Equilibrium Constants for the Formation of Silver
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The Reductive Amination of Ethanol Using Supported Metal Catalysts
The Reductive Amination of Ethanol using Supported Metal Catalysts By Gary Stanton Sewell- BSc (Chern. Eng.) Submitted to the University of Cape Town in fulfilment of the requirements for the degree of '• DOCTOR OF PHILOSOPHY University of Cape Town Department of Chemi~al Engineering 14 August 1996 University of Cape Town Rondebosch Cape Town South Africa ---"----""_______ " __ The copyright of this thesis vests in the author. No quotation from it or information derived from it is to be published without full acknowledgement of the source. The thesis is to be used for private study or non- commercial research purposes only. Published by the University of Cape Town (UCT) in terms of the non-exclusive license granted to UCT by the author. University of Cape Town Acknowledgements Acknowledgements I would like to thank my supervisors Dr Eric van Steen and Professor Cyril O'Connor for their guidance and encouragement without which this thesis would not have been possible. My thanks also go to Dr Klaus Moller for the fruitful discussions and to Professor Mark Dry for his help with aspects of metal catalysis. I would like to thank Rob for the great times, Tony for his friendship, Jannie for his cool hairstyle and Rein for having a comfortable couch. Thanks to Dave for introducing me to the finer intricacies of toolboxes, to Ashley for his unending optimism and to Peter for always losing at pool. To the II Young Ones II, Chappie, St. John, Frank, Andrew, Mary and Frans, thanks for the great parties and may the department survive you. -
Oxidation of Amines at Absorber Conditions for CO2 Capture from Flue Gas
Energy Procedia Energy Procedia 4 (2011) 171–178 Energy Procedia 00 (2010) 000–000 www.elsevier.com/locate/procedia www.elsevier.com/locate/XXX GHGT-10 Oxidation of amines at absorber conditions for CO2 capture from flue gas Alexander K. Voice, Gary T. Rochelle* Department of Chemical Engineering, Luminant Carbon Management Program, University of Texas, 1 University Station C0400, Austin, TX 78712, USA Elsevier use only: Received date here; revised date here; accepted date here Abstract Eleven amines that are suitable for CO2 capture by an amine scrubbing system have been evaluated for their stability in the presence of oxygen. Six amines produced measureable quantities of ammonia in the order: 1,2-diamino-propane (DAP) > monoethanolamine (MEA) > ethylene diamine (EDA) > 3-methylamino-1-propylamine (MAPA) > potassium glycinate (GLY) > potassium taurinate (TAU). Five other amines produced no detectable ammonia (<0.2mmol/kg/hr): piperazine (PZ), 1-methyl-piperazine (1-MPZ), diglycolamine (DGA®), 2-amino-2-methyl-propanol (AMP), and 1- methyl-diethanolamine (MDEA). The effect of temperature on ammonia production from aqueous MEA in the presence of Inh. A was also measured. The activation energy of ammonia production varied from 86 kJ/mol with no inhibitor to 133 kJ/mol with 200 mM Inh. A. At 55°C, ammonia production was reduced by 74-99% with 50-200 mM Inh. A. ⃝©c 20102011 Elsevier Published Ltd. by ElsevierAll rights Ltd. reserved Keywords: Oxidative degradation; amine screening; ammonia rates; activation energy. 1.0 Introduction Aqueous monoethanolamine (MEA) is the baseline solvent for carbon dioxide capture from flue gas by absorption- stripping. MEA is an attractive solvent, because it is relatively cheap, has a fast reaction rate with CO2, and has a high heat of absorption. -
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. -
02/06/2019 12:05 PM Appendix 3745-21-09 Appendix A
ACTION: Final EXISTING DATE: 02/06/2019 12:05 PM Appendix 3745-21-09 Appendix A List of Organic Chemicals for which Paragraphs (DD) and (EE) of Rule 3745-21-09 of the Administrative Code are Applicable Organic Chemical Organic Chemical Acetal Benzaldehyde Acetaldehyde Benzamide Acetaldol Benzene Acetamide Benzenedisulfonic acid Acetanilide Benzenesulfonic acid Acetic acid Benzil Acetic Anhydride Benzilic acid Acetone Benzoic acid Acetone cyanohydrin Benzoin Acetonitrile Benzonitrile Acetophenone Benzophenone Acetyl chloride Benzotrichloride Acetylene Benzoyl chloride Acrolein Benzyl alcohol Acrylamide Benzylamine Acrylic acid Benzyl benzoate Acrylonitrile Benzyl chloride Adipic acid Benzyl dichloride Adiponitrile Biphenyl Alkyl naphthalenes Bisphenol A Allyl alcohol Bromobenzene Allyl chloride Bromonaphthalene Aminobenzoic acid Butadiene Aminoethylethanolamine 1-butene p-aminophenol n-butyl acetate Amyl acetates n-butyl acrylate Amyl alcohols n-butyl alcohol Amyl amine s-butyl alcohol Amyl chloride t-butyl alcohol Amyl mercaptans n-butylamine Amyl phenol s-butylamine Aniline t-butylamine Aniline hydrochloride p-tertbutyl benzoic acid Anisidine 1,3-butylene glycol Anisole n-butyraldehyde Anthranilic acid Butyric acid Anthraquinone Butyric anhydride Butyronitrile Caprolactam APPENDIX p(183930) pa(324943) d: (715700) ra(553210) print date: 02/06/2019 12:05 PM 3745-21-09, Appendix A 2 Carbon disulfide Cyclohexene Carbon tetrabromide Cyclohexylamine Carbon tetrachloride Cyclooctadiene Cellulose acetate Decanol Chloroacetic acid Diacetone alcohol -
) Synthesis of Quinoline and Derivatives1)
Faculty of Science Damietta University Chemistry Department An Essay on : Evaluation of the Synthesis, Reactions and Biological Activities of Quinolines _______________________________________________________________________ ____________________________________________________________ Presented BY MOHAMED ELNEKETY b.s.C student (special 2016 chemistry) Acknowledgment First my thank and gratitude to Allah I am greatly indebted to Prof.Dr : FAWZIA EL-ABLACK Professor of Organic Chemistry Chemistry Department Faculty of Science Damietta University To his supervision on my research. He taught me How to design a research plan and how to write it. I appreciate your help, guiding and encouragement. Again many thanks for what you have done for me. Fourth year Chemistry Department 2015 - 2016 Contents : Page Introduction..……………………………………..…………………….…..3 (1) Synthesis of Quinolines………………….………….…….…....5 1.1 Skraup reaction…………………………………………………..5 1.2 Combes quinoline synthesis…………………………….…….…6 1.3 Doebner reaction..………………………………..…….………..6 1.4 Doebner–Miller reaction …………………………….………….7 1.5 Knorr quinoline synthesis…………………………….…………7 1.6 Friedlaender Synthesis……………………………….………….8 1.7 Pfitzinger Synthesis………………………………….…………..8 1.8 Green preparation of quinolone……………………….……….9 1.9 Quinolines by Forming the N–C-2 Bond……………….……...11 1.10 From Aldehyde and Aniline……………………………………11 1.11 By condensation reaction of ortho-acylanilines and Alkenyl iodides…………………………………………….……12 1.12 By dehydrogenation of tetrahydroquinolines………….……..12 1.13 By cyclization of 2-ethynylanilines -
Phencyclidine (PCP) Abuse: an Appraisal
PHENCYCLIDINE Latest Revision: May 16, 2005 1. SYNONYMS CFR: Phencyclidine CAS #: Base: 77-10-1 Hydrochloride: 956-90-1 Other Names: 1-(1-Phenylcyclohexyl) piperidine PCP Angel dust CI-395 Sernylan Sernyl 2. CHEMICAL AND PHYSICAL DATA 2.1. CHEMICAL DATA Form Chemical Formula Molecular Weight Melting Point (°C) Base C17H25N 243.4 46-46.5 Hydrochloride C17H26NCl 279.9 233-235 2.2. SOLUBILITY Form A C E H M W Base FS FS FS FS S VSS Hydrochloride SS FS I I FS FS A = acetone, C = chloroform, E = ether, H = hexane, M = methanol and W = water, VS = very soluble, FS = freely soluble, S = soluble, PS = sparingly soluble, SS = slightly soluble, VSS = very slightly soluble and I = insoluble 3. SCREENING TECHNIQUES 3.1. COLOR TESTS REAGENT COLOR PRODUCED p-Dimethylaminobenzaldehyde Red 3.2. CRYSTAL TESTS REAGENT CRYSTALS FORMED Potassium permanganate Bow-tie shaped 3.3. THIN-LAYER CHROMATOGRAPHY Visualization Acidified iodoplatinate spray Dragendorff spray COMPOUND RELATIVE R1 System System System TLC17 TLC11 TLC16 piperidine 0.4 0.2 0.1 PCP 1.0 1.0 1.0 piperidinocyclohexylcarbonitrile (PCC) 4.5 1.7 1.7 Both iodoplatinate and Dragendorff sprays will detect the three components. Iodine vapor produces a white spot outlined in brown for PCC, where as PCP and piperidine both give brown spots. 3.4. GAS CHROMATOGRAPHY Method PCP-GCS1 Instrument: Gas chromatograph operated in split mode with FID Column: 5% phenyl/95% methyl silicone 12 m x 0.2 mm x 0.33 µm film thickness Carrier gas: Helium at 1.0 mL/min Temperatures: Injector: 270°C Detector: 280°C Oven program: 1) 175°C initial temperature for 1.0 min 2) Ramp to 275°C at 15°C/min 3) Hold final temperature for 3.0 min Injection Parameters: Split Ratio = 60:1, 1 µL injected Samples are to be dissolved or diluted in chloroform and filtered. -
Title Several Reactions of Isocyanide and Related Compounds( Dissertation 全文 ) Author(S) Kobayashi, Shiro Citation
Several Reactions of Isocyanide and Related Compounds( Title Dissertation_全文 ) Author(s) Kobayashi, Shiro Citation 京都大学 Issue Date 1969-07-23 URL https://doi.org/10.14989/doctor.k916 Right Type Thesis or Dissertation Textversion author Kyoto University IN ISOCYANIDE AND COMPOUNDS 6 IR B s SEVERAL REACTIONS OF ISOCYANIDE AND RELATED COMPOUNDS 1 9 6 9 SHIRO KOBA Y ASHI PREFACE In the present thesis are collected the author's studies which have been carried out under the direction of Profossor Takeo Saegusa at Kyoto University during 1966 -- 1969. The studies include new organic reactions of isocyanide, carbon monoxide and carbene, which are characterized by a carbon atom carry ing lone-pair electrons. Reactions catalyzed by copper compounds as well as other Groups IB and IIB metal compounds constitute the central featl1re of tIl':' present studies. New organic reactions of isocyanidE' without catalysts are also presented. The author expresses his deep gratitude to Professor Takeo Saes'Usa for his constant guidance and encouragement throughout the work. Grateful acknowledgement is also made to Dr. Yoshihiko Ito for his valuable advice an? dis cussions during the course of studies. The author wishes to express his deep appreciation to Messrs. Kiwami Hirota, Nobuyuki Takeda, Toyoji Shimizu, Hiroshi Yoshioka, Yoshiharu Okumura. and Ikuo Morino for their active collaborations in carrying out the experiments. Shiro Kobayashi Department of Synthetic Chemistry Kyoto University March, 1969. (i) CON TEN TS Page INTRODUCTION ............................ .. 1 SYNOPSES .............................. .. 7 PART I. INSERTION REACTIONS OF ISOCYNJIDE CATALYZED BY COPPER COMPOUNDS 15 Chapter 1. Reaction of Isocyanide with Amine Catalyzed by Groups IB and IIB Metal Compounds, main ly by Copper Compounds. -
Kinetic Modeling of the Thermal Destruction of Nitrogen Mustard
Kinetic Modeling of the Thermal Destruction of Nitrogen Mustard Gas Juan-Carlos Lizardo-Huerta, Baptiste Sirjean, Laurent Verdier, René Fournet, Pierre-Alexandre Glaude To cite this version: Juan-Carlos Lizardo-Huerta, Baptiste Sirjean, Laurent Verdier, René Fournet, Pierre-Alexandre Glaude. Kinetic Modeling of the Thermal Destruction of Nitrogen Mustard Gas. Journal of Physical Chemistry A, American Chemical Society, 2017, 121 (17), pp.3254-3262. 10.1021/acs.jpca.7b01238. hal-01708219 HAL Id: hal-01708219 https://hal.archives-ouvertes.fr/hal-01708219 Submitted on 13 Feb 2018 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. Kinetic Modeling of the Thermal Destruction of Nitrogen Mustard Gas Juan-Carlos Lizardo-Huerta†, Baptiste Sirjean†, Laurent Verdier‡, René Fournet†, Pierre-Alexandre Glaude†,* †Laboratoire Réactions et Génie des Procédés, CNRS, Université de Lorraine, 1 rue Grandville BP 20451 54001 Nancy Cedex, France ‡DGA Maîtrise NRBC, Site du Bouchet, 5 rue Lavoisier, BP n°3, 91710 Vert le Petit, France *corresponding author: [email protected] Abstract The destruction of stockpiles or unexploded ammunitions of nitrogen mustard (tris (2- chloroethyl) amine, HN-3) requires the development of safe processes. -
Monoethanolamine Diethanolamine Triethanolamine DSA9781.Qxd 1/31/03 10:21 AM Page 2
DSA9781.qxd 1/31/03 10:21 AM Page 1 ETHANOLAMINES Monoethanolamine Diethanolamine Triethanolamine DSA9781.qxd 1/31/03 10:21 AM Page 2 CONTENTS Introduction ...............................................................................................................................2 Ethanolamine Applications.........................................................................................................3 Gas Sweetening ..................................................................................................................3 Detergents, Specialty Cleaners, Personal Care Products.......................................................4 Textiles.................................................................................................................................4 Metalworking ......................................................................................................................5 Other Applications...............................................................................................................5 Ethanolamine Physical Properties ...............................................................................................6 Typical Physical Properties ....................................................................................................6 Vapor Pressure of Ethanolamines (Figure 1).........................................................................7 Heat of Vaporization of Ethanolamines (Figure 2)................................................................7 Specific -
Synthesis of Morpholine and Derivatives Thereof Via the Reaction of Dialkylene Glycol and Ammonia
Europaisches Patentamt J» European Patent Office © Publication number: 0036 331 B2 Office europeen des brevets NEW EUROPEAN PATENT SPECIFICATION Date of publication of the new patent specification: mtci C07D 295/02 18.10.89 Application number: 81301126.9 Date of filing: 17.03.81 Synthesis of morpholine and derivatives thereof via the reaction of dialkylene glycol and ammonia. Priority: 17.03.80 US 130782 © Proprietor: AIR PRODUCTS AND CHEMICALS, INC., P.O. Box 538, Allentown, Pennsylvania 18105 (US) Date of publication of application : 23.09.81 Bulletin 81/38 Inventor: Daughenbaugh, Randall Jay, Box 334A, RD No. 1 Barton, PA 19505 (US) Inventor: Dixon, Dale David, Box 53D RD No. 2, @ Publication of the grant of the patent : Kutztown, PA 19530 (US) 01 .08.84 Bulletin 84/31 Inventor: Fowlkes, Robert Lee, 220 Cedar Street, Milton Florida 32570 (US) @ Mention of the opposition decision : 18.10.89 Bulletin 89/42 Representative: Burford, Anthony Frederick et al, W.H. Beck, Greener & Co. 7 Stone Buildings Lincoln's Inn, London WC2A3SZ(GB) Designated Contracting States: AT BE CH DE FR GB IT LI LU NL SE References cited - DE-A-2738115 DE-A-2 758 769 Cfi DE-C- 1 941 633 DE-C-2 040 507 SU-A-175 512 CO US-A-3151 112 US-A-3154 544 O CHEMICAL ABSTRACTS, vol. 75, no. 23, December 6. <0 1971, oage 327, abstract 140871h. COLUMBUS, OHIO O (US) o Q. Ill ACTORUM AG EP 0036 331 B2 Description carrying out the process the reactants are charged to an autoclave and reacted at 240°C and Technical field 25x105 Pa (25 atmospheres) in the presence of This invention relates to an improved process for hydrogen. -
Ttes Patent 0 Patented Jan
1 R 2,777,846 ttes Patent 0 Patented Jan. 1 5, 1957 l. 2 furic acid as the dehydration medium. In carrying out 2,777,846 ‘the process of this invention, glass, ceramics and‘ acid resistant steels such as the high-silicon. alloy known as PROCESS OF PRODUCING MORPHOLINE FROM “Duriron” can be used as the material of construction DIETHANQLAMINE for the reaction vessel. George Joseph Laemmle, In, Austin, 'l‘ex., assignor to At the conclusion of the reaction, themorpholine is Jefferson Chemical Company, Inc., New York, N. Y., separated from the reaction product mixture by steam a corporation of Delaware distillation after addition of alkali in amount sufficient to No Drawing. Application September 27, 1954, render the mixture strongly alkaline. '_ Theresultant aque ous solution of morpholine may be concentrated and/or Serial No. 458,685 puri?ed in any known manner. 9 Claims. (Cl. 260-247)‘ While it is preferred to carry out the reaction under atmospheric pressure conditions or under a pressure of This invention relates to the 2-5 pounds above atmospheric, somewhat higher pres production of morpholine 15 sures may be used if desired and the reaction mixture from diethanolamine. All percentages and parts herein are on a weight basis. may be re?uxed under superatmospheric pressure, the overhead vapors condensed and returned to the reaction Dehydration of diethanolamine employing. about 1.8 mixture. Particularly preferred procedure involves car parts of 66° Baumé sulfuric acid per part of diethanol~ rying out the reaction at a pressure of 2-5 pounds above amine by slowly adding the amine to the acid while agi 20 atmospheric so that when the reaction is completed, the tating and cooling with cold- Water and then heating the reaction products may be discharged under this pressure reaction mixture for from 7 to 8 hours at 175° to 180° into the neutralizer without requiring the use of pumps C. -
Study of Various Aqueous and Non-Aqueous Amine Blends for Hydrogen Sulfide Removal from Natural Gas
processes Article Study of Various Aqueous and Non-Aqueous Amine Blends for Hydrogen Sulfide Removal from Natural Gas Usman Shoukat , Diego D. D. Pinto and Hanna K. Knuutila * Department of Chemical Engineering, Norwegian University of Science and Technology (NTNU), 7491 Trondheim, Norway; [email protected] (U.S.); [email protected] (D.D.D.P.) * Correspondence: [email protected] Received: 8 February 2019; Accepted: 8 March 2019; Published: 15 March 2019 Abstract: Various novel amine solutions both in aqueous and non-aqueous [monoethylene glycol (MEG)/triethylene glycol(TEG)] forms have been studied for hydrogen sulfide (H2S) absorption. The study was conducted in a custom build experimental setup at temperatures relevant to subsea operation conditions and atmospheric pressure. Liquid phase absorbed H2S, and amine concentrations were measured analytically to calculate H2S loading (mole of H2S/mole of amine). Maximum achieved H2S loadings as the function of pKa, gas partial pressure, temperature and amine concentration are presented. Effects of solvent type on absorbed H2S have also been discussed. Several new solvents showed higher H2S loading as compared to aqueous N-Methyldiethanolamine (MDEA) solution which is the current industrial benchmark compound for selective H2S removal in natural gas sweetening process. Keywords: H2S absorption; amine solutions; glycols; desulfurization; aqueous and non-aqueous solutions 1. Introduction Natural gas is considered one of the cleanest forms of fossil fuel. Its usage in industrial processes and human activities is increasing worldwide, providing 23.4% of total world energy requirement in 2017 [1]. Natural gas is half of the price of crude oil and produces 29% less carbon dioxide than oil per unit of energy output [2].