion on : Disperse Violet 1 impurified with Disperse Red 15 ____________________________________________________________________________________________ 1. Terms of Reference 1.1 Context of the question The adaptation to technical progress of the Annexes to Council Directive 76/768/EEC of 27 July 1976 on the approximation of the laws of the Member States relating to cosmetic products. 1.2 Request to the SCCNFP The SCCNFP is requested to answer the following questions : * Is Disperse Violet 1 impurified with Disperse Red 15 safe for use in cosmetic products? * Does the SCCNFP propose any restrictions or conditions for its use in cosmetic products? 1.3 Statement on the toxicological evaluation The SCCNFP is the scientific advisory body to the European Commission in matters of consumer protection with respect to cosmetics and non-food products intended for consumers. The Commission’s general policy regarding research on animals supports the development of alternative methods to replace or to reduce animal testing when possible. In this context, the SCCNFP has a specific working group on alternatives to animal testing which, in co-operation with other Commission services such as ECVAM (European Centre for Validation of Alternative Methods), evaluates these methods. The extent to which these validated methods are applicable to cosmetic products and its ingredients is a matter of the SCCNFP.
    [Show full text]
  • 95[.95]Functionalizable Glyconanoparticles for A
    nanomaterials Communication Functionalizable Glyconanoparticles for a Versatile Redox Platform Marie Carrière 1,2, Paulo Henrique M. Buzzetti 1 , Karine Gorgy 1, Muhammad Mumtaz 2, Christophe Travelet 2 , Redouane Borsali 2,* and Serge Cosnier 1,* 1 UMR 5250, Département de Chimie Moléculaire, CNRS, Université Grenoble Alpes, CEDEX 09, 38058 Grenoble, France; [email protected] (M.C.); [email protected] (P.H.M.B.); [email protected] (K.G.) 2 CERMAV, UPR 5301, CNRS, Université Grenoble Alpes, CEDEX 09, 38058 Grenoble, France; [email protected] (M.M.); [email protected] (C.T.) * Correspondence: [email protected] (R.B.); [email protected] (S.C.) Abstract: A series of new glyconanoparticles (GNPs) was obtained by self-assembly by direct nano- precipitation of a mixture of two carbohydrate amphiphilic copolymers consisting of polystyrene- block-β-cyclodextrin and polystyrene-block-maltoheptaose with different mass ratios, respectively 0–100, 10–90, 50–50 and 0–100%. Characterizations for all these GNPs were achieved using dynamic light scattering, scanning and transmission electron microscopy techniques, highlighting their spher- ical morphology and their nanometric size (diameter range 20–40 nm). In addition, by using the inclusion properties of cyclodextrin, these glyconanoparticles were successfully post-functionalized using a water-soluble redox compound, such as anthraquinone sulfonate (AQS) and characterized by cyclic voltammetry. The resulting glyconanoparticles exhibit the classical electroactivity of free AQS in solution. The amount of AQS immobilized by host–guest interactions is proportional to the percentage of polystyrene-block-β-cyclodextrin entering into the composition of GNPs.
    [Show full text]
  • Structural Changes and Dynamic Behaviour of Vanadium Oxide‐Based Catalysts for Gas‐Phase Selective Oxidations
    Alma Mater Studiorum ‐ Università di Bologna Facoltà di Chimica Industriale Dipartimento di Chimica Industriale e dei Materiali Structural changes and dynamic behaviour of vanadium oxide‐based catalysts for gas‐phase selective oxidations Tesi di Dottorato di Ricerca Presentata da: Relatore: Dott.ssa Silvia Luciani Prof. Fabrizio Cavani Co‐relatore: Dott. Nicola Ballarini Coordinatore: Chiar.mo Prof. Luigi Angiolini Dottorato di Ricerca in Chimica Industriale (settore CHIM/04) ciclo XXI Esame finale anno 2009 Index INDEX ABSTRACT 1 PART A 5 1 Introduction 7 1.1 Maleic Anhydride: production and uses 7 1.1.1 Maleic Anhydride uses 8 1.1.2 Maleic Anhydride production 9 1.2 Catalytic System 16 1.2.1 Synthesis of vanadyl pyrophosphate 16 1.2.2 P/V ratio 21 1.2.3 The role of the different V species 21 1.2.4 Supported systems 22 1.2.5 Recent developments to improve the catalytic system 25 1.3 Reaction scheme and mechanism 28 1.3.1 Reaction scheme 28 1.3.2 Reaction mechanism 30 1.3.3 Nature of active sites 31 1.4 References 34 2 Experimental 41 2.1 Catalysts synthesis 41 2.1.1 Synthesis of vanadyl pyrophosphate, (VO)2P2O7 41 2.1.2 Synthesis of supported catalysts 42 2.2 Samples characterization 42 2.3 Catalytic tests 43 2.3.1 Bench scale plant 43 2.3.2 Analytical system 45 2.3.3 Elaboration of catalytic data 46 I Index 3 Surface dynamic of V/P/O catalyst 47 3.1 Introduction 47 3.2 Experimental 48 3.3 Results and discussion 49 3.3.1 “In‐situ” calcination 49 3.3.2 Ex‐situ characterization 52 3.3.3 “In‐situ” Raman spectroscopy 55 3.3.4 Steady state
    [Show full text]
  • Process for Preparation of Hydrogen Peroxide
    Europaisches Patentamt J) European Patent Office ® Publication number: 0 286 610 Office europeen des brevets A2 EUROPEAN PATENT APPLICATION Application number: 88850082.4 ® Int.CI.4: C 01 B 15/023 Date of filing: 09.03.88 Priority: 27.03.87 SE 8701293 @ Applicant: Eka Nobel Aktiebolag S-44501Surte (SE) Date of publication of application: 12.10.88 Bulletin 88/41 @ Inventor: Bengtsson, Erik Alvar Asbacken 45 Designated Contracting States: S-44500Surte (SE) AT BE DE FR GB IT SE Andersson, Ulf, Mikael Bangegatan 2B S-41504G6teborg (SE) @ Representative: Schold, Zaid c/o Nobel Industries Sweden AB Patent Department Box 11554 S-1 00 61 Stockholm (SE) @ Process for preparation of hydrogen peroxide. (57) A process for the production of hydrogen peroxide according to the anthraquinone process. According to the process certain alkyl substituted caprolactames are used as solvents, and particularly as solvents for anthrahydroquinones. The substituted caprolactames, which for example can be hexyl caprolactam and octyl caprolactam, give a very good solubility for anthrahydroquinones and also for anthraquinones. The compounds can be used as the sole solvent at the production of hydrogen peroxide or in combination with conventionally used solvents such CM as hydrocarbons. < O to CO 00 CM Q_ LLJ Bundesdruckerei Berlin 0 286 610 , Description A process for the production of hydrogen peroxide The present invention relates to the production of hydrogen peroxide according to the per se well known anthraquinone process. More particularly the invention relates to the production of hydrogen peroxide 5 according to the anthraquinone process using particular solvents which give very good solubility for anthrahydroquinones and also for anthraquinones.
    [Show full text]
  • The Anthraquinone Process
    COVER STORY: H₂O₂ BACKGROUND How H₂O₂ is produced: The anthraquinone process Healthy and durable: In The industrial production of hydrogen peroxide began in the town of Weißenstein in the Austrian state of the food industry, PET bottles are sterilized Carinthia. This is where the Österreichische Chemische Werke company operated the world’s first hydrogen with hydrogen peroxide peroxide factory using electrolysis. Today this production plant is part of Evonik. The Weißenstein process before being filled made it possible to produce hydrogen peroxide on an industrial scale for the first time. Today this plant uses the autoxidation process, as do almost all the other hydrogen peroxide factories in the world. This process was developed by Georg Pfleiderer and Hans-Joachim Riedl at IG Farben in Ludwigshafen between 1935 and 1945, and since then it has been continuously refined. The process is based on the cyclical reduction and oxidation of an alkylated anthraquinone. The first step, hydrogenation, takes place in a reactor full of a solution of the anthraquinone (the “working solution”). “In the reactor, in the presence of a palladium catalyst hydrogen combines with the reaction carrier, a quinone derivative, to form a hydroquinone,” explains Dr. Jürgen Glenneberg, Head of Process Engineering at the Active Oxygens Business Line. The catalyst is then completely filtered out of the working solution. In the second step, the oxidation stage, huge compressors pump air into a bubble reactor that is full of the working solution. When the hydroquinone in the organic phase comes into contact with the oxygen in the air, it oxidizes spontaneously back into quinone, forming hydrogen peroxide in the process.
    [Show full text]
  • Managing Hazardous Materials Incidents
    1,3-Butadiene 1,3-Butadiene (C4 H6 ) CAS 106-99-0; UN 1010 Synonyms include butadiene, buta-1,3-diene, biethylene, bivinyl, vinylethylene, erythrene, ",(-butadiene, divinyl, and pyrrolylene. • Persons exposed to 1,3-butadiene gas do not pose a significant risk of secondary contamination to response personnel outside the Hot Zone. Persons whose skin or clothing has been contaminated with liquid 1,3-butadiene can secondarily contaminate response personnel by direct contact or through off-gassing vapor. • 1,3-Butadiene is a colorless, highly flammable gas at room temperature. The gas is heavier than air and potentially explosive. It has a mild, aromatic, gasoline-like odor that is often an adequate warning to protect against acute overexposure. • The major route of exposure to 1,3-butadiene is inhalation. 1,3-Butadiene escaping its container in liquid or gas form can produce irritation or frostbite injury. Significant dermal absorption is unlikely. • 1,3-Butadiene’s extreme flammability and potential for explosion is probably of greater health concern than its toxic effects. Description 1,3-Butadiene is a colorless gas with a mild, aromatic, gasoline- like odor. It is non-corrosive but highly flammable. The vapor is heavier than air. 1,3- Butadiene is commercially available as a liquefied gas (under pressure) with a stabilizer added for shipment. Liquid 1,3-butadiene floats and boils on water. Because of 1,3-butadiene’s physical properties (e.g., low flashpoint and tendency to polymerize), its fire and explosion potential might be greater concerns (more likely to occur and more dangerous) than its health effects.
    [Show full text]
  • Cyclic Sequential Removal of Alizarin Red S Dye and Cr(VI) Ions Using Wool As a Low-Cost Adsorbent
    processes Article Cyclic Sequential Removal of Alizarin Red S Dye and Cr(VI) Ions Using Wool as a Low-Cost Adsorbent Mustafa I. Khamis 1, Taleb H. Ibrahim 2,*, Fawwaz H. Jumean 1, Ziad A. Sara 1 and Baraa A. Atallah 1 1 Department of Biology, Chemistry and Environmental Sciences, American University of Sharjah, Sharjah 26666, UAE; [email protected] (M.I.K.); [email protected] (F.H.J.); [email protected] (Z.A.S.); [email protected] (B.A.A.) 2 Department of Chemical Engineering, American University of Sharjah, Sharjah 26666, UAE * Correspondence: [email protected]; Tel.: +971-507769239 Received: 22 April 2020; Accepted: 5 May 2020; Published: 9 May 2020 Abstract: Alizarin red S (ARS) removal from wastewater using sheep wool as adsorbent was investigated. The influence of contact time, pH, adsorbent dosage, initial ARS concentration and temperature was studied. Optimum values were: pH = 2.0, contact time = 90 min, adsorbent dosage = 8.0 g/L. Removal of ARS under these conditions was 93.2%. Adsorption data at 25.0 ◦C and 90 min contact time were fitted to the Freundlich and Langmuir isotherms. R2 values were 0.9943 and 0.9662, respectively. Raising the temperature to 50.0 ◦C had no effect on ARS removal. Free wool and wool loaded with ARS were characterized by Fourier Transform Infrared Spectroscopy (FTIR). ARS loaded wool was used as adsorbent for removal of Cr(VI) from industrial wastewater. ARS adsorbed on wool underwent oxidation, accompanied by a simultaneous reduction of Cr(VI) to Cr(III). The results hold promise for wool as adsorbent of organic pollutants from wastewater, in addition to substantial self-regeneration through reduction of toxic Cr(VI) to Cr(III).
    [Show full text]
  • United States Patent (19) 11) 4,379,092 Devic 45) Apr
    United States Patent (19) 11) 4,379,092 Devic 45) Apr. 5, 1983 2,401,225 5/1946 Caesar et al. ................... 260/384 X 54 PROCESS FOR THE PREPARATION OF ANTHRAQUINONE AND ITS SUBSTITUTED 2,842,562 7/1958 Bloom et al......................... 260/369 DERVATIVES 2,871,244 l/1959 Kamlet ................................ 260/369 2,967,187 1/1961 Serres et al. .................... 260/384 X 75 Inventor: Michel Devic, Lyons, France 73) Assignee: PC UK Produits Chimiques Ugine FOREIGN PATENT DOCUMENTS 634987 8/1936 Fed. Rep. of Germany ...... 260/369 Kuhlmann, Courbevoie, France 2031430 2/1972 Fed. Rep. of Germany ...... 260/369 (21) Appl. No.: 324,520 2262007 9/1975 France ................................ 260/369 22 Filed: Nov. 24, 1981 2307786 11/1976 France ................................ 260/369 Primary Examiner-Paul F. Shaver (30) Foreign Application Priority Data Attorney, Agent, or Firm-Beveridge, DeGrandi & Dec. 16, 1980 FR) France ................................ 80 26637 Kline 51) Int. Cl. ......................... C07C 50/18; C09B 1/00 57 ABSTRACT 52 U.S. Cl. ..................................... 260/369; 260/384 58) Field of Search ................................ 260/369,384 A process for the preparation of anthraquinone com pounds by condensation of phthalic anhydride with a 56 References Cited benzene derivative wherein a mixture of hydrofluoric U.S. PATENT DOCUMENTS acid and boron trifluoride is utilized as catalyst. l,515,325 11/1924 Bailey .................................. 260/369 2,174,118 9/1939 Calcott et al. ...................... 260/35 7 Claims, No Drawings 4,379,092 1. 2 molecular mixture of HF and BF3 does not cause cycli PROCESS FOR THE PREPARATION OF zation is quite unexpected since the cyclization of benz ANTHRAQUINONE AND ITS SUBSTITUTED oyl-benzoic acid takes place in anhydrous HF (U.S.
    [Show full text]
  • Extraction of Byproducts of Hydrogen Peroxide Working Solution Using Solvent
    "Science Stays True Here" Biological and Chemical Research, Volume 2014, 34-39 | Science Signpost Publishing Extraction of Byproducts of Hydrogen Peroxide Working Solution Using Solvent M Arshad Majeed, Suneela Sardar and S R Malik NFC Institute of Engineering and Fertilizer Research, Faisalabad. Received: September 03, 2014 / Accepted: September 27, 2014 / Published: November 25, 2014 Abstract: Working solution comprising anthraquinone and its derivatives, used for preparation of hydrogen peroxide, leads to the formation of byproducts. These byproducts contain highly complex mixture of degradation products, which cannot take active part in the production of hydrogen peroxide, and cause higher viscosity and density of working solution. The low viscosity is important for mechanical reasons in cycling of the working solution through the equipment and density must be substantially different from the density of the water hydrogen peroxide solution resulting from water extraction of the hydrogen peroxide from the organic phase, in order to facilitate the extraction. The degradation products must be extracted from the working solution to prevent deteriorating the crude hydrogen peroxide color, smell, dissolved organic compounds and increase in density and viscosity of the working solution. A decrease in surface tension of the working solution promotes the formation of an emulsion during extraction degradation products decrease the activity and life time of the hydrogenation catalyst. Regeneration of the working solution for bringing it back to the good health a solvent Tetra Butyl Urea (TBU) is added in degraded working solution in a different proportion. Keywords: Regeneration, Anthraquinone, Tetra Butyl Urea, Degradation. 1. Introduction Widely used method for production of hydrogen peroxide is auto-oxidation process in which 2-ethyl-anthraquinone (EAQ) is dissolved in a carrier solvent such as Tri-Octyl Phosphate(TOP) and Tri methyl Benzene(TMB).
    [Show full text]
  • PROVISIONAL PEER REVIEWED TOXICITY VALUES for ALIZARIN RED COMPOUNDS (VARIOUS CASRNS) Derivation of Subchronic and Chronic Oral Rfds
    EPA/690/R-04/001F l Final 12-20-2004 Provisional Peer Reviewed Toxicity Values for Alizarin Red Compounds (Various CASRNs) Derivation of Subchronic and Chronic Oral RfDs Superfund Health Risk Technical Support Center National Center for Environmental Assessment Office of Research and Development U.S. Environmental Protection Agency Cincinnati, OH 45268 Acronyms and Abbreviations bw body weight cc cubic centimeters CD Caesarean Delivered CERCLA Comprehensive Environmental Response, Compensation and Liability Act of 1980 CNS central nervous system cu.m cubic meter DWEL Drinking Water Equivalent Level FEL frank-effect level FIFRA Federal Insecticide, Fungicide, and Rodenticide Act g grams GI gastrointestinal HEC human equivalent concentration Hgb hemoglobin i.m. intramuscular i.p. intraperitoneal i.v. intravenous IRIS Integrated Risk Information System IUR inhalation unit risk kg kilogram L liter LEL lowest-effect level LOAEL lowest-observed-adverse-effect level LOAEL(ADJ) LOAEL adjusted to continuous exposure duration LOAEL(HEC) LOAEL adjusted for dosimetric differences across species to a human m meter MCL maximum contaminant level MCLG maximum contaminant level goal MF modifying factor mg milligram mg/kg milligrams per kilogram mg/L milligrams per liter MRL minimal risk level i MTD maximum tolerated dose MTL median threshold limit NAAQS National Ambient Air Quality Standards NOAEL no-observed-adverse-effect level NOAEL(ADJ) NOAEL adjusted to continuous exposure duration NOAEL(HEC) NOAEL adjusted for dosimetric differences across species
    [Show full text]
  • Development of Textile Dyeing Using the Green Supercritical Fluid Technology: a Review
    https://doi.org/10.33263/Materials23.373390 ISSN: 2668-5728 https://materials.international Volume 2, Issue 3, Pages 0373-0390 2020 Received: 9.06.2020 Accepted: 2.09.2020 Review Published: 10.09.2020 Development of Textile Dyeing Using the Green Supercritical Fluid Technology: A Review Tarek Abou Elmaaty* 1 , Abdallah Mousa 2 , Hatem Gaafar 2 , Ali Hebeish 2 , Heba Sorour 1 1 Department of Textile Printing, Dyeing & Finishing, Faculty of Applied Arts, Damietta University, Damietta 34512, Damietta, Egypt 2 Department of Textile Printing, Dyeing & auxiliaries, National research center, Cairo, Egypt * Correspondence: [email protected]; Scopus ID: 6603460941 Abstract: Recently, a green supercritical carbon dioxide dyeing process with zero waste-water emission is a hot topic. This review gives light on advances in recent years, including solubilities of different dyes in the supercritical solvent as well as most recent reports about the dyeing of synthetic and natural fibers under supercritical carbon dioxide medium. Keywords: supercritical carbon dioxide; solubility; synthetic fibers; natural fibers; dyes. © 2020 by the authors. This article is an open-access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/). 1. Introduction Supercritical carbon dioxide (scCO2) is an eco- disposal in the water streamlet [6,7]. Textile wet friendly solvent known for its potentiality as a processing can outstandingly get an advantage from replacement for aqueous textile wet processing, the utilization of scCO2 as a dyeing medium. scCO2 mainly dyeing [1-4]. A supercritical fluid is a matter has lower mass transfer resistance and higher in a closed system above its critical temperature and diffusion rates than water.
    [Show full text]