Hydrogen Fluoride Dangers and Alternatives
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Review of Market for Octane Enhancers
May 2000 • NREL/SR-580-28193 Review of Market for Octane Enhancers Final Report J.E. Sinor Consultants, Inc. Niwot, Colorado National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401-3393 NREL is a U.S. Department of Energy Laboratory Operated by Midwest Research Institute • Battelle • Bechtel Contract No. DE-AC36-99-GO10337 May 2000 • NREL/SR-580-28193 Review of Market for Octane Enhancers Final Report J.E. Sinor Consultants, Inc. Niwot, Colorado NREL Technical Monitor: K. Ibsen Prepared under Subcontract No. TXE-0-29113-01 National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401-3393 NREL is a U.S. Department of Energy Laboratory Operated by Midwest Research Institute • Battelle • Bechtel Contract No. DE-AC36-99-GO10337 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or any agency thereof. Available electronically at http://www.doe.gov/bridge Available for a processing fee to U.S. -
Vibrationally Excited Hydrogen Halides : a Bibliography On
VI NBS SPECIAL PUBLICATION 392 J U.S. DEPARTMENT OF COMMERCE / National Bureau of Standards National Bureau of Standards Bldg. Library, _ E-01 Admin. OCT 1 1981 191023 / oO Vibrationally Excited Hydrogen Halides: A Bibliography on Chemical Kinetics of Chemiexcitation and Energy Transfer Processes (1958 through 1973) QC 100 • 1X57 no. 2te c l !14 c '- — | NATIONAL BUREAU OF STANDARDS The National Bureau of Standards' was established by an act of Congress March 3, 1901. The Bureau's overall goal is to strengthen and advance the Nation's science and technology and facilitate their effective application for public benefit. To this end, the Bureau conducts research and provides: (1) a basis for the Nation's physical measurement system, (2) scientific and technological services for industry and government, (3) a technical basis for equity in trade, and (4) technical services to promote public safety. The Bureau consists of the Institute for Basic Standards, the Institute for Materials Research, the Institute for Applied Technology, the Institute for Computer Sciences and Technology, and the Office for Information Programs. THE INSTITUTE FOR BASIC STANDARDS provides the central basis within the United States of a complete and consistent system of physical measurement; coordinates that system with measurement systems of other nations; and furnishes essential services leading to accurate and uniform physical measurements throughout the Nation's scientific community, industry, and commerce. The Institute consists of a Center for Radiation Research, an Office of Meas- urement Services and the following divisions: Applied Mathematics — Electricity — Mechanics — Heat — Optical Physics — Nuclear Sciences" — Applied Radiation 2 — Quantum Electronics 1 — Electromagnetics 3 — Time 3 1 1 and Frequency — Laboratory Astrophysics — Cryogenics . -
APPENDIX M SUMMARY of MAJOR TYPES of Carfg2 REFINERY
APPENDIX M SUMMARY OF MAJOR TYPES OF CaRFG2 REFINERY MODIFICATIONS Appendix M: Summan/ of Major Types of CaRFG2 Refinery Modifications: Alkylation Units A process unit that combines small-molecule hydrocarbon gases produced in the FCCU with a branched chain hydrocarbon called isobutane, producing a material called alkylate, which is blended into gasoline to raise the octane rating. Alkylate is a high octane, low vapor pressure gasoline blending component that essentially contains no olefins, aromatics, or sulfur. This plant improves the ultimate gasoline-making ability of the FCC plant. Therefore, many California refineries built new or modified existing units to increase alkylate production to blend and to produce greater amounts of CaRFG2. Alkylate is produced by combining C3, C4, and C5 components with isobutane (nC4). The process of alkylation is the reverse of cracking. Olefins (such as butenes and propenes) and isobutane are used as feedstocks and combined to produce alkylate. This process enables refiners to utilize lighter components that otherwise could not be blended into gasoline due to their high vapor pressures. Feed to alkylation unit can include pentanes from light cracked gasoline treaters, isobutanes from butane isomerization unit, and C3/C4 streams from delayed coking units. Isomerization Units - C4/C5/C6 A refinery that has an alkylation plant is not likely to have exactly enough is-butane to match the proplylene and butylene (olefin) feeds. The refiner usually has two choices - buy iso-butane or make it in a butane isomerization (Bl) plant. Isomerization is the rearrangement of straight chain hydrocarbon molecules to form branched chain products or to convert normal paraffins to their isomer. -
Chemical Kinetic Research on HCCI & Diesel Fuels
Lawrence Livermore National Laboratory Chemical Kinetic Research on HCCI & Diesel Fuels William J. Pitz (PI), Charles K. Westbrook, Marco Mehl, M. Lee Davisson Lawrence Livermore National Laboratory May 12, 2009 Project ID # ace_13_pitz DOE National Laboratory Advanced Combustion Engine R&D Merit Review and Peer Evaluation Washington, DC This presentation does not contain any proprietary or confidential information This work performed under the auspices of the U.S. Department of Energy by LLNL-PRES-411416 Lawrence Livermore National Laboratory under Contract DE-AC52-07NA27344 Overview Timeline Barriers • Ongoing project with yearly • Increases in engine efficiency and direction from DOE decreases in engine emissions are being inhibited by an inadequate ability to simulate in-cylinder combustion and emission formation processes • Chemical kinetic models are critical for Budget improved engine modeling and ultimately for engine design • Funding received in FY08 and expected in FY09: Partners • 800K (DOE) • Interactions/ collaborations: DOE Working Group, National Labs, many universities, FACE Working group. Lawrence Livermore National Laboratory 2 LLNL-PRES-411416LLNL-PRES- 411416 2009 DOE Merit Review Relevance to DOE objectives Support DOE objectives of petroleum-fuel displacement by • Improving engine models so that further improvements in engine efficiency can be made • Developing models for alternative fuels (biodiesel, ethanol, other biofuels, oil-sand derived fuels, Fischer-Tropsch derived fuels) so that they can be better used -
Exposure Investigation Protocol: the Identification of Air Contaminants Around the Continental Aluminum Plant in New Hudson, Michigan Conducted by ATSDR and MDCH
Exposure Investigation Protocol - Continental Aluminum New Hudson, Lyon Township, Oakland County, Michigan Exposure Investigation Protocol: The Identification of Air Contaminants Around the Continental Aluminum Plant in New Hudson, Michigan Conducted by ATSDR and MDCH MDCH/ATSDR - 2004 Exposure Investigation Protocol - Continental Aluminum New Hudson, Lyon Township, Oakland County, Michigan TABLE OF CONTENTS OBJECTIVE/PURPOSE..................................................................................................... 3 RATIONALE...................................................................................................................... 4 BACKGROUND ................................................................................................................ 5 AGENCY ROLES .............................................................................................................. 6 ESTABLISHING CRITERIA ............................................................................................ 7 “Odor Events”................................................................................................................. 7 Comparison Values......................................................................................................... 7 METHODS ....................................................................................................................... 12 Instantaneous (“Grab”) Air Sampling........................................................................... 12 Continuous Air Monitoring.......................................................................................... -
UNITED STATES PATENT of FICE 2,640,086 PROCESS for SEPARATING HYDROGEN FLUORIDE from CHLORODFLUORO METHANE Robert H
Patented May 26, 1953 2,640,086 UNITED STATES PATENT of FICE 2,640,086 PROCESS FOR SEPARATING HYDROGEN FLUORIDE FROM CHLORODFLUORO METHANE Robert H. Baldwin, Chadds Ford, Pa., assignor to E. H. du Pont de Nemours and Company, Wi inington, Del, a corporation of Delaware No Drawing. Application December 15, 1951, Serial No. 261,929 9 Claims. (C. 260-653) 2 This invention relates to a process for Sep These objects are accomplished essentially by arating hydrogen fluoride from monochlorodi Subjecting a mixture of hydrogen fluoride and fluoronethane, and more particularly, separat Inonochlorodifluoromethane in the liquid phase ing these components from the reaction mixture to temperatures below 0° C., preferably at about obtained in the fluorination of chloroform with -30° C. to -50° C., at either atmospheric or hydrogen fluoride, Super-atmospheric pressures, together with from In the fluorination of chloroform in the prest about 0.25 mol to about 2.5 mols of chloroform ence Of a Catalyst, a reaction mixture is pro per mol of chlorodifluoronethane contained in duced which consists essentially of HCl, HF, the mixture and separating an upper layer rich CHCIF2, CHCl2F, CHCls, and CHF3. A method O in HF from a lower organic layer. The proceSS of Separating these components is disclosed in is operative with mixtures containing up to 77% U. S. Patent No. 2,450,414 which involves sep by weight of HF. arating the components by a special fractional It has been found that chloroform is substan distillation under appropriate temperatures and tially immiscible With EIF at temperatures be pressures. -
Cylinder Valve Selection Quick Reference for Valve Abbreviations
SHERWOOD VALVE COMPRESSED GAS PRODUCTS Appendix Cylinder Valve Selection Quick Reference for Valve Abbreviations Use the Sherwood Cylinder Valve Series Abbreviation Chart on this page with the Sherwood Cylinder Valve Selection Charts found on pages 73–80. The Sherwood Cylinder Valve Selection Chart are for reference only and list: • The most commonly used gases • The Compressed Gas Association primary outlet to be used with each gas • The Sherwood valves designated for use with this gas • The Pressure Relief Device styles that are authorized by the DOT for use with these gases PLEASE NOTE: The Sherwood Cylinder Valve Selection Charts are partial lists extracted from the CGA V-1 and S-1.1 pamphlets. They can change without notice as the CGA V-1 and S-1.1 pamphlets are amended. Sherwood will issue periodic changes to the catalog. If there is any discrepancy or question between these lists and the CGA V-1 and S-1.1 pamphlets, the CGA V-1 and S-1.1 pamphlets take precedence. Sherwood Cylinder Valve Series Abbreviation Chart Abbreviation Sherwood Valve Series AVB Small Cylinder Acetylene Wrench-Operated Valves AVBHW Small Cylinder Acetylene Handwheel-Operated Valves AVMC Small Cylinder Acetylene Wrench-Operated Valves AVMCHW Small Cylinder Acetylene Handwheel-Operated Valves AVWB Small Cylinder Acetylene Wrench-Operated Valves — WB Style BV Hi/Lo Valves with Built-in Regulator DF* Alternative Energy Valves GRPV Residual Pressure Valves GV Large Cylinder Acetylene Valves GVT** Vertical Outlet Acetylene Valves KVAB Post Medical Valves KVMB Post Medical Valves NGV Industrial and Chrome-Plated Valves YVB† Vertical Outlet Oxygen Valves 1 * DF Valves can be used with all gases; however, the outlet will always be ⁄4"–18 NPT female. -
Transition Metal Hydrides That Mediate Catalytic Hydrogen Atom Transfers
Transition Metal Hydrides that Mediate Catalytic Hydrogen Atom Transfers Deven P. Estes Submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy in the Graduate School of Arts and Sciences COLUMBIA UNIVERSITY 2014 © 2014 Deven P. Estes All Rights Reserved ABSTRACT Transition Metal Hydrides that Mediate Catalytic Hydrogen Atom Transfers Deven P. Estes Radical cyclizations are important reactions in organic chemistry. However, they are seldom used industrially due to their reliance on neurotoxic trialkyltin hydride. Many substitutes for tin hydrides have been developed but none have provided a general solution to the problem. Transition metal hydrides with weak M–H bonds can generate carbon centered radicals by hydrogen atom transfer (HAT) to olefins. This metal to olefin hydrogen atom transfer (MOHAT) reaction has been postulated as the initial step in many hydrogenation and hydroformylation reactions. The Norton group has shown MOHAT can mediate radical cyclizations of α,ω dienes to form five and six membered rings. The reaction can be done catalytically if 1) the product metalloradical reacts with hydrogen gas to reform the hydride and 2) the hydride can perform MOHAT reactions. The Norton group has shown that both CpCr(CO)3H and Co(dmgBF2)2(H2O)2 can catalyze radical cyclizations. However, both have significant draw backs. In an effort to improve the catalytic efficiency of these reactions we have studied several potential catalyst candidates to test their viability as radical cyclization catalysts. I investigate the hydride CpFe(CO)2H (FpH). FpH has been shown to transfer hydrogen atoms to dienes and styrenes. I measured the Fe–H bond dissociation free energy (BDFE) to be 63 kcal/mol (much higher than previously thought) and showed that this hydride is not a good candidate for catalytic radical cyclizations. -
Oxidation of Ethane to Ethylene and Acetic Acid by Movnbo Catalysts Martial Roussel, Michel Bouchard, Elisabeth Bordes-Richard, Khalid Karim, Saleh Al-Sayari
Oxidation of ethane to ethylene and acetic acid by MoVNbO catalysts Martial Roussel, Michel Bouchard, Elisabeth Bordes-Richard, Khalid Karim, Saleh Al-Sayari To cite this version: Martial Roussel, Michel Bouchard, Elisabeth Bordes-Richard, Khalid Karim, Saleh Al-Sayari. Oxida- tion of ethane to ethylene and acetic acid by MoVNbO catalysts. Catalysis Today, Elsevier, 2005, 99, pp.77-87. 10.1016/j.cattod.2004.09.026. hal-00103604 HAL Id: hal-00103604 https://hal.archives-ouvertes.fr/hal-00103604 Submitted on 4 Oct 2006 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Oxidation of ethane to ethylene and acetic acid by MoVNbO catalysts M. Roussel 1, M. Bouchard 1, E. Bordes-Richard 1*, K. Karim 2, S. Al-Sayari 2 1: Laboratoire de Catalyse de Lille, UMR CNRS 8010, USTL-ENSCL, 59655 Villeneuve d'Ascq Cedex, France 2: SABIC R&T, P.O. Box 42503, Riyadh, Saoudi Arabia ABSTRACT The influence of niobium on the physicochemical properties of the Mo-V-O system and on its catalytic properties in the oxidation of ethane to ethylene and acetic acid is examined. Solids based on MoV 0.4 Ox and MoV 0.4 Nb 0.12 Oy composition and calcined at 350 or 400°C were studied by X-ray diffraction, and by laser Raman and X-ray photoelectron spectroscopies. -
Energy and the Hydrogen Economy
Energy and the Hydrogen Economy Ulf Bossel Fuel Cell Consultant Morgenacherstrasse 2F CH-5452 Oberrohrdorf / Switzerland +41-56-496-7292 and Baldur Eliasson ABB Switzerland Ltd. Corporate Research CH-5405 Baden-Dättwil / Switzerland Abstract Between production and use any commercial product is subject to the following processes: packaging, transportation, storage and transfer. The same is true for hydrogen in a “Hydrogen Economy”. Hydrogen has to be packaged by compression or liquefaction, it has to be transported by surface vehicles or pipelines, it has to be stored and transferred. Generated by electrolysis or chemistry, the fuel gas has to go through theses market procedures before it can be used by the customer, even if it is produced locally at filling stations. As there are no environmental or energetic advantages in producing hydrogen from natural gas or other hydrocarbons, we do not consider this option, although hydrogen can be chemically synthesized at relative low cost. In the past, hydrogen production and hydrogen use have been addressed by many, assuming that hydrogen gas is just another gaseous energy carrier and that it can be handled much like natural gas in today’s energy economy. With this study we present an analysis of the energy required to operate a pure hydrogen economy. High-grade electricity from renewable or nuclear sources is needed not only to generate hydrogen, but also for all other essential steps of a hydrogen economy. But because of the molecular structure of hydrogen, a hydrogen infrastructure is much more energy-intensive than a natural gas economy. In this study, the energy consumed by each stage is related to the energy content (higher heating value HHV) of the delivered hydrogen itself. -
Chapter 2: Alkanes Alkanes from Carbon and Hydrogen
Chapter 2: Alkanes Alkanes from Carbon and Hydrogen •Alkanes are carbon compounds that contain only single bonds. •The simplest alkanes are hydrocarbons – compounds that contain only carbon and hydrogen. •Hydrocarbons are used mainly as fuels, solvents and lubricants: H H H H H H H H H H H H C H C C H C C C C H H C C C C C H H H C C H H H H H H CH2 H CH3 H H H H CH3 # of carbons boiling point range Use 1-4 <20 °C fuel (gasses such as methane, propane, butane) 5-6 30-60 solvents (petroleum ether) 6-7 60-90 solvents (ligroin) 6-12 85-200 fuel (gasoline) 12-15 200-300 fuel (kerosene) 15-18 300-400 fuel (heating oil) 16-24 >400 lubricating oil, asphalt Hydrocarbons Formula Prefix Suffix Name Structure H CH4 meth- -ane methane H C H H C H eth- -ane ethane 2 6 H3C CH3 C3H8 prop- -ane propane C4H10 but- -ane butane C5H12 pent- -ane pentane C6H14 hex- -ane hexane C7H16 hept- -ane heptane C8H18 oct- -ane octane C9H20 non- -ane nonane C10H22 dec- -ane decane Hydrocarbons Formula Prefix Suffix Name Structure H CH4 meth- -ane methane H C H H H H C2H6 eth- -ane ethane H C C H H H H C H prop- -ane propane 3 8 H3C C CH3 or H H H C H 4 10 but- -ane butane H3C C C CH3 or H H H C H 4 10 but- -ane butane? H3C C CH3 or CH3 HydHrydorcocaarrbobnos ns Formula Prefix Suffix Name Structure H CH4 meth- -ane methane H C H H H H C2H6 eth- -ane ethane H C C H H H H C3H8 prop- -ane propane H3C C CH3 or H H H C H 4 10 but- -ane butane H3C C C CH3 or H H H C H 4 10 but- -ane iso-butane H3C C CH3 or CH3 HydHrydoroccarbrobnsons Formula Prefix Suffix Name Structure H H -
Ammonium Bifluoride CAS No
Product Safety Summary Ammonium Bifluoride CAS No. 1341-49-7 This Product Safety Summary is intended to provide a general overview of the chemical substance. The information on the summary is basic information and is not intended to provide emergency response information, medical information or treatment information. The summary should not be used to provide in-depth safety and health information. In-depth safety and health information can be found in the Safety Data Sheet (SDS) for the chemical substance. Names • Ammonium bifluoride (ABF) • Ammonium difluoride • Ammonium acid fluoride • Ammonium hydrogen difluoride • Ammonium fluoride compound with hydrogen fluoride (1:1) Product Overview Solvay Fluorides, LLC does not sell ammonium bifluoride directly to consumers. Ammonium bifluoride is used in industrial applications and in other processes where workplace exposures can occur. Ammonium bifluoride (ABF) is used for cleaning and etching of metals before they are further processed. It is used as an oil well acidifier and in the etching of glass or cleaning of brick and ceramics. It may also be used for pH adjustment in industrial textile processing or laundries. ABF is available as a solid or liquid solution (in water). Ammonium bifluoride is a corrosive chemical and contact can severely irritate and burn the skin and eyes causing possible permanent eye damage. Breathing ammonium bifluoride can severely irritate and burn the nose, throat, and lungs, causing nosebleeds, cough, wheezing and shortness of breath. On contact with water or moist skin, ABF can release hydrofluoric acid, a very dangerous acid. Inhalation or ingestion of large amounts of ammonium bifluoride can cause nausea, vomiting and loss of appetite.