List of Major Physical Hazards
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Transport of Dangerous Goods
ST/SG/AC.10/1/Rev.16 (Vol.I) Recommendations on the TRANSPORT OF DANGEROUS GOODS Model Regulations Volume I Sixteenth revised edition UNITED NATIONS New York and Geneva, 2009 NOTE The designations employed and the presentation of the material in this publication do not imply the expression of any opinion whatsoever on the part of the Secretariat of the United Nations concerning the legal status of any country, territory, city or area, or of its authorities, or concerning the delimitation of its frontiers or boundaries. ST/SG/AC.10/1/Rev.16 (Vol.I) Copyright © United Nations, 2009 All rights reserved. No part of this publication may, for sales purposes, be reproduced, stored in a retrieval system or transmitted in any form or by any means, electronic, electrostatic, magnetic tape, mechanical, photocopying or otherwise, without prior permission in writing from the United Nations. UNITED NATIONS Sales No. E.09.VIII.2 ISBN 978-92-1-139136-7 (complete set of two volumes) ISSN 1014-5753 Volumes I and II not to be sold separately FOREWORD The Recommendations on the Transport of Dangerous Goods are addressed to governments and to the international organizations concerned with safety in the transport of dangerous goods. The first version, prepared by the United Nations Economic and Social Council's Committee of Experts on the Transport of Dangerous Goods, was published in 1956 (ST/ECA/43-E/CN.2/170). In response to developments in technology and the changing needs of users, they have been regularly amended and updated at succeeding sessions of the Committee of Experts pursuant to Resolution 645 G (XXIII) of 26 April 1957 of the Economic and Social Council and subsequent resolutions. -
Rhode Island Hazardous Substance List
Rhode Island Hazardous Substance List Source: T - ACGIH F - NFPA49 C - IARC Alphabetical Order C.A.S. ACGIH NFPA IARC CHEMICAL NAME 13010-47-4 C 1,-(2-Chloroethyl)-3-cyclohexyl-1-Nitrosourea 76-11-9 T 1,1,1,2-tetrachloro-2,2-difluoroethane 76-12-0 T 1,1,2,2-tetrachloro-1,2-difluoroethane 79-34-5 T 1,1,2,2-tetrachloroethane - skin 76-13-1 T 1,1,2-trichloro-1,2,2-trifluoroethane 79-00-5 T F C 1,1,2-trichloroethane - skin 594-72-9 T 1,1-Dichloro-1-nitroethane 74-34-3 T 1,1-dichloroethane 57-14-7 T 1,1-dimethylhydrazine (udmh) 96-18-4 T 1,2,3-trichloropropane 120-82-1 T 1,2,4-Trichlorobenzene 106-88-7 F 1,2-Butylene oxide 107-15-3 T F 1,2-Diaminoethane 96-12-8 C 1,2-Dibromo-3-chloropropane 106-93-4 T F C 1,2-Dibromoethane - skin 107-06-2 T F 1,2-Dichlorethane 540-59-0 T F 1,2-Dichloroethene 540-59-0 T F 1,2-Dichloroetylene 1615-80-1 C 1,2-Diethylhydrazine C 1,2-Dimethyl hydrazine - skin 106-99-0 T F 1,3-Butadiene 118-52-5 T 1,3-Dichloro-5,5-dimethylhydantoin 542-75-6 T F 1,3-Dichloropropene (cis and trans) 542-75-6 T F 1,3-Dichloropropylene 110-56-5 F 1,4-Dichlorobutane 123-91-1 T F C 1,4-Dioxane 1120-71-4 1-3-Propane sultone 110-53-2 F 1-Bromopentane 106-89-8 T F C 1-Chloro,2,3-epoxy-propane 600-25-9 T 1-Chloro-1-nitropropane 97-00-7 F 1-chloro-2,4-dinitrobenzene 543-59-9 F 1-Chloropentane 112-30-1 F 1-Decanol 111-27-3 F 1-Hexanol 141-79-7 T F 1-Isobutenyl methyl ketone 108-03-2 T F 1-Nitropropane 71-41-0 F 1-Pentanol 110-58-7 F 1-Pentylamine 111-40-0 T F 2,2'-Diaminodiethylamine 111-44-4 F 2,2'Dichlorodiethyl ether 75-99-0 T 2,2-dichloropropionic acid 556-52-5 T 2,3-Epoxy-1-propanol 93-76-5 T 2,4,5-T 95-95-4 F 2,4,5-trichlorophenol 88-06-2 F C 2,4,6-trichlorophenol 118-96-7 T F 2,4,6-Trinitro Toluene 479-95-8 T 2,4,6-Trinitrophenyl-methylnitramine 94-75-7 T 2,4-d (2,4-dichlorophenoxyacetic acid) 97-02-9 F 2,4-dinitroaniline 584-84-9 T F 2,4-Tolylene diisocyanate 108-83-8 T 2,6-Dimethyl-4-heptanone 108-83-8 T 2,6-Dimethyl-4-heptanone 128-37-0 T 2,6-Ditert. -
Transition Metal Phosphides for the Catalytic Hydrodeoxygenation of Waste Oils Into Green Diesel
catalysts Review Transition Metal Phosphides for the Catalytic Hydrodeoxygenation of Waste Oils into Green Diesel M. Consuelo Alvarez-Galvan * , Jose M. Campos-Martin * and Jose L. G. Fierro * Energy and Sustainable Chemistry Group (EQS), Instituto de Catálisis y Petroleoquímica, CSIC, c/Marie Curie, 2 Cantoblanco, 28049 Madrid, Spain * Correspondence: [email protected] (M.C.A.-G.); [email protected] (J.M.C.-M.); jlgfi[email protected] (J.L.G.F.) Received: 28 February 2019; Accepted: 15 March 2019; Published: 22 March 2019 Abstract: Recently, catalysts based on transition metal phosphides (TMPs) have attracted increasing interest for their use in hydrodeoxygenation (HDO) processes destined to synthesize biofuels (green or renewable diesel) from waste vegetable oils and fats (known as hydrotreated vegetable oils (HVO)), or from bio-oils. This fossil-free diesel product is produced completely from renewable raw materials with exceptional quality. These efficient HDO catalysts present electronic properties similar to noble metals, are cost-efficient, and are more stable and resistant to the presence of water than other classical catalytic formulations used for hydrotreatment reactions based on transition metal sulfides, but they do not require the continuous supply of a sulfide source. TMPs develop a bifunctional character (metallic and acidic) and present tunable catalytic properties related to the metal type, phosphorous-metal ratio, support nature, texture properties, and so on. Here, the recent progress in TMP-based catalysts for HDO of waste oils is reviewed. First, the use of TMPs in catalysis is addressed; then, the general aspects of green diesel (from bio-oils or from waste vegetable oils and fats) production by HDO of nonedible oil compounds are presented; and, finally, we attempt to describe the main advances in the development of catalysts based on TMPs for HDO, with an emphasis on the influence of the nature of active phases and effects of phosphorous, promoters, and preparation methods on reactivity. -
Antimony Pentachloride Apc
ANTIMONY PENTACHLORIDE APC CAUTIONARY RESPONSE INFORMATION 4. FIRE HAZARDS 7. SHIPPING INFORMATION 4.1 Flash Point: 7.1 Grades of Purity: 99+% Common Synonyms Liquid Colorless to brown Unpleasant odor Not flammable 7.2 Storage Temperature: Ambient Antimony (V) chloride 4.2 Flammable Limits in Air: Not flammable Antimony perchloride 7.3 Inert Atmosphere: No requirement 4.3 Fire Extinguishing Agents: Not pertinent Sinks in water. Irritating vapor is produced. Freezing point is 37°F. 7.4 Venting: Pressure-vacuum 4.4 Fire Extinguishing Agents Not to Be 7.5 IMO Pollution Category: Currently not available Avoid contact with liquid. Keep people away. Used: Do not use water or foam on Wear rubber overclothing (including gloves). adjacent fires. 7.6 Ship Type: Currently not available Stop discharge if possible. 4.5 Special Hazards of Combustion 7.7 Barge Hull Type: Currently not available Evacuate. Products: Not pertinent Isolate and remove discharged material. 4.6 Behavior in Fire: Irritating fumes of Notify local health and pollution control agencies. 8. HAZARD CLASSIFICATIONS hydrogen chloride given off when water Protect water intakes. or foam is used to extinguish adjacent 8.1 49 CFR Category: Corrosive material fire. 8.2 49 CFR Class: 8 Not flammable. 4.7 Auto Ignition Temperature: Not pertinent Fire POISONOUS GASES ARE PRODUCED WHEN HEATED. 8.3 49 CFR Package Group: II DO NOT USE WATER ON ADJACENT FIRES. 4.8 Electrical Hazards: Not pertinent 8.4 Marine Pollutant: No 4.9 Burning Rate: Not pertinent 8.5 NFPA Hazard Classification: Exposure Call for medical aid. 4.10 Adiabatic Flame Temperature: Not pertinent Category Classification VAPOR Health Hazard (Blue)......... -
(12) Patent Application Publication (10) Pub. No.: US 2005/0044778A1 Orr (43) Pub
US 20050044778A1 (19) United States (12) Patent Application Publication (10) Pub. No.: US 2005/0044778A1 Orr (43) Pub. Date: Mar. 3, 2005 (54) FUEL COMPOSITIONS EMPLOYING Publication Classification CATALYST COMBUSTION STRUCTURE (51) Int. CI.' ........ C10L 1/28; C1OL 1/24; C1OL 1/18; (76) Inventor: William C. Orr, Denver, CO (US) C1OL 1/12; C1OL 1/26 Correspondence Address: (52) U.S. Cl. ................. 44/320; 44/435; 44/378; 44/388; HOGAN & HARTSON LLP 44/385; 44/444; 44/443 ONE TABOR CENTER, SUITE 1500 1200 SEVENTEENTH ST DENVER, CO 80202 (US) (57) ABSTRACT (21) Appl. No.: 10/722,127 Metallic vapor phase fuel compositions relating to a broad (22) Filed: Nov. 24, 2003 Spectrum of pollution reducing, improved combustion per Related U.S. Application Data formance, and enhanced Stability fuel compositions for use in jet, aviation, turbine, diesel, gasoline, and other combus (63) Continuation-in-part of application No. 08/986,891, tion applications include co-combustion agents preferably filed on Dec. 8, 1997, now Pat. No. 6,652,608. including trimethoxymethylsilane. Patent Application Publication Mar. 3, 2005 US 2005/0044778A1 FIGURE 1 CALCULATING BUNSEN BURNER LAMINAR FLAME VELOCITY (LFV) OR BURNING VELOCITY (BV) CONVENTIONAL FLAME LUMINOUS FLAME Method For Calculating Bunsen Burner Laminar Flame Velocity (LHV) or Burning Velocity Requires Inside Laminar Cone Angle (0) and The Gas Velocity (Vg). LFV = A, SIN 2 x VG US 2005/0044778A1 Mar. 3, 2005 FUEL COMPOSITIONS EMPLOYING CATALYST Chart of Elements (CAS version), and mixture, wherein said COMBUSTION STRUCTURE element or derivative compound, is combustible, and option 0001) The present invention is a CIP of my U.S. -
Lithium Hydride Powered PEM Fuel Cells for Long-Duration Small Mobile Robotic Missions
Lithium Hydride Powered PEM Fuel Cells for Long-Duration Small Mobile Robotic Missions Jekanthan Thangavelautham, Daniel Strawser, Mei Yi Cheung Steven Dubowsky Abstract— This paper reports on a study to develop power supplies for small mobile robots performing long duration missions. It investigates the use of fuel cells to achieve this objective, and in particular Proton Exchange Membrane (PEM) fuel cells. It is shown through a representative case study that, in theory, fuel cell based power supplies will provide much longer range than the best current rechargeable battery technology. It also briefly discusses an important limitation that prevents fuel cells from achieving their ideal performance, namely a practical method to store their fuel (hydrogen) in a form that is compatible with small mobile field robots. A very efficient Fig. 1. Example of small robots (Left) A ball shaped hopping robot concept fuel storage concept based on water activated lithium hydride for exploration of extreme terrains and caves developed for NASA. (Right) (LiH) is proposed that releases hydrogen on demand. This iRobot 110 Firstlook used for observation, security and search and rescue. concept is very attractive because water vapor from the air is passively extracted or waste water from the fuel cell is recycled and transferred to the lithium hydride where the hydrogen is the near future. Hence, new means for powering field robots “stripped” from water and is returned to the fuel cell to form more water. This results in higher hydrogen storage efficiencies need to be considered. than conventional storage methods. Experimental results are This paper explores the use of fuel cells, and in particular presented that demonstrate the effectiveness of the approach. -
Chemical Chemical Hazard and Compatibility Information
Chemical Chemical Hazard and Compatibility Information Acetic Acid HAZARDS & STORAGE: Corrosive and combustible liquid. Serious health hazard. Reacts with oxidizing and alkali materials. Keep above freezing point (62 degrees F) to avoid rupture of carboys and glass containers.. INCOMPATIBILITIES: 2-amino-ethanol, Acetaldehyde, Acetic anhydride, Acids, Alcohol, Amines, 2-Amino-ethanol, Ammonia, Ammonium nitrate, 5-Azidotetrazole, Bases, Bromine pentafluoride, Caustics (strong), Chlorosulfonic acid, Chromic Acid, Chromium trioxide, Chlorine trifluoride, Ethylene imine, Ethylene glycol, Ethylene diamine, Hydrogen cyanide, Hydrogen peroxide, Hydrogen sulfide, Hydroxyl compounds, Ketones, Nitric Acid, Oleum, Oxidizers (strong), P(OCN)3, Perchloric acid, Permanganates, Peroxides, Phenols, Phosphorus isocyanate, Phosphorus trichloride, Potassium hydroxide, Potassium permanganate, Potassium-tert-butoxide, Sodium hydroxide, Sodium peroxide, Sulfuric acid, n-Xylene. Acetone HAZARDS & STORAGE: Store in a cool, dry, well ventilated place. INCOMPATIBILITIES: Acids, Bromine trifluoride, Bromine, Bromoform, Carbon, Chloroform, Chromium oxide, Chromium trioxide, Chromyl chloride, Dioxygen difluoride, Fluorine oxide, Hydrogen peroxide, 2-Methyl-1,2-butadiene, NaOBr, Nitric acid, Nitrosyl chloride, Nitrosyl perchlorate, Nitryl perchlorate, NOCl, Oxidizing materials, Permonosulfuric acid, Peroxomonosulfuric acid, Potassium-tert-butoxide, Sulfur dichloride, Sulfuric acid, thio-Diglycol, Thiotrithiazyl perchlorate, Trichloromelamine, 2,4,6-Trichloro-1,3,5-triazine -
Chemical Name Federal P Code CAS Registry Number Acutely
Acutely / Extremely Hazardous Waste List Federal P CAS Registry Acutely / Extremely Chemical Name Code Number Hazardous 4,7-Methano-1H-indene, 1,4,5,6,7,8,8-heptachloro-3a,4,7,7a-tetrahydro- P059 76-44-8 Acutely Hazardous 6,9-Methano-2,4,3-benzodioxathiepin, 6,7,8,9,10,10- hexachloro-1,5,5a,6,9,9a-hexahydro-, 3-oxide P050 115-29-7 Acutely Hazardous Methanimidamide, N,N-dimethyl-N'-[2-methyl-4-[[(methylamino)carbonyl]oxy]phenyl]- P197 17702-57-7 Acutely Hazardous 1-(o-Chlorophenyl)thiourea P026 5344-82-1 Acutely Hazardous 1-(o-Chlorophenyl)thiourea 5344-82-1 Extremely Hazardous 1,1,1-Trichloro-2, -bis(p-methoxyphenyl)ethane Extremely Hazardous 1,1a,2,2,3,3a,4,5,5,5a,5b,6-Dodecachlorooctahydro-1,3,4-metheno-1H-cyclobuta (cd) pentalene, Dechlorane Extremely Hazardous 1,1a,3,3a,4,5,5,5a,5b,6-Decachloro--octahydro-1,2,4-metheno-2H-cyclobuta (cd) pentalen-2- one, chlorecone Extremely Hazardous 1,1-Dimethylhydrazine 57-14-7 Extremely Hazardous 1,2,3,4,10,10-Hexachloro-6,7-epoxy-1,4,4,4a,5,6,7,8,8a-octahydro-1,4-endo-endo-5,8- dimethanonaph-thalene Extremely Hazardous 1,2,3-Propanetriol, trinitrate P081 55-63-0 Acutely Hazardous 1,2,3-Propanetriol, trinitrate 55-63-0 Extremely Hazardous 1,2,4,5,6,7,8,8-Octachloro-4,7-methano-3a,4,7,7a-tetra- hydro- indane Extremely Hazardous 1,2-Benzenediol, 4-[1-hydroxy-2-(methylamino)ethyl]- 51-43-4 Extremely Hazardous 1,2-Benzenediol, 4-[1-hydroxy-2-(methylamino)ethyl]-, P042 51-43-4 Acutely Hazardous 1,2-Dibromo-3-chloropropane 96-12-8 Extremely Hazardous 1,2-Propylenimine P067 75-55-8 Acutely Hazardous 1,2-Propylenimine 75-55-8 Extremely Hazardous 1,3,4,5,6,7,8,8-Octachloro-1,3,3a,4,7,7a-hexahydro-4,7-methanoisobenzofuran Extremely Hazardous 1,3-Dithiolane-2-carboxaldehyde, 2,4-dimethyl-, O- [(methylamino)-carbonyl]oxime 26419-73-8 Extremely Hazardous 1,3-Dithiolane-2-carboxaldehyde, 2,4-dimethyl-, O- [(methylamino)-carbonyl]oxime. -
Boron- and Nitrogen-Based Chemical Hydrogen Storage Materials
international journal of hydrogen energy 34 (2009) 2303–2311 Available at www.sciencedirect.com journal homepage: www.elsevier.com/locate/he Review Boron- and nitrogen-based chemical hydrogen storage materials Tetsuo Umegaki, Jun-Min Yan, Xin-Bo Zhang, Hiroshi Shioyama, Nobuhiro Kuriyama, Qiang Xu* National Institute of Advanced Industrial Science and Technology (AIST), 1-8-31 Midorigaoka, Ikeda, Osaka 563-8577, Japan article info abstract Article history: Boron- and nitrogen-based chemical hydrides are expected to be potential hydrogen Received 20 November 2008 carriers for PEM fuel cells because of their high hydrogen contents. Significant efforts have Accepted 4 January 2009 been devoted to decrease their dehydrogenation and hydrogenation temperatures and Available online 4 February 2009 enhance the reaction kinetics. This article presents an overview of the boron- and nitrogen-based compounds as hydrogen storage materials. Keywords: ª 2009 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights Boron-based chemical hydrides reserved. Nitrogen-based chemical hydrides Hydrogen storage Dehydrogenation Hydrogenation Ammonia borane 1. Introduction in operating the system at high temperature poses an obstacle to its practical application. Chemical hydrogen Hydrogen is a globally accepted clean fuel. The use of storage materials, due to their high hydrogen contents, are hydrogen fuel cells in portable electronic devices or vehicles expected as potential hydrogen sources for fuel cells. Among requires lightweight -
United States Patent Office Patented Aug
3,459,514 United States Patent Office Patented Aug. 5, 1969 2 quired is smaller than the requirements of the prior art. 3,459,514 It is still a further object of the present invention to pro METHOD FOR PREPARING ALKAL vide a process whereby the amount of by-product pro METAL BOROHYDRDES James D. Johnston and Albert P. Giraitis, Baton Rouge, duced is less than that produced by the prior art. Other La., assignors to Ethyl Corporation, New York, N.Y., a objects will become apparent from the ensuing descrip corporation of Virginia tion. No Drawing. Continuation-in-part of applications Ser. No. The above objects are accomplished by the provision 308,691, Sept. 13, 1963, and Ser. No. 322,054, Nov. 7, of a process for producing an alkali metal borohydride 1963. This application Oct. 1, 1964, Ser. No. 400,888 which comprises reacting together an alkali metal hy ret, C. C01b 6/14 O dride, desiccated borax, hydrogen, and silicon at a tem U.S. C. 23-362 6 Claims perature within the range of from about 200 C. to about 900° C. The alkali metal present during the course of the re ABSTRACT OF THE DISCLOSURE action is a member selected from Group I-A of the A method of preparing alkali metal borohydrides com Periodic Chart of the Elements, Fisher Scientific Com prising reacting an alkali metal or alkali metal hydride, pany, 1955. The alkali metals include lithium, sodium, desiccated borax, hydrogen, and silicon, in an inert hy potassium, rubidium, and cesium. Sodium is a preferred drocarbon at about 250° C. -
Catalysis of the Oxygen Evolution Reaction by 4–10 Nm Cobalt Nanoparticles
Topics in Catalysis https://doi.org/10.1007/s11244-018-0923-4 ORIGINAL PAPER Catalysis of the Oxygen Evolution Reaction by 4–10 nm Cobalt Nanoparticles Edward Locke1 · Shan Jiang1 · Simon K. Beaumont1 © The Author(s) 2018 Abstract Electrolysis of water is key technology, not only for clean energy production, but to ensure a continued supply of hydrogen beyond fossil resources, essential to the manufacture of many chemical goods other than fuels. Cobalt nanomaterials have been widely identified as a promising candidate for the anode (oxygen evolution) reaction in this process, but much work has focused on applied materials or electrode design. Given the importance of oxidation state changes Co(III) → Co(IV) in the accepted reaction mechanism, in this work we look at size effects in small (4–10 nm) cobalt nanoparticles, where the ease of oxidation for lower cobalt oxidation states is known to change with particle size. To discriminate between geometric and chemical effects we have compared the catalysts in this study to others in the literature by turnover frequency (widely used in other areas of catalysis), in addition to the more commonly employed performance metric of the overpotential required to produce a current density of 10 mA cm−2. Comparisons are drawn to key examples of using well defined nanomaterials (where the surface are of cobalt sites can be estimated). This has enabled an estimated intrinsic turnover rate of ~ 1 O2 mol- ecule per surface Co atom per second at an overpotential of 500 mV in the oxygen evolution reaction under typical alkaline reaction conditions (pH 14.0) to be identified. -
WO 2016/074683 Al 19 May 2016 (19.05.2016) W P O P C T
(12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization International Bureau (10) International Publication Number (43) International Publication Date WO 2016/074683 Al 19 May 2016 (19.05.2016) W P O P C T (51) International Patent Classification: (81) Designated States (unless otherwise indicated, for every C12N 15/10 (2006.01) kind of national protection available): AE, AG, AL, AM, AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, (21) International Application Number: BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DK, DM, PCT/DK20 15/050343 DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, (22) International Filing Date: HN, HR, HU, ID, IL, IN, IR, IS, JP, KE, KG, KN, KP, KR, 11 November 2015 ( 11. 1 1.2015) KZ, LA, LC, LK, LR, LS, LU, LY, MA, MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, OM, (25) Filing Language: English PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, SC, (26) Publication Language: English SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW. (30) Priority Data: PA 2014 00655 11 November 2014 ( 11. 1 1.2014) DK (84) Designated States (unless otherwise indicated, for every 62/077,933 11 November 2014 ( 11. 11.2014) US kind of regional protection available): ARIPO (BW, GH, 62/202,3 18 7 August 2015 (07.08.2015) US GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, ST, SZ, TZ, UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, (71) Applicant: LUNDORF PEDERSEN MATERIALS APS TJ, TM), European (AL, AT, BE, BG, CH, CY, CZ, DE, [DK/DK]; Nordvej 16 B, Himmelev, DK-4000 Roskilde DK, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, (DK).