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A Comparison of Composite Transparent Conducting Oxides Based on the Binary Compounds Cdo and Sno2
October 2001 • NREL/CP-520-31017 A Comparison of Composite Transparent Conducting Oxides Based on the Binary Compounds CdO and SnO2 Preprint X. Li, T. Gessert, C. DeHart, T. Barnes, H. Moutinho, Y. Yan, D. Young, M. Young, J. Perkins, and T. Coutts To be presented at the NCPV Program Review Meeting Lakewood, Colorado 14-17 October 2001 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 The submitted manuscript has been offered by an employee of the Midwest Research Institute (MRI), a contractor of the US Government under Contract No. DE-AC36-99GO10337. Accordingly, the US Government and MRI retain a nonexclusive royalty-free license to publish or reproduce the published form of this contribution, or allow others to do so, for US Government purposes. 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. -
The Combination of Calcium Oxide and Cu/Zro2 Catalyst and Their Selective Products for CO2 Hydrogenation
Article The Combination of Calcium Oxide and Cu/ZrO2 Catalyst and their Selective Products for CO2 Hydrogenation Soipatta Soisuwan1,a,b,*, Wilasinee Wisaijorn1, Chalida Nimnul1, Orawan Maunghimapan1, and Piyasan Praserthdam2 1 Department of Chemical Engineering, Faculty of Engineering, Burapha University, 169 Long-Hard Bangsaen Road, Saensuk Sub-District, Muang District, Chonburi, 20130, Thailand 2 Center of Excellence in Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Phayathai Road, Pathuwan District, Bangkok 10330, Thailand E-mail: [email protected] (Corresponding author), [email protected] Abstract. The catalytic activities of Cu/ZrO2_CaO catalysts were investigated on CO2 hydrogenation. The CO2 hydrogenations were carried out over combination of calcium oxide and Cu/ZrO2 catalyst. Two calcination temperatures were chosen at 300 and 650 oC according to thermal decomposition results. The catalysts were characterized by means of N2 adsorption-desorption, H2 temperature programmed reduction and X-ray diffraction. The CO2 hydrogenation under atmospheric pressure and at 250 oC was carried out over copper-based catalysts combined with calcium oxide namely i.e. Cu/ZrO 2 _CaO300, Cu/ZrO 2 _CaO650, Cu/ZrO2_Cu/CaO and Cu/ZrO2+CaO. The catalytic activities over all catalysts were consistent for 4 hours. The catalytic reaction rates over copper-based catalysts were in the range of 21.8 – 47.4 mol L-1 s-1 g cat-1. The modification of calcium oxide can improve the catalytic activity of copper-based catalysts to 47.4 mol L-1 s-1 g cat-1. The calcination temperature can cause a difference in active species that impact on product selectivity. -
Calcium Oxide
CALCIUM OXIDE Prepared at the 19th JECFA (1975), published in NMRS 55B (1976) and in FNP 52 (1992). Metals and arsenic specifications revised at the 59th JECFA (2002). An ADI ‘Not limited’ was established at the 9th JECFA (1965). SYNONYMS Lime; INS No. 529 DEFINITION Chemical names Calcium oxide C.A.S. number 1305-78-8 Chemical formula CaO Formula weight 56.08 Assay Not less than 95.0% after ignition DESCRIPTION Odourless, hard, white or greyish white masses or granules, or white to greyish white powder FUNCTIONAL USES Alkali, dough conditioner, yeast food CHARACTERISTICS IDENTIFICATION Solubility (Vol. 4) Slightly soluble in water, insoluble in ethanol, soluble in glycerol (Caution: Protect eyes when adding water) Reaction with water Moisten the sample with water; heat is generated (Caution: Protect eyes when adding water). Test for alkali The sample is alkaline to moistened litmus paper Test for calcium (Vol. 4) Passes test PURITY Loss on ignition (Vol. 4) Not more than 10% (1 g, about 800o to constant weight) Barium Not more than 0.03% Cautiously mix 1.5 g of the sample with 10 ml water, add 15 ml of dilute hydrochloric acid TS, dilute to 30 ml with water and filter. To 20 ml of the filtrate add 2 g of sodium acetate, 1 ml of dilute acetic acid TS and 0.5 ml of potassium chromate TS and allow to stand for 15 min. The turbidity of the solution is not greater than that of a control prepared by adding water to 0.3 ml of barium standard solution (1.779 g barium chloride in 1000 ml of water) to make to 20 ml, adding 2 g of sodium acetate, 1 ml of dilute acetic acid TS and 0.5 ml of potassium chromate TS and allowing to stand for 15 min. -
Appendix a of Final Environmental Impact Statement for a Geologic Repository for the Disposal of Spent Nuclear Fuel and High-Lev
Appendix A Inventory and Characteristics of Spent Nuclear Fuel, High-Level Radioactive Waste, and Other Materials Inventory and Characteristics of Spent Nuclear Fuel, High-Level Radioactive Waste, and Other Materials TABLE OF CONTENTS Section Page A. Inventory and Characteristics of Spent Nuclear Fuel, High-Level Radioactive Waste, and Other Materials ................................................................................................................................. A-1 A.1 Introduction .............................................................................................................................. A-1 A.1.1 Inventory Data Summary .................................................................................................... A-2 A.1.1.1 Sources ......................................................................................................................... A-2 A.1.1.2 Present Storage and Generation Status ........................................................................ A-4 A.1.1.3 Final Waste Form ......................................................................................................... A-6 A.1.1.4 Waste Characteristics ................................................................................................... A-6 A.1.1.4.1 Mass and Volume ................................................................................................. A-6 A.1.1.4.2 Radionuclide Inventories ...................................................................................... A-8 A.1.1.4.3 -
Interaction of Water with the Cao(001) Surface † ‡ † § ‡ † ∥ Yuichi Fujimori, Xunhua Zhao, Xiang Shao, , Sergey V
Article pubs.acs.org/JPCC Interaction of Water with the CaO(001) Surface † ‡ † § ‡ † ∥ Yuichi Fujimori, Xunhua Zhao, Xiang Shao, , Sergey V. Levchenko, Niklas Nilius, , † ⊥ † Martin Sterrer,*, , and Hans-Joachim Freund † ‡ Department of Chemical Physics and Theory Department, Fritz-Haber-Institut der Max-Planck-Gesellschaft, Faradayweg 4-6, 14195 Berlin, Germany ∥ Institute of Physics, Carl-von-Ossietzky University, 26111 Oldenburg, Germany ⊥ Institute of Physics, University of Graz, Universitatsplatz̈ 5, 8010 Graz, Austria *S Supporting Information ABSTRACT: The interaction of water with the CaO(001) surface has been studied from ultrahigh-vacuum to submillibar water vapor pressures and at temperatures of 100 and 300 K using well-structured CaO(001)/Mo(001) thin-film model systems. Infrared reflection absorption spectroscopy (IRAS), X-ray photoelectron spectroscopy (XPS), and scanning tunneling microscopy (STM) in combination with density functional theory (DFT) calculations have been employed to reveal the correlation between the vibrational frequencies of the hydroxyl groups and the distinct hydroxylated surface phases that develop as a function of water exposure. In the low-coverage regime, water monomers, small water clusters, and one-dimensional water chains are formed on the CaO(001) surface. At increasing water coverages, water-induced structural disorder is observed, indicating 2+ partial solvation of Ca ions. Partial transformation of CaO(001) into a Ca(OH)2-like phase occurs upon dosing of water at submillibar water pressure. In addition, it was found that interfacial hydroxyl groups formed on the CaO(001) surface during water exposure at temperatures as low as 100 K shift the temperatures for ice desorption and for the transition from amorphous solid water to crystalline ice by 10 K as compared to those for the nonhydroxylated MgO surface. -
The Preparation of Polysiloxanes from Halosilanes
European Patent Office © Publication number: 0 205 066 Office europeen des brevets A2 © EUROPEAN PATENT APPLICATION © Application number: 86107474.8 © Int. CI.4: C 08 G 77/08 © Date of filing: 02.06.86 © Priority: 14.06.85 US 744708 © Applicant: DOW CORNING CORPORATION P.O. Box 1767 Midland Michigan 48640(US) © Date of publication of application: 17.12.86 Bulletin 86/51 @ Inventor: Marko, Ollie William Route 2 Box 60 © Designated Contracting States: Carrollton Kentucky(US) DE FR GB @ Inventor: Steinmeyer, Robert David 214 Deatherage Drive Carrollton Kentucky(US) © Inventor: Rentsch, Stefan Felix 5800 Siebert Midland Michigan(US) © Representative: Sternagel, Hans-Gunther, Dr. et al, Patentanwalte Dr. Michael Hann Dr. H.-G. Sternagel Sander Aue30 D-5060 Bergisch Gladbach 2(DE) © The preparation of polysiloxanes from halosilanes. ©@ This This invention relates to a process for the preparation of polysiloxanes by reacting halosilanes in the presence of metal oxides and sulfolane. Preferred metal oxides include anti- mony (III) oxide, antimony (V) oxide, cadmium oxide, calcium oxide, copper (II) oxide, indium oxide, iron (II) oxide, iron (III) oxide, magnesium oxide, manganese (II) oxide, mercury (II) oxide, nickel (II) oxide, thallium (III) oxide, tin (II) oxide, and zinc oxide. Improved yields and rates of reaction can be observed with the process of this invention. Croydon Printing Company Ltd. This invention relates to a process for the preparation of polysiloxanes from halosilanes. 14ore specifically, this invention relates to a process for the preparation of polysiloxanes by reacting halosilanes in the presence of metal oxides and sulfolane. Polysiloxanes are most commonly prepared by the hydrolysis of halosilanes. -
Cadmium Oxide Ec Number: 215-146-2 Cas Number: 1306-19-0
SUBSTANCE NAME: CADMIUM OXIDE EC NUMBER: 215-146-2 CAS NUMBER: 1306-19-0 MEMBER STATE COMMITTEE SUPPORT DOCUMENT FOR IDENTIFICATION OF CADMIUM OXIDE AS A SUBSTANCE OF VERY HIGH CONCERN BECAUSE OF ITS CMR 1 PROPERTIES AND BECAUSE OF ITS ADVERSE EFFECTS ON KIDNEY AND BONE TISSUES AFTER PROLONGED EXPOSURE, WHICH CAUSE PROBABLE SERIOUS EFFECTS TO HUMAN HEALTH WHICH GIVE RISE TO AN EQUIVALENT LEVEL OF CONCERN TO THOSE OF CMR AND PBT/vPvB2 SUBSTANCES Adopted on 12 June 2013 1 CMR means carcinogenic, mutagenic or toxic for reproduction 2 PBT means persistent, bioaccumulative and toxic; vPvB means very persistent and very bioaccumulative SVHC SUPPORT DOCUMENT – CADMIUM OXIDE CONTENTS 1 IDENTITY OF THE SUBSTANCE AND PHYSICAL AND CHEMICAL PROPERTIES................. 9 1.1 Name and other identifiers of the substance ....................................................... 9 1.2 Composition of the substance............................................................................ 9 1.3 Physico-chemical properties .............................................................................. 10 2 HARMONISED CLASSIFICATION AND LABELLING....................................................... 11 3 ENVIRONMENTAL FATE PROPERTIES........................................................................ 12 4 HUMAN HEALTH HAZARD ASSESSMENT ................................................................... 14 4.1 Toxicokinetics (absorption, metabolism, distribution and elimination)..................... 14 4.2 Kidney toxicity ............................................................................................... -
Material Safety Data Sheet for Calcium Oxide ------Section I - Identity
Flammability 0 Health Reactivity 1 1 Specific Hazard Calcium Oxide Material Safety Data Sheet for Calcium Oxide --------------------------------------------------------------------------------------------------------------------------- Section I - Identity --------------------------------------------------------------------------------------------------------------------------- Manufacturer's name and address: Ash Grove Cement Company 8900 Indian Creek Parkway P. O. Box 25900 Overland Park, KS 66225 Emergency Telephone Number: (913) 451-8900 Information Telephone Number: (913) 451-8900 Chemical Name and Synonyms: Calcium oxide, CaO, quicklime, lime, unslaked lime Trade Name and Synonyms: Pebble Quicklime, Cal-Max CAS No.: 1305-78-8 Date Revised: July 2000 --------------------------------------------------------------------------------------------------------------------------- Section II - Hazardous Ingredients --------------------------------------------------------------------------------------------------------------------------- CAS Number OSHA PEL ACGIH TLV Quicklime, CaO 1305-78-8 5 mg/m3 2 mg/m3 PEL = 10mg/m3 3 Quartz, crystalline silica 14808-60-7 % SiO2*+2 0.05 mg/m * Calcium oxide may contain greater than 0.1% quartz, crystalline silica. Chronic exposure above the allowed limit to the respirable dust of materials containing crystalline silica or quartz may cause silicosis. *Respirable fraction ACGIH American Conference of Governmental Industrial Hygienists OSHA Occupational Safety and Health Administration PEL Permissible Exposure -
Chemical Names and CAS Numbers Final
Chemical Abstract Chemical Formula Chemical Name Service (CAS) Number C3H8O 1‐propanol C4H7BrO2 2‐bromobutyric acid 80‐58‐0 GeH3COOH 2‐germaacetic acid C4H10 2‐methylpropane 75‐28‐5 C3H8O 2‐propanol 67‐63‐0 C6H10O3 4‐acetylbutyric acid 448671 C4H7BrO2 4‐bromobutyric acid 2623‐87‐2 CH3CHO acetaldehyde CH3CONH2 acetamide C8H9NO2 acetaminophen 103‐90‐2 − C2H3O2 acetate ion − CH3COO acetate ion C2H4O2 acetic acid 64‐19‐7 CH3COOH acetic acid (CH3)2CO acetone CH3COCl acetyl chloride C2H2 acetylene 74‐86‐2 HCCH acetylene C9H8O4 acetylsalicylic acid 50‐78‐2 H2C(CH)CN acrylonitrile C3H7NO2 Ala C3H7NO2 alanine 56‐41‐7 NaAlSi3O3 albite AlSb aluminium antimonide 25152‐52‐7 AlAs aluminium arsenide 22831‐42‐1 AlBO2 aluminium borate 61279‐70‐7 AlBO aluminium boron oxide 12041‐48‐4 AlBr3 aluminium bromide 7727‐15‐3 AlBr3•6H2O aluminium bromide hexahydrate 2149397 AlCl4Cs aluminium caesium tetrachloride 17992‐03‐9 AlCl3 aluminium chloride (anhydrous) 7446‐70‐0 AlCl3•6H2O aluminium chloride hexahydrate 7784‐13‐6 AlClO aluminium chloride oxide 13596‐11‐7 AlB2 aluminium diboride 12041‐50‐8 AlF2 aluminium difluoride 13569‐23‐8 AlF2O aluminium difluoride oxide 38344‐66‐0 AlB12 aluminium dodecaboride 12041‐54‐2 Al2F6 aluminium fluoride 17949‐86‐9 AlF3 aluminium fluoride 7784‐18‐1 Al(CHO2)3 aluminium formate 7360‐53‐4 1 of 75 Chemical Abstract Chemical Formula Chemical Name Service (CAS) Number Al(OH)3 aluminium hydroxide 21645‐51‐2 Al2I6 aluminium iodide 18898‐35‐6 AlI3 aluminium iodide 7784‐23‐8 AlBr aluminium monobromide 22359‐97‐3 AlCl aluminium monochloride -
A Kinetic Study of the Strontium Extraction by Metallothermic Reduction Using Submerged Sro Powders Injection ⁎ R
Available online at www.sciencedirect.com Materials Letters 62 (2008) 637–640 www.elsevier.com/locate/matlet A kinetic study of the strontium extraction by metallothermic reduction using submerged SrO powders injection ⁎ R. Muñiz a, , A. Flores a, J. Torres a, S. Luna a, N. Rodríguez b a CINVESTAV Unidad Saltillo, Saltillo-Monterrey highway Km. 13.5 P.O. Box 663, 25000, Saltillo, Coahuila, México b Instituto Tecnológico de Saltillo V. Carranza Blvd. 2500, Saltillo, Coahuila, México Received 3 May 2007; accepted 8 June 2007 Available online 16 June 2007 Abstract This work reports the results of laboratory experiments conduced to follow the kinetics of strontium recovery into the Al–Mg alloy by metallothermic reduction of SrO. The reagent was incorporated to molten alloy by the use of submerged powders injection technique. The variables analyzed were the injection time, the melt temperature and the initial magnesium content. Magnesium is added to the melt to increase the reactivity and reduce the surface tension of the molten aluminum. It was possible to increase the strontium content from 0 to 5 wt.% after 60 min of treatment. The results were fitted to a general kinetic equation, which allowed it to obtain the kinetic parameters, i.e. order of reaction and activation energy of the process. As the main mechanism of the strontium recovery process is of diffusive type, the global process rate increases as the temperature and initial amount of the magnesium increased. © 2007 Elsevier B.V. All rights reserved. Keywords: Strontium recovery; Submerged powder injection; Metallothermic reduction; Reaction kinetic 1. Introduction a vapour by vacuum distillation [2]. -
Synthesis Target Structures for Alkaline Earth Oxide Clusters
inorganics Article Synthesis Target Structures for Alkaline Earth Oxide Clusters Susanne G. E. T. Escher, Tomas Lazauskas ID , Martijn A. Zwijnenburg and Scott M. Woodley * ID Department of Chemistry, University College London, London WC1H 0AJ, UK; [email protected] (S.G.E.T.E.); [email protected] (T.L.); [email protected] (M.A.Z.) * Correspondence: [email protected] Received: 21 November 2017; Accepted: 7 February 2018; Published: 21 February 2018 Abstract: Knowing the possible structures of individual clusters in nanostructured materials is an important first step in their design. With previous structure prediction data for BaO nanoclusters as a basis, data mining techniques were used to investigate candidate structures for magnesium oxide, calcium oxide and strontium oxide clusters. The lowest-energy structures and analysis of some of their structural properties are presented here. Clusters that are predicted to be ideal targets for synthesis, based on being both the only thermally accessible minimum for their size, and a size that is thermally accessible with respect to neighbouring sizes, include global minima for: sizes n = 9, 15, 16, 18 and 24 for (MgO)n; sizes n = 8, 9, 12, 16, 18 and 24 for (CaO)n; the greatest number of sizes of (SrO)n clusters (n = 8, 9, 10, 12, 13, 15, 16, 18 and 24); and for (BaO)n sizes of n = 8, 10 and 16. Keywords: inorganic nanoclusters; global optimization; data mining; computational modelling; magnesium oxide; calcium oxide; strontium oxide; barium oxide 1. Introduction Structure determination of materials plays an important role in materials design because the properties of materials are inherently linked to their atomic and electronic structure. -
Mineral Carbonation and Industrial Uses of Carbon Dioxide 319 7
Chapter 7: Mineral carbonation and industrial uses of carbon dioxide 319 7 Mineral carbonation and industrial uses of carbon dioxide Coordinating Lead Author Marco Mazzotti (Italy and Switzerland) Lead Authors Juan Carlos Abanades (Spain), Rodney Allam (United Kingdom), Klaus S. Lackner (United States), Francis Meunier (France), Edward Rubin (United States), Juan Carlos Sanchez (Venezuela), Katsunori Yogo (Japan), Ron Zevenhoven (Netherlands and Finland) Review Editors Baldur Eliasson (Switzerland), R.T.M. Sutamihardja (Indonesia) 320 IPCC Special Report on Carbon dioxide Capture and Storage Contents EXECUTIVE SUMMARY 321 7.3 Industrial uses of carbon dioxide and its emission reduction potential 330 7.1 Introduction 322 7.3.1 Introduction 330 7.3.2 Present industrial uses of carbon dioxide 332 7.2 Mineral carbonation 322 7.3.3 New processes for CO2 abatement 332 7.2.1 Definitions, system boundaries and motivation 322 7.3.4 Assessment of the mitigation potential of CO2 7.2.2 Chemistry of mineral carbonation 323 utilization 333 7.2.3 Sources of metal oxides 324 7.3.5 Future scope 334 7.2.4 Processing 324 7.2.5 Product handling and disposal 328 References 335 7.2.6 Environmental impact 328 7.2.7 Life Cycle Assessment and costs 329 7.2.8 Future scope 330 Chapter 7: Mineral carbonation and industrial uses of carbon dioxide 321 EXECUTIVE SUMMARY This Chapter describes two rather different options for carbon and recycled using external energy sources. The resulting dioxide (CO2) storage: (i) the fixation of CO2 in the form of carbonated solids must be stored at an environmentally suitable inorganic carbonates, also known as ‘mineral carbonation’ or location.