Phosphine and Ammonia Photochemistry in Jupiter's
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Ammonia As a Refrigerant
1791 Tullie Circle, NE. Atlanta, Georgia 30329-2305, USA www.ashrae.org ASHRAE Position Document on Ammonia as a Refrigerant Approved by ASHRAE Board of Directors February 1, 2017 Expires February 1, 2020 ASHRAE S H A P I N G T O M O R R O W ’ S B U I L T E N V I R O N M E N T T O D A Y © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. COMMITTEE ROSTER The ASHRAE Position Document on “Ammonia as a Refrigerant” was developed by the Society’s Refrigeration Committee. Position Document Committee formed on January 8, 2016 with Dave Rule as its chair. Dave Rule, Chair Georgi Kazachki IIAR Dayton Phoenix Group Alexandria, VA, USA Dayton, OH, USA Ray Cole Richard Royal Axiom Engineers, Inc. Walmart Monterey, CA, USA Bentonville, Arkansas, USA Dan Dettmers Greg Scrivener IRC, University of Wisconsin Cold Dynamics Madison, WI, USA Meadow Lake, SK, Canada Derek Hamilton Azane Inc. San Francisco, CA, USA Other contributors: M. Kent Anderson Caleb Nelson Consultant Azane, Inc. Bethesda, MD, USA Missoula, MT, USA Cognizant Committees The chairperson of Refrigerant Committee also served as ex-officio members: Karim Amrane REF Committee AHRI Bethesda, MD, USA i © 2017 ASHRAE (www.ashrae.org). For personal use only. Additional reproduction, distribution, or transmission in either print or digital form is not permitted without ASHRAE’s prior written permission. HISTORY of REVISION / REAFFIRMATION / WITHDRAWAL -
Safer Cocktail for an Ethanol/Water/Ammonia Solvent
L A S C P LSC in Practice C P O C L Safer Cocktail for an Ethanol/Water/ K T I A I C Ammonia Solvent Mixture L S A Problem T A laboratory had been under pressure to move towards Using this mixture, the sample uptake capacity of I the newer generation of safer liquid scintillation ULTIMA-Flo AP, ULTIMA-Flo M and ULTIMA Gold O cocktails. Unfortunately, the sample composition of LLT (PerkinElmer 6013599, 6013579 and 6013377, one of their targets kept giving the researchers problems. respectively) at 20 °C was determined and N Before the lead researcher contacted PerkinElmer, the results were: they had tried PerkinElmer’s Opti-Fluor®, ULTIMA ULTIMA-Flo AP 4.00 mL in 10 mL cocktail N Gold LLT, and ULTIMA Gold XR. All of the safer O ™ ULTIMA-Flo M 4.25 mL in 10 mL cocktail cocktails could incorporate each of the constituents T as indicated by their sample capacity graphs. ULTIMA Gold LLT 4.25 mL in 10 mL cocktail E The problematic sample was an extraction solvent From these results, we observed that it was possible consisting of 900 mL ethanol, 50 mL ammonium to get 4.0 mL of the sample into all of these cocktails. hydroxide, 500 mL water and an enzyme containing In addition, we determined that it was not possible to 14C. The mixture had a pH in the range of 10 to 11. get 4 mL sample into 7 mL of any of these cocktails. To complete this work, we also checked for lumines- Discussion cence using 4 mL of sample in 10 mL of each cocktail. -
Improving the Efficiency of Ammonia Electrolysis for Hydrogen Production
Improving The Efficiency Of Ammonia Electrolysis For Hydrogen Production A dissertation presented to the faculty of the Russ College of Engineering and Technology of Ohio University In partial fulfillment of the requirements for the degree Doctor of Philosophy Ramasamy Palaniappan December 2013 © 2013 Ramasamy Palaniappan. All Rights Reserved. 2 This dissertation titled Improving the Efficiency of Ammonia Electrolysis for Hydrogen Production by RAMASAMY PALANIAPPAN has been approved for the Department of Chemical and Biomolecular Engineering and the Russ College of Engineering and Technology by Gerardine G. Botte Professor of Chemical and Biomolecular Engineering Dennis Irwin Dean, Russ College of Engineering and Technology 3 ABSTRACT PALANIAPPAN, RAMASAMY, Ph.D., December 2013, Chemical Engineering Improving the Efficiency of Ammonia Electrolysis for Hydrogen Production Director of Dissertation: Gerardine G. Botte Given the abundance of ammonia in domestic and industrial wastes, ammonia electrolysis is a promising technology for remediation and distributed power generation in a clean and safe manner. Efficiency has been identified as one of the key issues that require improvement in order for the technology to enter the market phase. Therefore, this research was performed with the aim of improving the efficiency of hydrogen production by finding alternative materials for the cathode and electrolyte. 1. In the presence of ammonia the activity for hydrogen evolution reaction (HER) followed the trend Rh>Pt>Ru>Ni. The addition of ammonia resulted in lower rates for HER for Pt, Ru, and Ni, which have been attributed to competition from the ammonia adsorption reaction. 2. The addition of ammonia offers insight into the role of metal-hydrogen underpotential deposition (M-Hupd) on HER kinetics. -
Cellulosic Ethanol Production Via Aqueous Ammonia Soaking Pretreatment and Simultaneous Saccharification and Fermentation Asli Isci Iowa State University
Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 2008 Cellulosic ethanol production via aqueous ammonia soaking pretreatment and simultaneous saccharification and fermentation Asli Isci Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Agriculture Commons, and the Bioresource and Agricultural Engineering Commons Recommended Citation Isci, Asli, "Cellulosic ethanol production via aqueous ammonia soaking pretreatment and simultaneous saccharification and fermentation" (2008). Retrospective Theses and Dissertations. 15695. https://lib.dr.iastate.edu/rtd/15695 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. Cellulosic ethanol production via aqueous ammonia soaking pretreatment and simultaneous saccharification and fermentation by Asli Isci A dissertation submitted to the graduate faculty in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Co-majors: Agricultural and Biosystems Engineering; Biorenewable Resources and Technology Program of Study Committee: Robert P. Anex, Major Professor D. Raj Raman Anthony L. Pometto III. Kenneth J. Moore Robert C. Brown Iowa State University Ames, Iowa -
Algorithmic Analysis of Chemical Dynamics of the Autoignition of NH3–H2O2/Air Mixtures
energies Article Algorithmic Analysis of Chemical Dynamics of the Autoignition of NH3–H2O2/Air Mixtures Ahmed T. Khalil 1,2, Dimitris M. Manias 3, Efstathios-Al. Tingas 4, Dimitrios C. Kyritsis 1,2,* and Dimitris A. Goussis 1,2 1 Department of Mechanical Engineering, Khalifa University of Science and Technology, Abu Dhabi 127788, UAE; [email protected] (A.T.K.); [email protected] (D.A.G.) 2 Research and Innovation Center on CO2 and H2 (RICH), Khalifa University of Science and Technology, P.O. Box 127788, Abu Dhabi, UAE 3 Department of Mechanics, School of Applied Mathematics and Physical Sciences, National Technical University of Athens, 157 73 Athens, Greece; [email protected] 4 Perth College, University of the Highlands and Islands, (UHI), Perth PH1 2NX, UK; [email protected] * Correspondence: [email protected] Received: 8 September 2019; Accepted: 7 October 2019; Published: 21 November 2019 Abstract: The dynamics of a homogeneous adiabatic autoignition of an ammonia/air mixture at constant volume was studied, using the algorithmic tools of Computational Singular Perturbation. Since ammonia combustion is characterized by both unrealistically long ignition delays and elevated NOx emissions, the time frame of action of the modes that are responsible for ignition was analyzed by calculating the developing time scales throughout the process and by studying their possible relation to NOx emissions. The reactions that support or oppose the explosive time scale were identified, along with the variables that are related the most to the dynamics that drive the system to an explosion. -
BENZENE Disclaimer
United States Office of Air Quality EPA-454/R-98-011 Environmental Protection Planning And Standards June 1998 Agency Research Triangle Park, NC 27711 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF BENZENE Disclaimer This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and has been approved for publication. Mention of trade names and commercial products does not constitute endorsement or recommendation of use. EPA-454/R-98-011 ii TABLE OF CONTENTS Section Page LIST OF TABLES.....................................................x LIST OF FIGURES.................................................. xvi EXECUTIVE SUMMARY.............................................xx 1.0 PURPOSE OF DOCUMENT .......................................... 1-1 2.0 OVERVIEW OF DOCUMENT CONTENTS.............................. 2-1 3.0 BACKGROUND INFORMATION ...................................... 3-1 3.1 NATURE OF POLLUTANT..................................... 3-1 3.2 OVERVIEW OF PRODUCTION AND USE ......................... 3-4 3.3 OVERVIEW OF EMISSIONS.................................... 3-8 4.0 EMISSIONS FROM BENZENE PRODUCTION ........................... 4-1 4.1 CATALYTIC REFORMING/SEPARATION PROCESS................ 4-7 4.1.1 Process Description for Catalytic Reforming/Separation........... 4-7 4.1.2 Benzene Emissions from Catalytic Reforming/Separation .......... 4-9 4.2 TOLUENE DEALKYLATION AND TOLUENE DISPROPORTIONATION PROCESS ............................ 4-11 4.2.1 Toluene Dealkylation -
Phosphine Safety Data Sheet (180KB)
Phosphine Safety Data Sheet P-4643 This SDS conforms to U.S. Code of Federal Regulations 29 CFR 1910.1200, Hazard Communication. Date of issue: 01/01/1980 Revision date: 08/31/2018 Supersedes: 10/24/2016 SECTION: 1. Product and company identification 1.1. Product identifier Product form : Substance Substance name : Phosphine CAS-No. : 7803-51-2 Formula : PH3 Other means of identification : Hydrogen phosphide, Phosphorous hydride, Phosphorous trihydride, Phosphorated hydrogen 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the substance/mixture : Industrial use; Use as directed. 1.3. Details of the supplier of the safety data sheet Praxair, Inc. 10 Riverview Drive Danbury, CT 06810-6268 - USA T 1-800-772-9247 (1-800-PRAXAIR) - F 1-716-879-2146 www.praxair.com 1.4. Emergency telephone number Emergency number : Onsite Emergency: 1-800-645-4633 CHEMTREC, 24hr/day 7days/week — Within USA: 1-800-424-9300, Outside USA: 001-703-527-3887 (collect calls accepted, Contract 17729) SECTION 2: Hazard identification 2.1. Classification of the substance or mixture GHS-US classification Pyr. Gas H250 Flam. Gas 1 H220 Press. Gas (Liq.) H280 Acute Tox. 1 (Inhalation:gas) H330 Skin Corr. 1B H314 Eye Dam. 1 H318 Aquatic Acute 1 H400 2.2. Label elements GHS-US labeling Hazard pictograms (GHS-US) : GHS02 GHS04 GHS05 GHS06 GHS09 Signal word (GHS-US) : Danger Hazard statements (GHS-US) : H220 - EXTREMELY FLAMMABLE GAS H250 - CATCHES FIRE SPONTANEOUSLY IF EXPOSED TO AIR H280 - CONTAINS GAS UNDER PRESSURE; MAY EXPLODE IF HEATED H314 - Causes severe skin burns and eye damage H330 - FATAL IF INHALED H400 - VERY TOXIC TO AQUATIC LIFE CGA-HG04 - MAY FORM EXPLOSIVE MIXTURES WITH AIR CGA-HG11 - SYMPTOMS MAY BE DELAYED Precautionary statements (GHS-US) : P202 - Do not handle until all safety precautions have been read and understood. -
NATURE [APRIL 9, 1932 Having for Comparison a Standard Benzene Bulb
546 NATURE [APRIL 9, 1932 having for comparison a standard benzene bulb. filter transmitting 250-280 p.p. was used in these ex The powder was then melted, and recrystallised by periments. The effect was shown to have its origin heating the bulb in an electric heater to about 270° C. in the phosphine molecule, but in view of the fact and very slowly cooling it. After noting the defl.exion that phosphine itself does not absorb in the region due to the bulb with the resolidified bismuth, that of 250-280 p.p., it would seem that the incidental presence the container alone was determined by breaking it of mercury vapour resulted in the phosphine being open and dissolving out the metal with nitric acid. decomposed by excited mercury atoms into hydrogen Experiments with similar bulbs and bismuth regulus atoms and probably PH or PH2 radicals, which pro showed no change of defl.exion after heat treatment. duce the Hinshelwood-Clusius effect. Hinshelwood But when bismuth powder was melted and recrystal and Clusius concluded that the active material was lised, the diamagnetic susceptibility rose nearly to the present in the gas phase, but on repeating their ex regulus value. Many samples of colloidal bismuth periment by exposing the mixture in one tube and gave similar results. determining the explosion pressure immediately after These observations indicate that the fall in the in another similar tube, the effect was not observed. susceptibility value with reduction of particle size in That is, the effect is most probably a wall phenomenon, the case of bismuth is a genuine effect. -
Gas-Phase Reactions of Si+ with Ammonia and The
2396 J. Am. Chem. SOC.1988, 110, 2396-2399 Gas-Phase Reactions of Si+ with Ammonia and the Amines ( CH3)xNH3-x(x = 1-3): Possible Ion-Molecule Reaction Pathways toward SiH, SiCH, SiNH, SiCH3, SiNCH3, and H2SiNH S. Wlodek and D. K. Bohme* Contribution from the Department of Chemistry and Centre for Research in Experimental Space Science, York University, Downsview, Ontario, Canada M3J 1P3. Received August 31, 1987 Abstract: Rate constants and product distributions have been determined for gas-phase reactions of ground-state Si'(2P) ions with ammonia and the amines (CH,),NH3-, (x = 1-3) at 296 f 2 K with the selected-ion flow tube technique. All reactions were observed to be fast and can be understood in terms of Si' insertion into N-H and C-N bonds to form ions of the type SiNRIR2' (Rl, R2 = H, CHJ proceeding in competition (in the case of the amines) with hydride ion transfer to form immonium ions of the type CH2NRIR2' (Rl, R2 = H, CH,). C-N bond insertion appears more efficient than N-H bond insertion. The contribution of hydride ion transfer increases with increasing stability of the immonium ion. The latter reaction leads directly to SiH as a neutral product. Other minor reaction channels were seen which lead directly or indirectly to SiCH and SiCH3. Rapid secondary proton transfer reactions were observed for SiNH2' and SiNHCH3+to produce gas-phase SiNH and SiNCH3 molecules. With methylamine SiNH2+also appears to produce H2SiNH2' which may deprotonate to form the simplest silanimine, H2SiNH, or aminosilylene, HSiNH,. -
Ammonia/Ethanol Mixture for Adsorption Refrigeration
energies Article Ammonia/Ethanol Mixture for Adsorption Refrigeration Mauro Luberti, Chiara Di Santis and Giulio Santori * School of Engineering, Institute for Materials and Processes, the University of Edinburgh, Sanderson Building, King0s Buildings, Robert Stevenson Road, Edinburgh EH9 3FB, UK; [email protected] (M.L.); [email protected] (C.D.S.) * Correspondence: [email protected] Received: 29 January 2020; Accepted: 19 February 2020; Published: 22 February 2020 Abstract: Adsorption refrigeration has become an attractive technology due to the capability to exploit low-grade thermal energy for cooling power generation and the use of environmentally friendly refrigerants. Traditionally, these systems work with pure fluids such as water, ethanol, methanol, and ammonia. Nevertheless, the operating conditions make their commercialization still unfeasible, especially owing to safety and cost issues as a consequence of the working pressures, which are higher or lower than 1 atm. The present work represents the first thermodynamic insight in the use of mixtures for adsorption refrigeration and aims to assess the performance of a binary system of ammonia and ethanol. According to the Gibbs’ phase rule, the addition of a component introduces an additional degree of freedom, which allows to adjust the pressure of the system varying the composition of the mixture. The refrigeration process was simulated with isothermal- isochoric flash calculations to solve the phase equilibria, described by the Peng-Robinson-Stryjek-Vera (PRSV) equation of state for the vapor and liquid phases and by the ideal adsorbed solution theory (IAST) and the multicomponent potential theory of adsorption (MPTA) for the adsorbed phase. -
US3681281.Pdf
3,681,281 United States Patent Office Patented Aug. 1, 1972 2 phosphine oxide, poly-vinyl-di-phenyl phosphine oxide, 3,681,281 tribenzyl phosphine oxide, tris-hydroxyethyl phosphine FLAME-RETARDANT POLYESTERS oxide, di-hydroxyethyl phenyl phosphine oxide, tris Charles V. Juelke, Morristown, and Louis E. Trapasso, carboxyethyl phosphine oxide, and the like. Westfield, N.J., assignors to Celanese Corporation, New The amount of additive included in the polymer depends York, N.Y. on the level of flame retardance desired in a particular No Drawing. Filed July 10, 1970, Ser. No. 54,010 application of a polyester fiber or film forming mass. Int. C. C09k 3/28; D06p3/54 About 10 weight percent or more of the additives will U.S. C. 260-45.8 N 11. Claims impart self-extinguishing properties to the polyester mass. When the additive level is lowered to below about 5 O weight percent the polyester mass is no longer self ABSTRACT OF THE DISCLOSURE extinguishing but still resists burning better than such Fibers and other shaped structures of polyesters such masses without the additive. At a level of about 1 weight as polyethylene terephthalate are rendered flame-retardant percent, while flammability is reduced, it is not sufficiently by the incorporation of tertiary phosphine oxides such 15 flame retardant for most purposes. Larger amounts than as triphenyl phosphine oxide or ethylene bis-di-phenyl those indicated serve no purpose. phosphine oxide optionally along with a synergist such In accordance with a further aspect of the invention as benzil, dibenzyl or triphenylmelamine. there may also be incorporated along with the phosphine oxide a flame retardant synergistic additive. -
Environmental Health & Safety
Environmental Health & Safety Chemical Safety Program Chemical Segregation & Incompatibilities Guidelines Class of Recommended Incompatible Possible Reaction Examples Chemical Storage Method Materials If Mixed Corrosive Acids Mineral Acids – Separate cabinet or storage area Flammable Liquids Heat Chromic Acid away from potential water Flammable Solids Hydrogen Chloride sources, i.e. under sink Bases Hydrochloric Acid Oxidizers Gas Generation Nitric Acid Poisons Perchloric Acid Violent Phosphoric Acid Reaction Sulfuric Acid Corrosive Bases/ Ammonium Hydroxide Separate cabinet or storage area Flammable Liquids Heat Caustics Sodium Hydroxide away from potential water Flammable Solids Sodium Bicarbonate sources, i.e. under sink Acids Gas Generation Oxidizers Poisons Violent Reaction Explosives Ammonium Nitrate Secure location away from Flammable Liquids Nitro Urea other chemicals Oxidizers Picric Acid Poisons Explosion Hazard Trinitroaniline Acids Trinitrobenzene Bases Trinitrobenzoic Acid Trinitrotoluene Urea Nitrate Flammable Liquids Acetone Grounded flammable storage Acids Fire Hazard Benzene cabinet of flammable storage Bases Diethyl Ether refrigerator Oxidizers Methanol Poisons Heat Ethanol Toluene Violent Glacial Acetic Acid Reaction Flammable Solids Phosphorus Separate dry cool area Acids Fire Hazard Magnesium Bases Heat Oxidizers Violent Poisons Reaction Sodium Hypochlorite Spill tray that is separate from Reducing Agents Fire Oxidizers Benzoyl Peroxide flammable and combustible Flammables Hazard Potassium Permanganate materials Combustibles