Experimental Solubility of Carbon Dioxide in Monoethanolamine, Or
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Measurement of CO2 Solubility in Amine Based Deep Eutectic Solvents
International Journal of Environmental Science and Development, Vol. 11, No. 9, September 2020 Measurement of CO2 Solubility in Amine Based Deep Eutectic Solvents Khatereh Ali Pishro, Ghulam Murshid, Farouq Sabri Mjalli, and Jamil Naser loading capacity range 0.5-1 mole of CO2 per mole of amine, Abstract—The climate change assumes the warming of the and the reaction of CO2 with tertiary amines such as climate systems due to increase of global average temperature N-methyldiethanolamine (MDEA) and Sterically hindered to the observed increase of the greenhouse gas (GHG) amines occur with higher loading capacity of 1 mol of CO2 concentration in the atmosphere. Carbon dioxide (CO2) is per mole of amine [4]. considered the most important GHG. The processes of CO2 capture are gaining a great attention on the scientific Furthermore, Deep eutectic solvents (DES) prepared by community as an alternative for decreasing CO2 emission and mixing of two or more solvents to form a eutectic with reducing its concentration in ambient air. In this study, we melting point lower than the individual components [5]. report a new deep eutectic solvents (DESs) made of DESs have noticeable advantages such as simple synthesis, monoethanolamine hydrochloride-diethylenetriamine exhibits lower ingredients cost, and biodegradable nature. Although, a great candidate for CO2 capture. We developed solubility and physical properties studies at different pressures and many researches carried on study of DESs for CO2 capture, temperatures, and regression model was well in agreement with there are still a little report on CO2 absorption study by amine the calculated αCO2 values with R-square: 0.976. -
Exfoliation of Graphite with Deep Eutectic Solvents
(19) TZZ¥ZZ_T (11) EP 3 050 844 A1 (12) EUROPEAN PATENT APPLICATION published in accordance with Art. 153(4) EPC (43) Date of publication: (51) Int Cl.: 03.08.2016 Bulletin 2016/31 C01B 31/00 (2006.01) B82Y 30/00 (2011.01) (21) Application number: 14849900.7 (86) International application number: PCT/ES2014/070652 (22) Date of filing: 12.08.2014 (87) International publication number: WO 2015/044478 (02.04.2015 Gazette 2015/13) (84) Designated Contracting States: (72) Inventors: AL AT BE BG CH CY CZ DE DK EE ES FI FR GB • DE MIGUEL TURULLOIS, Irene GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO 28006 Madrid (ES) PL PT RO RS SE SI SK SM TR • HERRADÓN GARCÍA, Bernardo Designated Extension States: 28006 Madrid (ES) BA ME • MANN MORALES, Enrique Alejandro 28006 Madrid (ES) (30) Priority: 24.09.2013 ES 201331382 • MORALES BERGAS, Enrique 28006 Madrid (ES) (71) Applicant: Consejo Superior de Investigaciones Cientificas (74) Representative: Cueto, Sénida (CSIC) SP3 Patents S.L. 28006 Madrid (ES) Los Madroños, 23 28891 Velilla de San Antonio (ES) (54) EXFOLIATION OF GRAPHITE WITH DEEP EUTECTIC SOLVENTS (57) The invention relate to graphite materials, and more specifically to the exfoliation of graphite using deep eutectic solvents, to methods related thereto, to polymer- ic composite materials containing graphene and the methodsfor the production thereof, andto graphene/met- al, exfoliated graphite/metal, graphene/metal oxide and exfoliated graphite/metal oxide composite materials and the methods for the production thereof. EP 3 050 844 A1 Printed by Jouve, 75001 PARIS (FR) EP 3 050 844 A1 Description Field of the Invention 5 [0001] The present invention relates to graphitic materials, and more specifically to exfoliation of graphite using deep eutectic solvents, methods related to it, polymeric composites with exfoliated graphite/graphene, composites graph- ene/metal, exfoliated graphite/metal, graphene/metal oxide and exfoliated graphite/metal oxide, and methods for their preparation. -
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 -
Effect of Hydrogen Bond Donors and Acceptors on CO2 Absorption By
processes Article Effect of Hydrogen Bond Donors and Acceptors on CO2 Absorption by Deep Eutectic Solvents Tausif Altamash 1, Abdulkarem Amhamed 1 , Santiago Aparicio 2,* and Mert Atilhan 3,* 1 Qatar Environment & Energy Research Institute, Hamad Bin Khalifa University, Doha 34110, Qatar; [email protected] (T.A.); [email protected] (A.A.) 2 Department of Chemistry, University of Burgos, 09001 Burgos, Spain 3 Department of Chemical and Paper engineering, Western Michigan University, Kalamazoo, MI 49008, USA * Correspondence: [email protected] (S.A.); [email protected] (M.A.) Received: 7 November 2020; Accepted: 22 November 2020; Published: 25 November 2020 Abstract: The effects of a hydrogen bond acceptor and hydrogen bond donor on carbon dioxide absorption via natural deep eutectic solvents were studied in this work. Naturally occurring non-toxic deep eutectic solvent constituents were considered; choline chloride, b-alanine, and betaine were selected as hydrogen bond acceptors; lactic acid, malic acid, and fructose were selected as hydrogen bond donors. Experimental gas absorption data were collected via experimental methods that uses gravimetric principles. Carbon dioxide capture data for an isolated hydrogen bond donor and hydrogen bond acceptor, as well as natural deep eutectic solvents, were collected. In addition to experimental data, a theoretical study using Density Functional Theory was carried out to analyze the properties of these fluids from the nanoscopic viewpoint and their relationship with the macroscopic behavior of the system, and its ability for carbon dioxide absorption. The combined experimental and theoretical reported approach work leads to valuable discussions on what is the effect of each hydrogen bond donor or acceptor, as well as how they influence the strength and stability of the carbon dioxide absorption in deep eutectic solvents. -
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]. -
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. -
Cellulose Cosolvent Huy Vu Duc Nguyen, Renko De Vries, and Simeon D
This is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License, which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes. pubs.acs.org/journal/ascecg Research Article Natural Deep Eutectics as a “Green” Cellulose Cosolvent Huy Vu Duc Nguyen, Renko De Vries, and Simeon D. Stoyanov* Cite This: ACS Sustainable Chem. Eng. 2020, 8, 14166−14178 Read Online ACCESS Metrics & More Article Recommendations *sı Supporting Information ABSTRACT: In this study, we report a novel, green chemistry approach for creating new cellulose solvents based on a mixture of a natural deep eutectic solvent (NADES) and a primary cellulose solvent. Because of the strong hydrogen-bond donor and acceptor ability of both the NADES and the primary cellulose solvent, the new mixed system is a cellulose solvent, with an improved cellulose dissolution capacity. We believe that this is a generic approach to prepare an entirely new class of green solvent, capable of dissolving cellulose under mild conditions. This in turn will facilitate the creation of a large amount of new cellulose-based (soft) materials. To illustrate our approach, we show that a NADES based on choline chloride + malic acid can be used as cosolvent for the industrial cellulose solvent N-methylmorpholine-N-oxide mono- hydrate (NMMO). The new mixed cellulose solvent system has improved cellulose dissolution capacity and has a much broader processing window, which allows working with dissolved cellulose at ambient temperatures, far below 70 °C, where NNMO monohydrate will solidify. This, in turn, can not only help to address the thermal instability issue of pure NMMO when processed at elevated temperatures, but also expands the working conditions of the lyocell process. -
WO 2015/019093 Al 12 February 2015 (12.02.2015) 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 2015/019093 Al 12 February 2015 (12.02.2015) P O P C T (51) International Patent Classification: AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, C25B 1/00 (2006.01) C01B 31/04 (2006.01) BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DK, DM, DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, (21) International Application Number: HN, HR, HU, ID, IL, IN, IR, IS, JP, KE, KG, KN, KP, KR, PCT/GB20 14/0524 16 KZ, LA, LC, LK, LR, LS, LT, LU, LY, MA, MD, ME, (22) International Filing Date: MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, 6 August 2014 (06.08.2014) OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, (25) Filing Language: English TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, (26) Publication Language: English ZW. (30) Priority Data: (84) Designated States (unless otherwise indicated, for every 13 14084.3 6 August 2013 (06.08.2013) GB kind of regional protection available): ARIPO (BW, GH, GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, SZ, TZ, (71) Applicant: THE UNIVERSITY OF MANCHESTER UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, TJ, [GB/GB]; Oxford Road, Manchester, Greater Manchester, TM), European (AL, AT, BE, BG, CH, CY, CZ, DE, DK, M l 3 9PL (GB). -
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 -
Glycerol Hydrogen-Bonding Network Dominates Structure and Collective Dynamics in a Deep Eutectic Solvent † ‡ ‡ § ⊥ # # A
Article Cite This: J. Phys. Chem. B 2018, 122, 1261−1267 pubs.acs.org/JPCB Glycerol Hydrogen-Bonding Network Dominates Structure and Collective Dynamics in a Deep Eutectic Solvent † ‡ ‡ § ⊥ # # A. Faraone,*, D. V. Wagle, G. A. Baker,*, E. C. Novak, M. Ohl, D. Reuter, P. Lunkenheimer, # ∥ A. Loidl, and E. Mamontov*, † NIST Center for Neutron Research, National Institute of Standards and Technology Gaithersburg, Gaithersburg, Maryland 20899, United States ‡ Department of Chemistry, University of Missouri-Columbia, Columbia, Missouri 65211, United States § Department of Materials Science and Engineering, University of Tennessee, Knoxville, Tennessee 37996, United States ∥ Neutron Scattering Division, Neutron Sciences Directorate, Oak Ridge National Laboratory, Oak Ridge, Tennessee 37831, United States ⊥ Jülich Center for Neutron Science, Forschungszentrum Jülich GmbH, Jülich 52425, Germany # Experimental Physics V, Center for Electronic Correlations and Magnetism, University of Augsburg, Augsburg 86159, Germany *S Supporting Information ABSTRACT: The deep eutectic solvent glyceline formed by choline chloride and glycerol in 1:2 molar ratio is much less viscous compared to glycerol, which facilitates its use in many applications where high viscosity is undesirable. Despite the large difference in viscosity, we have found that the structural network of glyceline is completely defined by its glycerol constituent, which exhibits complex microscopic dynamic behavior, as expected from a highly correlated hydrogen- bonding network. Choline ions occupy interstitial voids in the glycerol network and show little structural or dynamic correlations with glycerol molecules. Despite the known higher long-range diffusivity of the smaller glycerol species in glyceline, in applications where localized dynamics is essential (e.g., in microporous media), the local transport and dynamic properties must be dominated by the relatively loosely bound choline ions. -
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.