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Frequency and Potential Dependence of Reversible Electrocatalytic Hydrogen Interconversion by [Fefe]-Hydrogenases
Frequency and potential dependence of reversible electrocatalytic hydrogen interconversion by [FeFe]-hydrogenases Kavita Pandeya,b, Shams T. A. Islama, Thomas Happec, and Fraser A. Armstronga,1 aInorganic Chemistry Laboratory, Department of Chemistry, University of Oxford, Oxford OX1 3QR, United Kingdom; bSchool of Solar Energy, Pandit Deendayal Petroleum University, Gandhinagar 382007, Gujarat, India; and cAG Photobiotechnologie Ruhr–Universität Bochum, 44801 Bochum, Germany Edited by Thomas E. Mallouk, The Pennsylvania State University, University Park, PA, and approved March 2, 2017 (received for review December 5, 2016) The kinetics of hydrogen oxidation and evolution by [FeFe]- CrHydA1 contains only the H cluster: in the living cell, it receives hydrogenases have been investigated by electrochemical imped- electrons from photosystem I via a small [2Fe–2S] ferredoxin ance spectroscopy—resolving factors that determine the excep- known as PetF (19). No accessory internal Fe–S clusters are tional activity of these enzymes, and introducing an unusual and present to mediate or store electrons. powerful way of analyzing their catalytic electron transport prop- For enzymes, PFE has focused entirely on net catalytic electron erties. Attached to an electrode, hydrogenases display reversible flow that is observed as direct current (DC) in voltammograms + electrocatalytic behavior close to the 2H /H2 potential, making (2, 3, 10). Use of DC cyclic voltammetry as opposed to single them paradigms for efficiency: the electrocatalytic “exchange” rate potential sweeps alone helps to distinguish rapid, steady-state (measured around zero driving force) is therefore an unusual pa- catalytic activity at different potentials from relatively slow, rameter with theoretical and practical significance. Experiments potential-dependent changes in activity that are revealed as were carried out on two [FeFe]-hydrogenases, CrHydA1 from the hysteresis (10). -
N,N-Dimethylformamide
This report contains the collective views of an international group of experts and does not necessarily represent the decisions or the stated policy of the United Nations Environment Programme, the International Labour Organization, or the World Health Organization. Concise International Chemical Assessment Document 31 N,N-DIMETHYLFORMAMIDE Please note that the layout and pagination of this pdf file are not identical to those of the printed CICAD First draft prepared by G. Long and M.E. Meek, Environmental Health Directorate, Health Canada, and M. Lewis, Commercial Chemicals Evaluation Branch, Environment Canada Published under the joint sponsorship of the United Nations Environment Programme, the International Labour Organization, and the World Health Organization, and produced within the framework of the Inter-Organization Programme for the Sound Management of Chemicals. World Health Organization Geneva, 2001 The International Programme on Chemical Safety (IPCS), established in 1980, is a joint venture of the United Nations Environment Programme (UNEP), the International Labour Organization (ILO), and the World Health Organization (WHO). The overall objectives of the IPCS are to establish the scientific basis for assessment of the risk to human health and the environment from exposure to chemicals, through international peer review processes, as a prerequisite for the promotion of chemical safety, and to provide technical assistance in strengthening national capacities for the sound management of chemicals. The Inter-Organization Programme for the Sound Management of Chemicals (IOMC) was established in 1995 by UNEP, ILO, the Food and Agriculture Organization of the United Nations, WHO, the United Nations Industrial Development Organization, the United Nations Institute for Training and Research, and the Organisation for Economic Co-operation and Development (Participating Organizations), following recommendations made by the 1992 UN Conference on Environment and Development to strengthen cooperation and increase coordination in the field of chemical safety. -
Safety Data Sheet
SAFETY DATA SHEET Creation Date 03-Sep-2009 Revision Date 17-Jan-2018 Revision Number 4 1. Identification Product Name N,N-Dimethylformamide Cat No. : D131-1; D131-4 CAS-No 68-12-2 Synonyms DMF Recommended Use Laboratory chemicals. Uses advised against Not for food, drug, pesticide or biocidal product use Details of the supplier of the safety data sheet Company Fisher Scientific One Reagent Lane Fair Lawn, NJ 07410 Tel: (201) 796-7100 Emergency Telephone Number CHEMTRECÒ, Inside the USA: 800-424-9300 CHEMTRECÒ, Outside the USA: 001-703-527-3887 2. Hazard(s) identification Classification This chemical is considered hazardous by the 2012 OSHA Hazard Communication Standard (29 CFR 1910.1200) Flammable liquids Category 3 Acute dermal toxicity Category 4 Acute Inhalation Toxicity - Vapors Category 4 Serious Eye Damage/Eye Irritation Category 2 Reproductive Toxicity Category 1B Specific target organ toxicity (single exposure) Category 3 Target Organs - Respiratory system, Central nervous system (CNS). Label Elements Signal Word Danger Hazard Statements Flammable liquid and vapor Harmful in contact with skin Causes serious eye irritation Harmful if inhaled May cause respiratory irritation May cause drowsiness or dizziness May damage the unborn child ______________________________________________________________________________________________ Page 1 / 8 N,N-Dimethylformamide Revision Date 17-Jan-2018 ______________________________________________________________________________________________ Precautionary Statements Prevention Obtain special instructions before use Do not handle until all safety precautions have been read and understood Use personal protective equipment as required Use only outdoors or in a well-ventilated area Wash face, hands and any exposed skin thoroughly after handling Wear eye/face protection Do not breathe dust/fume/gas/mist/vapors/spray Keep away from heat/sparks/open flames/hot surfaces. -
Synergistic Effect of 2-Acrylamido-2-Methyl-1-Propanesulfonic Acid on the Enhanced Conductivity for Fuel Cell at Low Temperature
membranes Article Synergistic Effect of 2-Acrylamido-2-methyl- 1-propanesulfonic Acid on the Enhanced Conductivity for Fuel Cell at Low Temperature Murli Manohar * and Dukjoon Kim * School of Chemical Engineering, Sungkyunkwan University, Suwon, Kyunggi 16419, Korea * Correspondence: [email protected] (M.M.); [email protected] (D.K.) Received: 3 November 2020; Accepted: 10 December 2020; Published: 15 December 2020 Abstract: This present work focused on the aromatic polymer (poly (1,4-phenylene ether-ether-sulfone); SPEES) interconnected/ cross-linked with the aliphatic monomer (2-acrylamido -2-methyl-1-propanesulfonic; AMPS) with the sulfonic group to enhance the conductivity and make it flexible with aliphatic chain of AMPS. Surprisingly, it produced higher conductivity than that of other reported work after the chemical stability was measured. It allows optimizing the synthesis of polymer electrolyte membranes with tailor-made combinations of conductivity and stability. Membrane structure is characterized by 1H NMR and FT-IR. Weight loss of the membrane in Fenton’s reagent is not too high during the oxidative stability test. The thermal stability of the membrane is characterized by TGA and its morphology by SEM and SAXS. The prepared membranes improved 1 proton conductivity up to 0.125 Scm− which is much higher than that of Nafion N115 which is 1 0.059 Scm− . Therefore, the SPEES-AM membranes are adequate for fuel cell at 50 ◦C with reduced relative humidity (RH). Keywords: 2-acrylamido-2-methyl-1-propanesulfonic; proton-exchange membrane; conductivity; cross-linking; temperature 1. Introduction Recently, lots of polymer electrolyte membranes have been prepared from the sulfonation of aromatic polymers such as poly(arylene ether sulfone) [1–4] and modified poly(arylene ether sulfone) [5–7] for the application of electrodialysis and fuel cells as their rigid-rod backbone structures are basically quite stable in thermal and mechanical aspects. -
Computational Redox Potential Predictions: Applications to Inorganic and Organic Aqueous Complexes, and Complexes Adsorbed to Mineral Surfaces
Minerals 2014, 4, 345-387; doi:10.3390/min4020345 OPEN ACCESS minerals ISSN 2075-163X www.mdpi.com/journal/minerals Review Computational Redox Potential Predictions: Applications to Inorganic and Organic Aqueous Complexes, and Complexes Adsorbed to Mineral Surfaces Krishnamoorthy Arumugam and Udo Becker * Department of Earth and Environmental Sciences, University of Michigan, 1100 North University Avenue, 2534 C.C. Little, Ann Arbor, MI 48109-1005, USA; E-Mail: [email protected] * Author to whom correspondence should be addressed; E-Mail: [email protected]; Tel.: +1-734-615-6894; Fax: +1-734-763-4690. Received: 11 February 2014; in revised form: 3 April 2014 / Accepted: 13 April 2014 / Published: 24 April 2014 Abstract: Applications of redox processes range over a number of scientific fields. This review article summarizes the theory behind the calculation of redox potentials in solution for species such as organic compounds, inorganic complexes, actinides, battery materials, and mineral surface-bound-species. Different computational approaches to predict and determine redox potentials of electron transitions are discussed along with their respective pros and cons for the prediction of redox potentials. Subsequently, recommendations are made for certain necessary computational settings required for accurate calculation of redox potentials. This article reviews the importance of computational parameters, such as basis sets, density functional theory (DFT) functionals, and relativistic approaches and the role that physicochemical processes play on the shift of redox potentials, such as hydration or spin orbit coupling, and will aid in finding suitable combinations of approaches for different chemical and geochemical applications. Identifying cost-effective and credible computational approaches is essential to benchmark redox potential calculations against experiments. -
"Relationships Between Oxidation-Reduction Potential
Relationships between Oxidation-Reduction Potential, Oxidant, and pH in Drinking Water Cheryl N. James3, Rachel C. Copeland2, and Darren A. Lytle1 1U.S. Environmental Protection Agency, NRMRL, Cincinnati, OH 2University of Cincinnati, Department of Environmental Engineering, Cincinnati, OH 3University of Cincinnati, Department of Chemical Engineering, Cincinnati, OH Abstract –Oxidation and reduction (redox) reactions are very important in drinking water. Oxidation-reduction potential (ORP) measurements reflect the redox state of water. Redox measurements are not widely made by drinking water utilities in part because they are not well understood. The objective of this study was to determine the effect of oxidant type and concentration on the ORP of carbonate buffered water as a function of pH. Oxidants that were studied included: chlorine, monochloramine, potassium permanganate, chlorine dioxide, and oxygen. ORP decreased with increasing pH, regardless of the oxidant type or concentration. ORP increased rapidly with increasing oxidant dosage, particularly at lower concentrations. Differences in the redox potentials of different oxidant systems were also observed. Waters that contained chlorine and chlorine dioxide had the highest ORPs. Tests also revealed that there were inconsistencies with redox electrode measurements. In the standard Zobell reference solution, two identical redox electrodes had nearly the same reading, but in test waters the readings sometimes showed a variation as great as 217.7 mV. Key words: ORP, redox potential, redox chemistry, oxidant, drinking water 1.0 BACKGROUND 1.1 Redox Theory Oxidation-reduction (redox) reactions describe the transfer of electrons between atoms, molecules, or ions. Oxidation and reduction reactions occur simultaneously and together make up an electrochemical couple. -
Butadiene, Supp. B
.. ..--.- PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California Abstract Process Economics Program Report No. 35B BUTADIENE (April 1982) Most of the world's butadiene is obtained as a coproduct of ethyl- ene, especially by the steam cracking of naphtha or gas oil. When there is not sufficient co-product butadiene available, supplies can be supplemented by material made by the oxidative dehydrogenation of n-butenes. Regardless of the source, the butadiene must be separated from other C4 hydrocarbons (mainly butane and butenes). Rxtractive distillation is the major separation process in current usem This report coataius process descriptions, capital investment esti- mates, and production cost estimates for the Petro-Tex oxidative dehydrogenation process to produce butadiene frox n-butenes and for the three extractive distillation processes that are presently available for licensing in the United States. The extractive distillation pro- cesses are the Nippon Zeon process (dimethylfornisxidesolvent), the BASP process (N-methyl pyrrolidone solvent), and the Union Carbide pro- cess (dixethylacetsxide solvent). All estimates are for a production rate of 50,000 metric toss per year of butadiene. PRP '80 CRR SUPPLEMENT B by GRANT E. RUSSELL April 1982 A private report by the PROCESS ECONOMICS PROGRAM Menlo Park, California 94025 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLD PETROCHEMICALS Program covers major hydrocarbons and their derivatives on a worldwide basis. In addition, the SRI DIRECTORY OF CHEMICAL PRODUCERS services provide detailed lists of chemical producers by company, prod- uct, and plant for the United States and Western Europe. -
Ch.14-16 Electrochemistry Redox Reaction
Redox Reaction - the basics ox + red <=> red + ox Ch.14-16 1 2 1 2 Oxidizing Reducing Electrochemistry Agent Agent Redox reactions: involve transfer of electrons from one species to another. Oxidizing agent (oxidant): takes electrons Reducing agent (reductant): gives electrons Redox Reaction - the basics Balance Redox Reactions (Half Reactions) Reduced Oxidized 1. Write down the (two half) reactions. ox1 + red2 <=> red1 + ox2 2. Balance the (half) reactions (Mass and Charge): a. Start with elements other than H and O. Oxidizing Reducing Agent Agent b. Balance O by adding water. c. balance H by adding H+. Redox reactions: involve transfer of electrons from one d. Balancing charge by adding electrons. species to another. (3. Multiply each half reaction to make the number of Oxidizing agent (oxidant): takes electrons electrons equal. Reducing agent (reductant): gives electrons 4. Add the reactions and simplify.) Fe3+ + V2+ → Fe2+ + V3 + Example: Balance the two half reactions and redox Important Redox Titrants and the Reactions reaction equation of the titration of an acidic solution of Na2C2O4 (sodium oxalate, colorless) with KMnO4 (deep purple). Oxidizing Reagents (Oxidants) - 2- 2+ MnO4 (qa ) + C2O4 (qa ) → Mn (qa ) + CO2(g) (1)Potassium Permanganate +qa -qa 2-qa 16H ( ) + 2MnO4 ( ) + 5C2O4 ( ) → − + − 2+ 2+ MnO 4 +8H +5 e → Mn + 4 H2 O 2Mn (qa ) + 8H2O(l) + 10CO2( g) MnO − +4H+ + 3 e − → MnO( s )+ 2 H O Example: Balance 4 2 2 Sn2+ + Fe3+ <=> Sn4+ + Fe2+ − − 2− MnO4 + e→ MnO4 2+ - 3+ 2+ Fe + MnO4 <=> Fe + Mn 1 Important Redox Titrants -
Dimethylacetamide 2004
DIMETHYLACETAMIDE 2004 CH3CON(CH3)2 MW: 87.12 CAS: 127-19-5 RTECS: AB7700000 METHOD: 2004, Issue 2 EVALUATION: FULL Issue 1: 15 May 1989 Issue 2: 15 August 1994 OSHA : 10 ppm (skin) PROPERTIES: liquid; BP 164.5 - 166 °C; MP •20 °C; NIOSH: 10 ppm (skin) d 0.937 g/mL @ 25 ° C; VP 1.5 mm Hg ACGIH: 10 ppm (skin) @ 20 °C; flash point 70 °C, explosive (1 ppm = 3.56 mg/m 3 @ NTP) range 1.8 to 11.5% SYNONYMS: N,N-dimethylacetamide; acetyldimethylamine; DMAC SAMPLING MEASUREMENT SAMPLER: SOLID SORBENT TUBE TECHNIQUE: GAS CHROMATOGRAPHY, FID (silica gel, 150 mg/75 mg) ANALYTE: dimethylacetamide FLOW RATE: 0.01 to 1 L/min DESORPTION: 1 mL methanol; 1 h in ultrasonic bath VOL-MIN: 15 L @ 30 mg/m 3 -MAX: 80 L INJECTION VOLUME: 5 µL SHIPMENT: routine TEMPERATURE-INJECTION: 240 °C SAMPLE -DETECTOR: 320 °C STABILITY: at least 5 days @ 25 °C [1] -COLUMN: 140 °C BLANKS: 2 to 10 field blanks per set CARRIER GAS: N2, 50 mL/min COLUMNS: 1.5 m x 6-mm OD glass; 10% UCON 50-HB-5100, 2% KOH on 100/120 mesh Chromosorb WHP ACCURACY CALIBRATION: analyte in methanol RANGE STUDIED: 18 to 105 mg/m 3 [1]; (45-L samples) RANGE: 0.5 to 4 mg per sample [1,2] BIAS: • 0.8% ESTIMATED LOD: 0.05 mg per sample [2] ˆ OVERALL PRECISION (S rT): 0.067 [1] PRECISION (S ): 0.032 [1] ACCURACY: ± 11.7% r APPLICABILITY: The working range is 10 to 80 mg/m 3 of dimethylacetamide or dimethyformamdide for a 50-L air sample. -
United States Patent (19) (11) 4,219,498 Doi Et Al
United States Patent (19) (11) 4,219,498 Doi et al. - (45) Aug. 26, 1980 54 PROCESS FOR PREPARING HIGHLY : (56) References Cited PURE-2-ACRYLAMDO-2-METHYLPRO PUBLICATIONS PANESULFONCACID Vogel, "Practical Org. Chem,” 3rd Ed. (1962), pp. 122-125. (75) Inventors: Shunichi Doi; Masatake Kamogawa, both of Yokohama, Japan Primary Examiner-A. Siegel Attorney, Agent, or Firm-Cushman, Darby & Cushman 73) Assignees: Nitto Chemical industry Co., Ltd.; 57 ABSTRACT Mitsubishi Rayon Co., Ltd., both of This disclosure relates to a process for preparing highly Tokyo, Japan pure 2-acylamido-2-methylpropanesulfonic acid, which comprises the steps of adding acetic acid to a slurry 21 Appl. No.: 8,113 containing crystals of 2-acrylamido-2-methylpropane sulfonic acid obtained by the reaction of acrylonitrile, isobutene and either conc. sulfuric acid, fuming sulfuric (22 Filed: Jan. 31, 1979 acid or sulfuric anhydride plus water in a solvent, then distilling the resulting mixture to replace the reaction 30 Foreign Application Priority Data solvent with acetic acid, adding water or hydrous acetic Jun. 12, 1978 JP Japan .................................. 53/69928 acid to the resulting mixture, heating the mixture to dissolve said crystals, and subjecting the solution to 51) Int. Cl’............................................ CO7C 143/02 recrystallization. 52 U.S.C. ................................................ 260/513 N 58 Field of Search .................................... 260/513 N 7 Claims, No Drawings 4,219,498 1. 2 of AMPS used as a starting material. The larger the said PROCESS FOR PREPARNG HIGHLY values, the higher the molecular weight of the copoly PURE-2-ACRYLAMDO-2-METHYLPROPANE mer and the more favorable the effect on papermaking. -
Chemical Redox Agents for Organometallic Chemistry
Chem. Rev. 1996, 96, 877−910 877 Chemical Redox Agents for Organometallic Chemistry Neil G. Connelly*,† and William E. Geiger*,‡ School of Chemistry, University of Bristol, U.K., and Department of Chemistry, University of Vermont, Burlington, Vermont 05405-0125 Received October 3, 1995 (Revised Manuscript Received January 9, 1996) Contents I. Introduction 877 A. Scope of the Review 877 B. Benefits of Redox Agents: Comparison with 878 Electrochemical Methods 1. Advantages of Chemical Redox Agents 878 2. Disadvantages of Chemical Redox Agents 879 C. Potentials in Nonaqueous Solvents 879 D. Reversible vs Irreversible ET Reagents 879 E. Categorization of Reagent Strength 881 II. Oxidants 881 A. Inorganic 881 1. Metal and Metal Complex Oxidants 881 2. Main Group Oxidants 887 B. Organic 891 The authors (Bill Geiger, left; Neil Connelly, right) have been at the forefront of organometallic electrochemistry for more than 20 years and have had 1. Radical Cations 891 a long-standing and fruitful collaboration. 2. Carbocations 893 3. Cyanocarbons and Related Electron-Rich 894 Neil Connelly took his B.Sc. (1966) and Ph.D. (1969, under the direction Compounds of Jon McCleverty) degrees at the University of Sheffield, U.K. Post- 4. Quinones 895 doctoral work at the Universities of Wisconsin (with Lawrence F. Dahl) 5. Other Organic Oxidants 896 and Cambridge (with Brian Johnson and Jack Lewis) was followed by an appointment at the University of Bristol (Lectureship, 1971; D.Sc. degree, III. Reductants 896 1973; Readership 1975). His research interests are centered on synthetic A. Inorganic 896 and structural studies of redox-active organometallic and coordination 1. -
8. AIGA 112/20 Solvents for Acetylene Filling Category
SOLVENTS FOR ACETYLENE FILLING AIGA 112/20 Asia Industrial Gases Association N0 2 Venture Drive, #22-28 Vision Exchange, Singapore 608526 Tel: +65 67055642 Fax: +65 68633379 Internet: http://www.asiaiga.org | LinkedIn Profile: https://www.linkedin.com/company/asiaigaorg AIGA 112/20 SOLVENTS FOR ACETYLENE FILLING Acknowledgement This document is adopted from the European Industrial Gases Association document Doc 225 ‘Solvents for Acetylene Filling’. Acknowledgement and thanks are hereby given to EIGA for permission granted for the use of their document. Disclaimer All publications of AIGA or bearing AIGA’s name contain information, including Codes of Practice, safety procedures and other technical information that were obtained from sources believed by AIGA to be reliable and/ or based on technical information and experience currently available from members of AIGA and others at the date of the publication. As such, we do not make any representation or warranty nor accept any liability as to the accuracy, completeness or correctness of the information contained in these publications. While AIGA recommends that its members refer to or use its publications, such reference to or use thereof by its members or third parties is purely voluntary and not binding. AIGA or its members make no guarantee of the results and assume no liability or responsibility in connection with the reference to or use of information or suggestions contained in AIGA’s publications. AIGA has no control whatsoever as regards, performance or non-performance, misinterpretation, proper or improper use of any information or suggestions contained in AIGA’s publications by any person or entity (including AIGA members) and AIGA expressly disclaims any liability in connection thereto.