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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 -
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]. -
APPENDIX G Acid Dissociation Constants
harxxxxx_App-G.qxd 3/8/10 1:34 PM Page AP11 APPENDIX G Acid Dissociation Constants § ϭ 0.1 M 0 ؍ (Ionic strength ( † ‡ † Name Structure* pKa Ka pKa ϫ Ϫ5 Acetic acid CH3CO2H 4.756 1.75 10 4.56 (ethanoic acid) N ϩ H3 ϫ Ϫ3 Alanine CHCH3 2.344 (CO2H) 4.53 10 2.33 ϫ Ϫ10 9.868 (NH3) 1.36 10 9.71 CO2H ϩ Ϫ5 Aminobenzene NH3 4.601 2.51 ϫ 10 4.64 (aniline) ϪO SNϩ Ϫ4 4-Aminobenzenesulfonic acid 3 H3 3.232 5.86 ϫ 10 3.01 (sulfanilic acid) ϩ NH3 ϫ Ϫ3 2-Aminobenzoic acid 2.08 (CO2H) 8.3 10 2.01 ϫ Ϫ5 (anthranilic acid) 4.96 (NH3) 1.10 10 4.78 CO2H ϩ 2-Aminoethanethiol HSCH2CH2NH3 —— 8.21 (SH) (2-mercaptoethylamine) —— 10.73 (NH3) ϩ ϫ Ϫ10 2-Aminoethanol HOCH2CH2NH3 9.498 3.18 10 9.52 (ethanolamine) O H ϫ Ϫ5 4.70 (NH3) (20°) 2.0 10 4.74 2-Aminophenol Ϫ 9.97 (OH) (20°) 1.05 ϫ 10 10 9.87 ϩ NH3 ϩ ϫ Ϫ10 Ammonia NH4 9.245 5.69 10 9.26 N ϩ H3 N ϩ H2 ϫ Ϫ2 1.823 (CO2H) 1.50 10 2.03 CHCH CH CH NHC ϫ Ϫ9 Arginine 2 2 2 8.991 (NH3) 1.02 10 9.00 NH —— (NH2) —— (12.1) CO2H 2 O Ϫ 2.24 5.8 ϫ 10 3 2.15 Ϫ Arsenic acid HO As OH 6.96 1.10 ϫ 10 7 6.65 Ϫ (hydrogen arsenate) (11.50) 3.2 ϫ 10 12 (11.18) OH ϫ Ϫ10 Arsenious acid As(OH)3 9.29 5.1 10 9.14 (hydrogen arsenite) N ϩ O H3 Asparagine CHCH2CNH2 —— —— 2.16 (CO2H) —— —— 8.73 (NH3) CO2H *Each acid is written in its protonated form. -
Personal Care
HAIR CONDITIONERS SURFACTANTSS • Behenamidopropyl Dime- pholine Lactate • Acetamide MEA • Lauramidopropyl Betaine thylamine • Myristyl Trimethyl Ammo- • Acetamide MEA, Lactamide • Lauramidopropyl Hydroxysul- • Cocodimonium Hydroxy- nium Bromide MEA taine propyl Hydrolyzed Rice • Polymethacrylamidoprop- • Alkyl Dimethyl (C12-C18) • Lauramidopropylamine Oxide Protein yltrimonium Chloride Amine Oxide • Lauramine Oxide • Cocodimonium Hydroxy- • Polyquaternium-2 • Alkylpolyglucoside • Laureth-1 Phosphate propyl Hydrolyzed Silk • Polyquaternium-6 • Ammonium Laureth Sulfate • Laureth-11 Carboxylic Acid Protein • Polyquaternium-7 • Ammonium Lauryl Sulfate • Laureth-11, Myreth-11 • Cocodimonium Hydroxy- • Polyquaternium-74 • Ammonium Lauryl Sulfate, • Laureth-3 Phosphate propyl Hydrolyzed Wheat • PPG-3 Caprylyl Ether Ammonium Laureth Sulfate • Laureth-6 Carboxylic Acid Protein • Quaternium-79 Hydrolyzed • Babassuamidopropyl Betaine • Laureth-9 • Dimethicone Keratin • Behenamidopropyl Dimethyl- • Lauryl Betaine • Guar Hydroxypropyltrimo- • Quaternium-79 Hydrolyzed amine • Lauryl Glucoside nium Chloride Silk • Behenoyl PG-Trimonium • Lauryl Hydroxysultaine • Hydroxypropyl Guar • Sodium Lauroyl Glutamate Chloride • Lauryl Lactate Hydroxypropyltrimonium • Stearalkonium Chloride • Behenoyl PG-Trimonium Chlo- • Modified Oleamide DEA Chloride • Stearamidopropyl Dime- ride, Cetyl Alcohol • Oleamidopropyl Betaine • Isostearamidopropyl Eth- thylamine • Behentrimonium Chloride • Oleth-20, Ceteth-20 yldimonium Ethosulfate, • Sunflowerseedamidopro- • Capryl/Caprylic -
Experimental Study Into Carbon Dioxide Solubility and Species Distribution in Aqueous Alkanolamine Solutions
Air Pollution XX 515 Experimental study into carbon dioxide solubility and species distribution in aqueous alkanolamine solutions H. Yamada, T. Higashii, F. A. Chowdhury, K. Goto S. Kazama Research Institute of Innovative Technology for the Earth, Japan Abstract We investigated the solubility of CO2 in aqueous solutions of alkanolamines at 40C and 120C over CO2 partial pressures ranging from a few kPa to 100 kPa to evaluate the potential for CO2 capture from flue gas. CO2 capacities were compared between monoethanolamine, N-ethyl ethanolamine and N-isopropyl ethanolamine. Speciation analyses were conducted in the alkanolamine solutions 13 at different CO2 loadings by accurate quantitative C nuclear magnetic resonance spectroscopy. N-isopropyl ethanolamine showed a large capacity for CO2 because of the formation of bicarbonate. However, we also found that at a lower CO2 loading a significant amount of carbamate was present in the aqueous N-isopropyl ethanolamine solutions. Keywords: carbon capture, amine absorbent, CO2 solubility, vapour-liquid equilibrium, nuclear magnetic resonance. 1 Introduction Carbon capture and storage is of central importance for the reduction of anthropogenic CO2 emissions in the atmosphere. Amine scrubbing is the most promising and currently applicable technology used in an industrial scale for the capture of CO2 from a gas stream [1]. To maximise the capture efficiency and to reduce energy costs we previously developed CO2 capture systems and high performance CO2 absorbents [2–5]. Recently, we demonstrated that hindered amino alcohols for the promotion of CO2 capture can be developed by rational molecular design and by the placement of functional groups [4, 5]. For aqueous solutions of primary and secondary amines the CO2 absorption proceeds by the formation of a carbamate anion or a bicarbonate anion. -
Ethanolamines Storage Guide Dow Manufactures Ethanolamines for A
DSA9782.qxd 1/29/03 2:34 PM Page 1 DSA9782.qxd 1/29/03 2:34 PM Page 2 DSA9782.qxd 1/29/03 2:34 PM Page 3 Contents PAGE Introduction 2 Product Characteristics 3 Occupational Health 3 Reactivity 3 Oxidation 4 Liquid Thermal Stability 4 Materials of Construction 5 Pure Ethanolamines 5 Aqueous Ethanolamines 6 Gaskets and Elastomers 7 Transfer Hose 8 Preparation for Service 9 Thermal Insulation Materials 10 Typical Storage System 11 Tank and Line Heating 11 Drum Thawing 11 Special Considerations 14 Vent Freezing 14 Color Buildup in Traced Pipelines 14 Thermal Relief for Traced Lines 14 Product Unloading 15 Unloading System 15 Shipping Vessel Descriptions 16 General Unloading Procedure 17 Product Handling 18 Personal Protective Equipment 18 Firefighting 18 Equipment Cleanup 18 Product Shipment 19 Environmental Considerations 19 Product Safety 20 1 DSA9782.qxd 1/29/03 2:34 PM Page 4 Ethanolamines Storage and Handling The Dow Chemical Company manufactures high-quality ethanolamines for a wide variety of end uses. Proper storage and handling will help maintain the high quality of these products as they are delivered to you. This will enhance your ability to use these products safely in your processes and maximize performance in your finished products. Ethanolamines have unique reactivity and solvent properties which make them useful as intermediates for a wide variety of applications. As a group, they are viscous, water-soluble liquids. In their pure, as-delivered state, these materials are chemically stable and are not corrosive to the proper containers. Ethanolamines can freeze at ambient temperatures. -
BETADET® BETADET® Anionic-Based Formulations
BETADET® S-20 BETADET® SHR VERY MILD SURFACTANT GREAT FORMULATION STABILITY ENHANCED FOAM VOLUME IMPROVED THICKENING EFFECT SULTAINES: MILD AMPHOTERIC SURFACTANTS FOR PERSONAL CARE KAO SURFACTANTS TECHNOLOGY AT YOUR SERVICE BETADET® S-20 & BETADET® SHR Foam, Viscosity & Mildness enhancers CHARACTERISTICS BETADET® S-20 and BETADET® SHR are recom- pH’s thus allowing their use in cosmetics formulations mended as secondary surfactants for very mild were alkali (i.e. depilatories) or acid media are neces- and high foaming products, achieving higher foam sary. Both products are also very stable to hard water, BETADET® S-20 and BETADET® volumes than alkyl betaines or alkyl amidopropyl improving the behavior of some sensitive anionic MAIN FEATURES betaines. These products are easier to thicken surfactants under extreme conditions. Additionally, SHR are very mild co-surfactants when combined with SLES, thus reducing the BETADET® S-20 shows a highlighted ability to reduce • Vegetable origin for personal care formulations. amount of electrolytes needed to obtain a desired the freezing point of final formulations making them • Preservative-free viscosity compared to other amphoteric surfactants. more stable at low temperatures, which helps to ob- Hydroxysultaines are highly effective amphoteric • Biodegradable Hydroxysultaines show excellent stability at extreme tain clear stable final products. Surfactants that improve the performance of final • Compatible with anionic, non-ionic and cationic cosmetic products. They are extremely mild cosur- surfactants -
Locating and Estimating Sources of Ethylene Oxide
United States Office of Air Quality EPA-450/4-84-007L Environmental Protection Planning And Standards Agency Research Triangle Park, NC 27711 September 1986 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF ETHYLENE OXIDE L &E EPA- 450/4-84-007L September 1986 LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF ETHYLENE OXIDE U.S. Environmental Protection Agency Office of Air and Radiation Office of Air Quality Planning and Standards Research Triangle Park, North Carolina 27711 This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and approved for publication as received from the contractor. Approval does not signify that the contents necessarily reflect the views and policies of the Agency, neither does mention of trade names or commercial products constitute endorsement or recommendation for use. EPA - 450/4-84-007L TABLE OF CONTENTS Section Page 1 Purpose of Document .......................................... 1 2 Overview of Document Contents ................................ 3 3 Background ................................................... 5 Nature of Pollutant .................................... 5 Overview of Production and Use ......................... 7 References for Section 3 .............................. 14 4 Emissions from Ethylene Oxide Production .................... 16 Ethylene Oxide Production ................................... 16 References for Section 4 .................................... 33 5 Emissions from Industries Which Use Ethylene -
Experimental Solubility of Carbon Dioxide in Monoethanolamine, Or
Experimental solubility of carbon dioxide in monoethanolamine, or diethanolamine or N-methyldiethanolamine (30 wt%) dissolved in deep eutectic solvent (choline chloride and ethylene glycol solution) Mohammed-Ridha Mahi, Ilham Mokbel, Latifa Negadi, Fatiha Dergal, Jacques Jose To cite this version: Mohammed-Ridha Mahi, Ilham Mokbel, Latifa Negadi, Fatiha Dergal, Jacques Jose. Experimen- tal solubility of carbon dioxide in monoethanolamine, or diethanolamine or N-methyldiethanolamine (30 wt%) dissolved in deep eutectic solvent (choline chloride and ethylene glycol solution). Journal of Molecular Liquids, Elsevier, 2019, 289, pp.111062. 10.1016/j.molliq.2019.111062. hal-02325445 HAL Id: hal-02325445 https://hal.archives-ouvertes.fr/hal-02325445 Submitted on 27 Apr 2021 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. Version of Record: https://www.sciencedirect.com/science/article/pii/S0167732219309687 Manuscript_b1cac4d1705988e9c9c303e3ba8c62e9 1 Experimental solubility of carbon dioxide in monoethanolamine, or 2 diethanolamine or N-methyldiethanolamine -
Study of Reactive Oxygen Species (ROS) and Nitric Oxide (NO) As Molecular Mediators of the Sepsis-Induced Diaphragmatic Contractile Dysfunction
Study of reactive oxygen species (ROS) and nitric oxide (NO) as molecular mediators of the sepsis-induced diaphragmatic contractile dysfunction. Protective effect of heme oxygenases Esther Barreiro Portela Department of Experimental Sciences and Health Universitat Pompeu Fabra Barcelona, Catalonia, Spain March 2002 Dipòsit legal: B. 36319-2003 ISBN: 84-688-3012-7 Esther Barreiro Portela 2002 UNIVERSITAT POMPEU FABRA DEPARTMENT DE CIÈNCIES EXPERIMENTALS I DE LA SALUT AREA DE CONEIXEMENT DE FISIOLOGIA POMPEU FABRA UNIVERSITY DEPARTMENT OF EXPERIMENTAL SCIENCES AND HEALTH PHYSIOLOGY DOCTORAL THESIS STUDY OF REACTIVE OXYGEN SPECIES (ROS) AND NITRIC OXIDE (NO) AS MOLECULAR MEDIATORS OF THE SEPSIS-INDUCED DIAPHRAGMATIC CONTRACTILE DYSFUNCTION. PROTECTIVE EFFECT OF HEME OXYGENASES Thesis presented by: Esther Barreiro Portela Medical Doctor Specialized in Respiratory Medicine Thesis director: Dr. Sabah N.A. Hussain, MD, PhD Critical Care and Respiratory Divisions, Royal Victoria Hospital Associate Professor, McGill University Montreal, Quebec, Canada CEXS Supervision: Dr. Joaquim Gea Guiral, MD, PhD Servei de Pneumologia Hospital del Mar-IMIM CEXS, Universitat Pompeu Fabra Barcelona, Catalonia, Spain March, 2002 Doctoral Thesis ABSTRACT Nitric oxide (NO) and reactive oxygen species (ROS) are constitutively synthesized in skeletal muscle, and they are produced in large quantities during active inflammatory processes such as in sepsis. These molecules modulate skeletal muscle contractility in both normal and septic muscles. Modification of tyrosine residues and formation of 3-nitrotyrosine is the most commonly studied covalent modification of proteins attributed to NO. Heme oxygenases (HOs), the rate limiting enzymes in heme catabolism, have been shown to exert protective effects against oxidative stress in several type tissues. We evaluated the involvement of NO synthases (NOS) and HOs in nitrosative and oxidative stresses in sepsis-induced diaphragmatic contractile dysfunction. -
Diethanolamine
DIETHANOLAMINE 1. Exposure Data 1.1 Chemical and physical data 1.1.1 Nomenclature Chem. Abstr. Serv. Reg. No.: 111-42-2 Deleted CAS Reg. No.: 8033-73-6 Chem. Abstr. Name: 2,2′-Iminobis[ethanol] IUPAC Systematic Name: 2,2′-Iminodiethanol Synonyms: Bis(hydroxyethyl)amine; bis(2-hydroxyethyl)amine; N,N-bis(2- hydroxyethyl)amine; DEA; N,N-diethanolamine; 2,2′-dihydroxydiethylamine; di- (β-hydroxyethyl)amine; di(2-hydroxyethyl)amine; diolamine; 2-(2-hydroxyethyl- amino)ethanol; iminodiethanol; N,N′-iminodiethanol; 2,2′-iminodi-1-ethanol 1.1.2 Structural and molecular formulae and relative molecular mass CH2 CH2 OH H N CH2 CH2 OH C4H11NO2 Relative molecular mass: 105.14 1.1.3 Chemical and physical properties of the pure substance (a) Description: Deliquescent prisms; colourless, viscous liquid with a mild ammonia odour (Budavari, 1998; Dow Chemical Company, 1999) (b) Boiling-point: 268.8 °C (Lide & Milne, 1996) (c) Melting-point: 28 °C (Lide & Milne, 1996) (d) Density: 1.0966 g/cm3 at 20 °C (Lide & Milne, 1996) (e) Spectroscopy data: Infrared (proton [5830]; grating [33038]), nuclear magnetic resonance (proton [6575]; C-13 [2936]) and mass spectral data have been reported (Sadtler Research Laboratories, 1980; Lide & Milne, 1996) (f) Solubility: Very soluble in water (954 g/L) and ethanol; slightly soluble in benzene and diethyl ether (Lide & Milne, 1996; Verschueren, 1996) –349– 350 IARC MONOGRAPHS VOLUME 77 (g) Volatility: Vapour pressure, < 0.01 mm Hg [1.33 Pa] at 20 °C; relative vapour density (air = 1), 3.6; flash-point, 149 °C (Verschueren, 1996) (h) Stability: Incompatible with some metals, halogenated organics, nitrites, strong acids and strong oxidizers (Dow Chemical Company, 1999) (i) Octanol/water partition coefficient (P): log P, –2.18 (Verschueren, 1996) (j) Conversion factor1: mg/m3 = 4.30 × ppm 1.1.4 Technical products and impurities Diethanolamine is commercially available with the following specifications: purity, 99.3% min.; monoethanolamine, 0.45% max.; triethanolamine (see monograph in this volume), 0.25% max.; and water content, 0.15% max. -
Degradation of Amine-Based Solvents in CO2 Capture Process by Chemical Absorption
CORE Metadata, citation and similar papers at core.ac.uk Provided by Heriot Watt Pure Degradation of amine-based solvents in CO2 capture process by chemical absorption F. Vega1, 2, A. Sanna2, B. Navarrete1, M.M. Maroto-Valer2, V. Cortés1 1Chemical and Environmental Engineering Department, School of Engineering, University of Seville, C/ Camino de los Descubrimientos s/n 41092 Sevilla, Spain, Phone: 954481397, [email protected] 2Centre for Innovation in Carbon Capture and Storage (CICCS), School of Engineering and Physical Sciences, Heriot-Watt University, EH14 4AS, Edinburgh, UK ABSTRACT Carbon dioxide capture and storage (CCS) technologies have been proposed as promising alternative to reduce CO2 emissions from fossil-fuel power plants with post- combustion capture. Absorption by aqueous amine-solutions is considered the most mature and industrially developed technology for post-combustion capture. One of the most significant issues hindering a large deployment of this technology is potential amine degradation. Amines degrade in presence of O2, CO2, NOx, SO2 and heat resulting in solvent loss, equipment corrosion and generation of volatile degradation compounds. Two types of degradation have been identified in the literature, namely oxidative and thermal degradation. A review of the amine-based solvents, its main degradation products, the apparatus and analytical methods most widely used, as well as the mechanism proposed and kinetic studies are presented and discussed here. Moreover, amines emissions from CO2 capture units can react in the atmosphere via photo-oxidation and also via NOX reactions to give nitrosamines and nitramines, which are potentially harmful to the human health and the environment. A discussion of the recent works on atmospheric degradation of amine solvents is also included in this review.