Title Synthetic Studies on Perfluorinated Compounds
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A Review on the Effect of Proton Exchange Membranes in Microbial Fuel Cells
Biofuel Research Journal 1 (2014) 7-15 Review A review on the effect of proton exchange membranes in microbial fuel cells Mostafa Rahimnejad *1, Gholamreza Bakeri1, Ghasem Najafpour1, Mostafa Ghasemi2, Sang-Eun Oh3 1Biotechnology Research Lab., Faculty of Chemical Engineering, Babol University of Technology, Babol, Iran 2Fuel Cell Institute, Universiti Kebangsaan Malaysia, 43600 UKM Bangi, Selangor Darul Ehsan, Malaysia 3Department of Biological Environment, Kangwon National University, Chuncheon, Kangwon-do, Republic of Korea HIGHLIGHTS MFC is a novel knowledge that can be used to obtain bioenergy in the form bioelectricity. Transfer of produced electrons to anode is one of the main parts in MFCs. Some MFCs needs artificial electron shuttle in their anaerobic anode compartment. The important goal of MFCs is to reach a suitable power for application in small electrical devices. ARTICLE INFO ABSTRACT Article history: Microorganisms in microbial fuel cells (MFC) liberate electrons while the electron donors are consumed. In the anaerobic Received 3 December 2013 anode compartment, substrates such as carbohydrates are utilized and as a result bioelectricity is produced in the MFC. MFCs Received in revised form 5 January 2014 may be utilized as electricity generators in small devices such as biosensors. MFCs still face practical barriers such as low Accepted 6 January 2014 generated power and current density. Recently, a great deal of attention has been given to MFCs due to their ability to operate Available online 17 February 2014 at mild conditions and using different biodegradable substrates as fuel. The MFC consists of anode and cathode compartments. Active microorganisms are actively catabolized to carbon sources, therefore generating bioelectricity. -
1,1,1,2-Tetrafluoroethane
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 Organisation, or the World Health Organization. Concise International Chemical Assessment Document 11 1,1,1,2-Tetrafluoroethane First draft prepared by Mrs P. Barker and Mr R. Cary, Health and Safety Executive, Liverpool, United Kingdom, and Dr S. Dobson, Institute of Terrestrial Ecology, Huntingdon, United Kingdom Please not that the layout and pagination of this pdf file are not identical to the printed CICAD Published under the joint sponsorship of the United Nations Environment Programme, the International Labour Organisation, 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, 1998 The International Programme on Chemical Safety (IPCS), established in 1980, is a joint venture of the United Nations Environment Programme (UNEP), the International Labour Organisation (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 -
Chlorofluorocarbons Chem 300A Tyler Jensen, Mackenzie Latimer, Jessie Luther, Jake Mcghee, Adeeb Noorani, Tyla Penner, & Maddy Springle
Chlorofluorocarbons Chem 300a Tyler Jensen, Mackenzie Latimer, Jessie Luther, Jake McGhee, Adeeb Noorani, Tyla Penner, & Maddy Springle 1.1: A Brief History of Chlorofluorocarbons Chlorofluorocarbons (CFCs), also known as Freons, were first synthesized in 1928 by Thomas Midgley Jr, who was working for General Motors trying to find a safe refrigerant to use in commercial applications. (Rosenbaum, n.d.). They are an anthropogenic compound containing fluorine, carbon, and chlorine atoms, and are classified as halocarbons. CFCs are a family of chemicals based upon hydrocarbon skeletons, where most hydrogens have been replaced with chlorine and/or fluorine atoms. They are chemically stable freons that are non-flammable, tasteless and odourless. CFCs are very volatile, which makes for ideal refrigerant gases, having a boiling point close to zero degrees (Rosenbaum, n.d) They were originally created to replace the toxic gases used in the late 1800’s and early 1900’s. Examples of the toxic gases replaced by CFCs as refrigerants are ammonia (NH3), methyl chloride (CH3Cl), and sulfur dioxide (SO2) (Wilkins, 1999). When first created dichlorodifloromethane was found to be less toxic than carbon dioxide, and as non-flammable as carbon tetrachloride (Midgley & Henne, 1930). The non-toxic, non-flammable, and non-reactive properties of CFCs made them ideal for use as refrigerants. CFCs were used in many developed countries for consumption and production as they were inflammable and non-toxic towards humanity. Chlorofluorocarbons can be used as refrigerants, cleaning agents, foaming agents, and propellants for aerosol sprays (Welch, n.d.). In 1974, Two University of California chemists, Professor F. Sherwood Rowland and Dr. -
Advances in PNNL's Mixed Acid Redox Flow Battery Stack
Advances in PNNL’s Mixed Acid Redox Flow Battery Stack David Reed, Ed Thomsen, Wei Wang, Zimin Nie, Bin Li, Brian Koeppel, Kurt Recknagle, and Vincent Sprenkle. Pacific Northwest National Laboratory Electrochemical Materials and Systems DOE Office of Electricity Energy Storage Program – Imre Gyuk Program Manager. OE Energy Storage Systems Program Review September 16-19th, 2014 Topics FY 14 Objectives and Goals Background Nafion membrane thickness development. Low cost interdigitated flow design 4 KW stack Conclusion and Future Work FY14 Redox Objectives and Goal Operate at 240 mA/cm2 with improved stack energy efficiency and lower stack pressure drop. Greater stack efficiency Use of 212/211 membrane versus 115. Greater system efficiency Use of interdigitated flow field Understand influence of temperature on stack efficiency Vanadium Mixed Acid Electrolyte 70% increase in capacity 2+ - Charge + Catholyte: VO + Cl + H2O – e Discharge VO2Cl + 2H εco=1.0 V . V2+, V3+, V4+, V5+ stable >2.8M, Anolyte: V3+ + e V2+ ε =-0.25 ao in SO2- and Cl- mixed solutions 2+ - 3+ + 2+ Overall: VO + Cl + H O + V VO Cl + 2H + V Eo=1.25 V 2 2 Power and Energy are separate enabling 80% increase in operating greater flexibility and safety. temperature window. Suitable for wide range of applications 10’s MW to ~ 5 kw . -5 – 50°C Wide range of chemistries available. Low energy density ~ 30 Whr/kg Redox Flow Battery Objectives Develop the technologies, tools, and system understanding required to move the mixed acid electrolyte chemistry from basic chemistry -
CHAPTER12 Atmospheric Degradation of Halocarbon Substitutes
CHAPTER12 AtmosphericDegradation of Halocarbon Substitutes Lead Author: R.A. Cox Co-authors: R. Atkinson G.K. Moortgat A.R. Ravishankara H.W. Sidebottom Contributors: G.D. Hayman C. Howard M. Kanakidou S .A. Penkett J. Rodriguez S. Solomon 0. Wild CHAPTER 12 ATMOSPHERIC DEGRADATION OF HALOCARBON SUBSTITUTES Contents SCIENTIFIC SUMMARY ......................................................................................................................................... 12.1 12.1 BACKGROUND ............................................................................................................................................... 12.3 12.2 ATMOSPHERIC LIFETIMES OF HFCS AND HCFCS ................................................................................. 12.3 12.2. 1 Tropospheric Loss Processes .............................................................................................................. 12.3 12.2.2 Stratospheric Loss Processes .............................................................................................................. 12.4 12.3 ATMOSPHERIC LIFETIMES OF OTHER CFC AND HALON SUBSTITUTES ......................................... 12.4 12.4 ATMOSPHERIC DEGRADATION OF SUBSTITUTES ................................................................................ 12.5 12.5 GAS PHASE DEGRADATION CHEMISTRY OF SUBSTITUTES .............................................................. 12.6 12.5.1 Reaction with NO .............................................................................................................................. -
Subpart L – Fluorinated Gas Production
Mandatory Greenhouse Gas Reporting Rule: EPA's Response to Public Comments Subpart L – Fluorinated Gas Production Subpart L – Fluorinated Gas Production U.S. Environmental Protection Agency Office of Atmospheric Programs Climate Change Division Washington, D.C. FOREWORD This document provides responses to public comments on the U.S. Environmental Protection Agency’s (EPA’s) Proposed Mandatory Greenhouse Gas Reporting Rule: Additional Sources of Fluorinated GHGs: Subpart L, Fluorinated Gas Production. EPA published a Notice of Proposed Rulemaking in the Federal Register (FR) on April 12, 2010 (75 FR 18652). EPA received comments on this proposed rule via mail, e-mail, and at a public hearing held in Washington D.C. on April 20, 2010. Copies of all comments submitted are available at the EPA Docket Center Public Reading Room. Comments letters and transcripts of the public hearings are also available electronically through http://www.regulations.gov by searching Docket ID EPA-HQ-OAR-2009-0927. EPA prepared this document in multiple sections, with each section focusing on a different broad category of comments on the rule. EPA’s responses to comments are generally provided immediately following each comment. In some cases, EPA provided responses to specific comments or groups of similar comments in the preamble to the final rulemaking. Rather than repeating those responses in this document, EPA has referenced the preamble. Comments were assigned to specific section of this document based on an assessment of the principal subject of the comment; however, some comments inevitably overlap multiple subject areas. For this reason, EPA encourages the public to read the other sections of this document relevant to their interests. -
Alkali Metal Ion-Proton Exchange Equilibria and Water Sorption
2 Abstract Alkali metal ion - H +exchanges on Nafion 117 membrane treated differently, Dowex 50 W x 4 and Dowex 50 W x 8 resins have been studied at a total ionic strength of 0.1 mol dm-3. The water sorption isotherms of these exchangers in different ionic forms generated over the entire range of water activity, have been analysed by the D’Arcy and Watt equation (DWE). Water sorption studies have shown that the physical structure of the exchangers have changed due to long - storage or aging, resulting in poorer water sorption and even formation of pores in the case of Dowex 50 W x 8 resin. As a result, the counter ions in the exchangers are not hydrated and the water is present in a free form, albeit structured, in the resin phase. The selectivity sequence for the alkali metal ions with reference to the H + (Li+<Na+<K+) for the exchangers used in the present study is in accordance with that reported in the literature for the ionomers having sulphonic acid as the functional group. In view of the absence of hydration of the cations in the resin phase, the driving force for the selectivity of the cation, namely, the net gain in entropy, is expected to come from the loss of structured water during the exchange process. Pre treating the Nafion 117 membrane with boiling acid solution activates the clustered region of the membrane in the H + form, while pretreatment with boiling water expands the non-ionic domain (the region connecting the clusters). These modifications influence the state of water present in the Nafion 117 membrane and the ion exchange equilibria. -
"Fluorine Compounds, Organic," In: Ullmann's Encyclopedia Of
Article No : a11_349 Fluorine Compounds, Organic GU¨ NTER SIEGEMUND, Hoechst Aktiengesellschaft, Frankfurt, Federal Republic of Germany WERNER SCHWERTFEGER, Hoechst Aktiengesellschaft, Frankfurt, Federal Republic of Germany ANDREW FEIRING, E. I. DuPont de Nemours & Co., Wilmington, Delaware, United States BRUCE SMART, E. I. DuPont de Nemours & Co., Wilmington, Delaware, United States FRED BEHR, Minnesota Mining and Manufacturing Company, St. Paul, Minnesota, United States HERWARD VOGEL, Minnesota Mining and Manufacturing Company, St. Paul, Minnesota, United States BLAINE MCKUSICK, E. I. DuPont de Nemours & Co., Wilmington, Delaware, United States 1. Introduction....................... 444 8. Fluorinated Carboxylic Acids and 2. Production Processes ................ 445 Fluorinated Alkanesulfonic Acids ...... 470 2.1. Substitution of Hydrogen............. 445 8.1. Fluorinated Carboxylic Acids ......... 470 2.2. Halogen – Fluorine Exchange ......... 446 8.1.1. Fluorinated Acetic Acids .............. 470 2.3. Synthesis from Fluorinated Synthons ... 447 8.1.2. Long-Chain Perfluorocarboxylic Acids .... 470 2.4. Addition of Hydrogen Fluoride to 8.1.3. Fluorinated Dicarboxylic Acids ......... 472 Unsaturated Bonds ................. 447 8.1.4. Tetrafluoroethylene – Perfluorovinyl Ether 2.5. Miscellaneous Methods .............. 447 Copolymers with Carboxylic Acid Groups . 472 2.6. Purification and Analysis ............. 447 8.2. Fluorinated Alkanesulfonic Acids ...... 472 3. Fluorinated Alkanes................. 448 8.2.1. Perfluoroalkanesulfonic Acids -
Thermodynamic Equilibrium Constants of Alkali Metal Ion-Hydrogen Ion
Indian Journal of Chemistry Vol. 31A,June 1992, pp. 317-322 Thermodynamic equilibrium constants of alkali metal ion-hydrogen ion exchanges and related swelling free energies in perfluorosulphonate ionomer membrane (Nafion-117) in aqueous medium Sita T Iyer, Deoki Nandan & R M Iyer" Chemistry Division, Bhabha Atomic Research Centre, Trombav. Bombay 400 085 Li + IH + , Na + IH t , K + IH + , Rb + IH + and Cs + IH + exchange equilibria on a perfluorosulphonate ex- changer (Nafion-1l7) have been investigated at 0.1 M ionic strength in aqueous medium and thermody- namic equilibrium constants of 0.78 to 12.6 (Li + IH t to Cs + IH + ) have been evaluated and the alkali me- tal selectivity sequence has been found to be Cs + > Rh + > K + > Na + > Li ". The various ionic forms of Nafion-1l7 involved have also been subjected to isopiestic water vapour sorption investigations and the hydration numbers and swelling free energies determined. The exchange selectivities have been found to be consistent with the sequence of ionic hydration and swelling free energies, the exchange free energies showing a linear relationship with the difference in free energies of hydration of the exchanging ions as per Eisenman's model. The expanded selectivity as well as swelling free energy ranges observed in Nafion- 117 compared to Dowex SOW type of resins have been interpreted in terms of hydrative and osmotic swelling behaviours of the two exchangers. Existence of a solvent shared ion pair in Nafion-1l7. i.e. - SO; (H20)Cs + observed in an earlier study has been supported -
D520CS/521CS, D2020CS/2021CS Ion Exchange Materials Polymer Dispersions
Product Bulletin P-14 D520CS/521CS, D2020CS/2021CS Ion Exchange Materials Polymer Dispersions Product Information Nafion™ perfluorosulfonic acid (PFSA) polymer and dispersant compositions. Typical uses include dispersions are made from chemically stabilized PFSA/ fabrication of thin films, coating formulations for fuel cell polytetrafluoroethylene (PTFE) copolymer in the acid membranes, catalyst coatings, sensors, and a variety of (H+) form and are available in several polymer content electrochemical applications. Typical Composition Nafion™ PFSA Polymer Dispersions by Composition Property D520CS D521CS D2020CS D2021CS 5.0 min. 5.0 min. 20.0 min. 20.0 min. Polymer Content, wt% 5.4 max. 5.4 max. 22.0 max. 22.0 max. Water Content, wt% 45 ± 3 45 ± 3 34 ± 2 34 ± 2 VOC Content, wt% 50 ± 3 50 ± 3 46 ± 2 46 ± 2 1-Propanol 48 ± 3 48 ± 3 44 ± 2 44 ± 2 Ethanol <4 <4 <2 <2 Mixed Ethers and Other VOCs <1 <1 <1 <1 Specific Gravity 0.92−0.94 0.92−0.94 1.01−1.03 1.01−1.03 Available Acid Capacity, meq/g, >1.00 >0.92 >1.00 >0.92 H+ polymer basis Total Acid Capacity, meq/g, 1.03−1.12 0.95−1.03 1.03−1.12 0.95−1.03 H+ polymer basis Viscosity, cP, at 25 °C (77 °F) and 10−40 10−40 50−500 50−500 40 sec–1 Shear Rate* *1 cP = 1 MPa·sec Nafion™ Ion Exchange Materials Order Information Handling Practices Dispersions are available in the following containers Ventilation should be provided for safe handling and (4-L minimum order): processing of Nafion™ dispersion. -
Pfass and Alternatives in Food Packaging (Paper and Paperboard): Report on the Commercial Availability and Current Uses
PFASs and alternatives in food packaging (paper and paperboard): Report on the commercial availability and current uses Series on Risk Management No. 58 1 Series on Risk Management 0 No. 58 PFASs and Alternatives in Food Packaging (Paper and Paperboard) Report on the Commercial Availability and Current Uses PUBE Please cite this publication as: OECD (2020), PFASs and Alternatives in Food Packaging (Paper and Paperboard) Report on the Commercial Availability and Current Uses, OECD Series on Risk Management, No. 58, Environment, Health and Safety, Environment Directorate, OECD. Acknowledgements: The OECD would like to acknowledge the drafting of a consultancy report by Steve Hollins of Exponent International Ltd. upon which this report is based. It was prepared under the framework of the OECD/UNEP Global PFC Group and included the contribution of information by several organisations (see Annex A). The report is published under the responsibility of the OECD Joint Meeting of the Chemicals Committee and the Working Party on Chemicals, Pesticides and Biotechnology. © Photo credits: Cover: Yuriy Golub/Shutterstock.com © OECD 2020 Applications for permission to reproduce or translate all or part of this material should be made to: Head of Publications Service, [email protected], OECD, 2 rue André-Pascal, 75775 Paris Cedex 16, France ABOUT THE OECD 3 About the OECD The Organisation for Economic Co-operation and Development (OECD) is an intergovernmental organisation in which representatives of 36 industrialised countries in North and South America, Europe and the Asia and Pacific region, as well as the European Commission, meet to co-ordinate and harmonise policies, discuss issues of mutual concern, and work together to respond to international problems. -
The Need for Fast Near-Term Climate Mitigation to Slow Feedbacks and Tipping Points
The Need for Fast Near-Term Climate Mitigation to Slow Feedbacks and Tipping Points Critical Role of Short-lived Super Climate Pollutants in the Climate Emergency Background Note DRAFT: 27 September 2021 Institute for Governance Center for Human Rights and & Sustainable Development (IGSD) Environment (CHRE/CEDHA) Lead authors Durwood Zaelke, Romina Picolotti, Kristin Campbell, & Gabrielle Dreyfus Contributing authors Trina Thorbjornsen, Laura Bloomer, Blake Hite, Kiran Ghosh, & Daniel Taillant Acknowledgements We thank readers for comments that have allowed us to continue to update and improve this note. About the Institute for Governance & About the Center for Human Rights and Sustainable Development (IGSD) Environment (CHRE/CEDHA) IGSD’s mission is to promote just and Originally founded in 1999 in Argentina, the sustainable societies and to protect the Center for Human Rights and Environment environment by advancing the understanding, (CHRE or CEDHA by its Spanish acronym) development, and implementation of effective aims to build a more harmonious relationship and accountable systems of governance for between the environment and people. Its work sustainable development. centers on promoting greater access to justice and to guarantee human rights for victims of As part of its work, IGSD is pursuing “fast- environmental degradation, or due to the non- action” climate mitigation strategies that will sustainable management of natural resources, result in significant reductions of climate and to prevent future violations. To this end, emissions to limit temperature increase and other CHRE fosters the creation of public policy that climate impacts in the near-term. The focus is on promotes inclusive socially and environmentally strategies to reduce non-CO2 climate pollutants, sustainable development, through community protect sinks, and enhance urban albedo with participation, public interest litigation, smart surfaces, as a complement to cuts in CO2.