Locating and Estimating Air Emissions from Sources of Chloroform
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Enagás' CH4 Emissions Reporting, Mitigation and Commitment
Enagás’ CH4 emissions reporting, mitigation and commitment Initial condition Enagás is a midstream company. It is a leading natural gas infrastructure company in Spain and the Technical Manager of the Spanish gas system. The company's activities include the management, operation and maintenance of gas infrastructure. In Spain Enagás has approximately 12,000 km of gas pipelines, 19 compressor stations, 493 regulation and metering stations, and 3 underground storage facilities. It also owns 4 LNG regasification plants, and it is the main shareholder of other two. Traditionally, Enagás managed methane emissions predominantly from the safety requirements perspective. However, as energy efficiency and GHG emissions reduction have become strategic priorities for the company, emissions of methane, being a potent short-lived climate pollutant, came to the forefront. The most relevant aspects addressed by Enagás in its climate change management model are: public commitment and the setting of targets, emissions reduction and compensation measures, as well as reporting on performance and results, following TCFD1 recommendations. Since 2013, the company voluntarily started to annually calculate and verify its Carbon Footprint, which constitutes the base for its emission reduction strategy. Quantification of methane emissions is a part of that process, which is subject to an independent third-party verification in accordance with standard ISO 14064. Process: the role of leaks detection and repair Methane emissions account for approximately 20% of Enagás’ greenhouse gas emissions (scope 1 and 2). 70% of these are fugitive methane emissions while the remainder (30%) is primary caused by safety precautions, or by design of equipment (vents). Due to the relatively large share of fugitive emissions, in 2013 Enagás started to carry out leak detection and repair campaigns (LDAR). -
Hydrogen and Carbon Isotope Fractionation During Degradation Of
ORIGINAL RESEARCH Hydrogen and carbon isotope fractionation during degradation of chloromethane by methylotrophic bacteria Thierry Nadalig1, Markus Greule2, Francßoise Bringel1,Stephane Vuilleumier1 & Frank Keppler2 1Equipe Adaptations et Interactions Microbiennes dans l’Environnement, UMR 7156 Universite de Strasbourg - CNRS, 28 rue Goethe, Strasbourg, 67083, France 2Max Planck Institute for Chemistry, Hahn-Meitner-Weg 1, 55128 Mainz, Germany Keywords Abstract Carbon isotope fractionation, chloromethane biodegradation, hydrogen isotope Chloromethane (CH3Cl) is a widely studied volatile halocarbon involved in the fractionation, methylotrophic bacteria. destruction of ozone in the stratosphere. Nevertheless, its global budget still remains debated. Stable isotope analysis is a powerful tool to constrain fluxes Correspondence of chloromethane between various environmental compartments which involve Thierry Nadalig, Universite de Strasbourg, a multiplicity of sources and sinks, and both biotic and abiotic processes. In UMR 7156 UdS-CNRS, 28 rue Goethe, this study, we measured hydrogen and carbon isotope fractionation of the 67083 Strasbourg Cedex, France. Tel: +33 3 68851973; Fax: +33 3 68852028; remaining untransformed chloromethane following its degradation by methylo- Methylobacterium extorquens Hyphomicrobium E-mail: [email protected] trophic bacterial strains CM4 and sp. MC1, which belong to different genera but both use the cmu pathway, the Funding Information only pathway for bacterial degradation of chloromethane characterized so far. Financial support for the acquisition of Hydrogen isotope fractionation for degradation of chloromethane was deter- GC-FID equipment by REALISE (http://realise. mined for the first time, and yielded enrichment factors (e)ofÀ29& and unistra.fr), the Alsace network for research À27& for strains CM4 and MC1, respectively. In agreement with previous and engineering in environmental sciences, is studies, enrichment in 13C of untransformed CH Cl was also observed, and gratefully acknowledged. -
Effect of Insulations on Cop in Vapor Compression Refrigeration System
International Journal of Mechanical Engineering and Technology (IJMET) Volume 10, Issue 01, January 2019, pp. 1201-1208, Article ID: IJMET_10_01_122 Available online at http://www.iaeme.com/ijmet/issues.asp?JType=IJMET&VType=10&IType= 01 ISSN Print: 0976-6340 and ISSN Online: 0976-6359 © IAEME Publication Scopus Indexed EFFECT OF INSULATIONS ON COP IN VAPOR COMPRESSION REFRIGERATION SYSTEM Anusha Peyyala Assistant Professor P V P Siddhartha Institute of Technology, Research Scholar, Acharya Nagarjuna University, India. Dr N V V S Sudheer Associate Professor, R V R & J C College of Engineering, Guntur India ABSTRACT In this project, experimentation is done on Vapour Compression Refrigeration System [VCRS] as the COP is high for this system and it is the present trend of the HVAC in the domestic industry. This study presents investigation of best suited refrigerant and insulation combination for gas pipeline and liquid pipeline of a split air conditioning system. Analysis are performed for R22-Chlorodiflouromethane, a HydroChloroFlouro Carbon refrigerant, which has been using in the present world that cause both global warming and ozone layer depletion and R410a, mixture of di- flouromethane and pentaflouroethane, a Hydroflouro carbon refrigerant, which is future of HVAC which reduces the effect of ozone layer depletion [ODP] and Global Warming Potential [GWP].For these two refrigerants, we had found out the best insulation suitable as insulation also affects the COP of air conditioner, which has been observed from the literature. Minimizing the temperature of refrigerant in suction line helps condensing unit work more effectively intern the system performance increases. This reduces the overall power required for working of air conditioner, thereby reducing the maintenance cost of system. -
New and Improved Infrared Absorption Cross Sections for Chlorodifluoromethane (HCFC-22)
Atmos. Meas. Tech., 9, 2593–2601, 2016 www.atmos-meas-tech.net/9/2593/2016/ doi:10.5194/amt-9-2593-2016 © Author(s) 2016. CC Attribution 3.0 License. New and improved infrared absorption cross sections for chlorodifluoromethane (HCFC-22) Jeremy J. Harrison1,2 1Department of Physics and Astronomy, University of Leicester, University Road, Leicester, LE1 7RH, UK 2National Centre for Earth Observation, University of Leicester, University Road, Leicester, LE1 7RH, UK Correspondence to: Jeremy J. Harrison ([email protected]) Received: 10 December 2015 – Published in Atmos. Meas. Tech. Discuss.: 18 January 2016 Revised: 3 May 2016 – Accepted: 6 May 2016 – Published: 17 June 2016 Abstract. The most widely used hydrochlorofluorocarbon 1 Introduction (HCFC) commercially since the 1930s has been chloro- difluoromethane, or HCFC-22, which has the undesirable The consumer appetite for safe household refrigeration led effect of depleting stratospheric ozone. As this molecule to the commercialisation in the 1930s of dichlorodifluo- is currently being phased out under the Montreal Pro- romethane, or CFC-12, a non-flammable and non-toxic re- tocol, monitoring its concentration profiles using infrared frigerant (Myers, 2007). Within the next few decades, other sounders crucially requires accurate laboratory spectroscopic chemically related refrigerants were additionally commer- data. This work describes new high-resolution infrared ab- cialised, including chlorodifluoromethane, or a hydrochlo- sorption cross sections of chlorodifluoromethane over the rofluorocarbon known as HCFC-22, which found use in a spectral range 730–1380 cm−1, determined from spectra wide array of applications such as air conditioners, chillers, recorded using a high-resolution Fourier transform spectrom- and refrigeration for food retail and industrial processes. -
Billing Code: 3510-Ds-P Department Of
This document is scheduled to be published in the Federal Register on 01/30/2015 and available online at http://federalregister.gov/a/2015-01795, and on FDsys.gov BILLING CODE: 3510-DS-P DEPARTMENT OF COMMERCE International Trade Administration C-570-009 Calcium Hypochlorite from the People’s Republic of China: Countervailing Duty Order AGENCY: Enforcement and Compliance, International Trade Administration, Department of Commerce SUMMARY: Based on affirmative final determinations by the Department of Commerce (“Department”) and the International Trade Commission (“ITC”), the Department is issuing a countervailing duty order on calcium hypochlorite from the People’s Republic of China (“PRC”). EFFECTIVE DATE: [(Insert date of publication in the Federal Register]. FOR FURTHER INFORMATION CONTACT: Katie Marksberry, AD/CVD Operations, Office V, Enforcement and Compliance, International Trade Administration, U.S. Department of Commerce, 14th Street and Constitution Avenue, NW, Washington, DC 20230; telephone: (202) 482-7906. SUPPLEMENTARY INFORMATION: Background In accordance with section 705(d) of the Tariff Act of 1930, as amended (“the Act”), on December 15, 2014, the Department published its final determination that countervailable subsidies are being provided to producers and exporters of calcium hypochlorite from the PRC.1 On January 21, 2015, the ITC notified the Department of its final determination pursuant to 1 See Calcium Hypochlorite from the People’s Republic of China: Final Affirmative Countervailing Duty Determination; 79 FR -
THE JOURNAL of INDUSTRIAL and ENGINEERING CHEMISTRY 953 with Stirring, and the Flask Allowed to Stand
OCt., 1917 THE JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY 953 with stirring, and the flask allowed to stand. The ascertaining the presence of aniline, the calcium hypo- solution, when the precipitate has settled, is filtered chlorite test is employed. The quantitative deter- through a Gooch crucible, using a bell jar arrangement, mination is carried out by precipitating the aniline into a 250 to 300 cc. Erlenmeyer flask. The crucible as tribromoaniline with bromine water. The precipi- is fitted preferably with a small circular filter paper tate is caught on a tared filter paper, dried in vacuo, (cut to size) instead of asbestos. The flask should be and weighed. washed with wash-ether (100parts absolute ether and In this connection, it occurred to the writer that it 2 parts alcoholic HC1) while filtering so as not to allow might be possible to work out, for estimating the any ferric chloride to dry on the white precipitate or aniline, a colorimetric method based on the qualita- on the crucible. The usual precautions of washing the tive test with hypochlorite. If this were possible, flask, crucible and funnel are taken to insure complete it certainly would be desirable, for not only would transfer of iron. It is not necessary, however, to trans- considerable time and effort be saved but probably fer all of the aluminum chloride precipitate to the a considerably smaller sample than IO liters would be Gooch crucible. The aluminum precipitate is removed sufficient and quantitative measurements could also with the paper from the crucible by tapping it into a be applied in cases where the amount of aniline in 25 cc. -
Biodiesel Handling and Use Guide (Fifth Edition)
Biodiesel Handling and Use Guide (Fifth Edition) DOE/GO-102016-4875 November 2016 Disclaimer 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 agen- cy 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. Every effort has been made to ensure that this manual is accurate, complete, and compre- hensive at the time of publication. It is intended to be used as a guide and resource docu- ment. The authors strongly encourage all parties with an interest in establishing E85 or other ethanol blends fueling systems to engage professional support during installation to ensure fuel integrity and systems compatibility. This document is not intended for use as a “how to” guide for individuals or organizations performing conversions. Report Contributors and Roles Lead Authors Teresa L. Alleman and Robert L. McCormick, National Renewable Energy Laboratory Contributing Authors Earl D. Christensen, Gina Fioroni, and Kristi Moriarty, National Renewable Energy Laboratory Janet Yanowitz, EcoEngineering Contents Introduction............................................................ -
SAFETY DATA SHEET Chlorodifluoromethane (R 22) Issue Date: 16.01.2013 Version: 1.0 SDS No.: 000010021746 Last Revised Date: 18.06.2015 1/15
SAFETY DATA SHEET Chlorodifluoromethane (R 22) Issue Date: 16.01.2013 Version: 1.0 SDS No.: 000010021746 Last revised date: 18.06.2015 1/15 SECTION 1: Identification of the substance/mixture and of the company/undertaking 1.1 Product identifier Product name: Chlorodifluoromethane (R 22) Trade name: Gasart 503 R22 Additional identification Chemical name: Chlorodifluoromethane Chemical formula: CHClF2 INDEX No. - CAS-No. 75-45-6 EC No. 200-871-9 REACH Registration No. 01-2119517587-31 1.2 Relevant identified uses of the substance or mixture and uses advised against Identified uses: Industrial and professional. Perform risk assessment prior to use. Refrigerant. Using gas alone or in mixtures for the calibration of analysis equipment. Using gas as feedstock in chemical processes. Formulation of mixtures with gas in pressure receptacles. Uses advised against Consumer use. 1.3 Details of the supplier of the safety data sheet Supplier Linde Gas GmbH Telephone: +43 50 4273 Carl-von-Linde-Platz 1 A-4651 Stadl-Paura E-mail: [email protected] 1.4 Emergency telephone number: Emergency number Linde: + 43 50 4273 (during business hours), Poisoning Information Center: +43 1 406 43 43 SDS_AT - 000010021746 SAFETY DATA SHEET Chlorodifluoromethane (R 22) Issue Date: 16.01.2013 Version: 1.0 SDS No.: 000010021746 Last revised date: 18.06.2015 2/15 SECTION 2: Hazards identification 2.1 Classification of the substance or mixture Classification according to Directive 67/548/EEC or 1999/45/EC as amended. N; R59 The full text for all R-phrases is displayed in section 16. Classification according to Regulation (EC) No 1272/2008 as amended. -
UNITED STATES PATENT of FICE 2,640,086 PROCESS for SEPARATING HYDROGEN FLUORIDE from CHLORODFLUORO METHANE Robert H
Patented May 26, 1953 2,640,086 UNITED STATES PATENT of FICE 2,640,086 PROCESS FOR SEPARATING HYDROGEN FLUORIDE FROM CHLORODFLUORO METHANE Robert H. Baldwin, Chadds Ford, Pa., assignor to E. H. du Pont de Nemours and Company, Wi inington, Del, a corporation of Delaware No Drawing. Application December 15, 1951, Serial No. 261,929 9 Claims. (C. 260-653) 2 This invention relates to a process for Sep These objects are accomplished essentially by arating hydrogen fluoride from monochlorodi Subjecting a mixture of hydrogen fluoride and fluoronethane, and more particularly, separat Inonochlorodifluoromethane in the liquid phase ing these components from the reaction mixture to temperatures below 0° C., preferably at about obtained in the fluorination of chloroform with -30° C. to -50° C., at either atmospheric or hydrogen fluoride, Super-atmospheric pressures, together with from In the fluorination of chloroform in the prest about 0.25 mol to about 2.5 mols of chloroform ence Of a Catalyst, a reaction mixture is pro per mol of chlorodifluoronethane contained in duced which consists essentially of HCl, HF, the mixture and separating an upper layer rich CHCIF2, CHCl2F, CHCls, and CHF3. A method O in HF from a lower organic layer. The proceSS of Separating these components is disclosed in is operative with mixtures containing up to 77% U. S. Patent No. 2,450,414 which involves sep by weight of HF. arating the components by a special fractional It has been found that chloroform is substan distillation under appropriate temperatures and tially immiscible With EIF at temperatures be pressures. -
Chloroform 18.08.2020.Pdf
Chloroform Chloroform, or trichloromethane, is an organic compound with formula CHCl3. It is a colorless, sweet-smelling, dense liquid that is produced on a large scale as a precursor to PTFE. It is also a precursor to various refrigerants. It is one of the four chloromethanes and a trihalomethane. It is a powerful anesthetic, euphoriant, anxiolytic and sedative when inhaled or ingested. Formula: CHCl₃ IUPAC ID: Trichloromethane Molar mass: 119.38 g/mol Boiling point: 61.2 °C Density: 1.49 g/cm³ Melting point: -63.5 °C The molecule adopts a tetrahedral molecular geometry with C3v symmetry. Chloroform volatilizes readily from soil and surface water and undergoes degradation in air to produce phosgene, dichloromethane, formyl chloride, carbon monoxide, carbon dioxide, and hydrogen chloride. Its half-life in air ranges from 55 to 620 days. Biodegradation in water and soil is slow. Chloroform does not significantly bioaccumulate in aquatic organisms. Production:- In industry production, chloroform is produced by heating a mixture of chlorine and either chloromethane (CH3Cl) or methane (CH4). At 400–500 °C, a free radical halogenation occurs, converting these precursors to progressively more chlorinated compounds: CH4 + Cl2 → CH3Cl + HCl CH3Cl + Cl2 → CH2Cl2 + HCl CH2Cl2 + Cl2 → CHCl3 + HCl Chloroform undergoes further chlorination to yield carbon tetrachloride (CCl4): CHCl3 + Cl2 → CCl4 + HCl The output of this process is a mixture of the four chloromethanes (chloromethane, dichloromethane, chloroform, and carbon tetrachloride), which can then be separated by distillation. Chloroform may also be produced on a small scale via the haloform reaction between acetone and sodium hypochlorite: 3 NaClO + (CH3)2CO → CHCl3 + 2 NaOH + CH3COONa Deuterochloroform[ Deuterated chloroform is an isotopologue of chloroform with a single deuterium atom. -
Epact Complementary Program Unconventional Resources Technical Advisory Committee Meeting
EPAct Complementary Program Unconventional Resources Technical Advisory Committee Meeting Alexandra Hakala Shale Gas Technical Coordinator, NETL-ORD September 19, 2013 National Energy Technology Laboratory Tech Transfer to Date: www.edx.netl.doe.gov/ucr 31 Conference Presentations 7 Published Articles & Reports • Additional manuscripts undergoing internal and external peer review 2 Datasets released via EDX 2 Data-driven tool/app via EDX Complementary Program Portfolio – UCR Fugitive Emission Factors and Air Emissions – Fugitive Air Emissions Field Data (2011 to present) – Greenhouse Gas Life Cycle Methane Emission Factor Assessment (2011 to 2012 -- completed) Produced Water and Waste Management – Predicting Compositions and Volumes of Produced Water (2011 to present) – Evaluation of the Geochemical and Microbiological Composition of Shale Gas Produced Water and Solid Wastes (2011 to present) – Biogeochemical Factors that Affect the Composition of Produced Waters and the Utility of Geochemical Tracer Tools (2011 to present) Subsurface Fluid and Gas Migration – Integrated Field Monitoring – Gas/Fluid Migration (2011 to present) – Gas Flow from Shallow Gas Formations (2012 to present) – Approach for Assessing Spatial Trends & Potential Risks with UCR Systems (2011 to present) – Impacts of Shale Gas Development on Shallow Groundwater (2012 to present) – Subsurface Gas and Fluid Migration Assessment (2011 to 2012 -- completed) – Develop a Suite of Naturally Occurring Geochemical Tracer Tools that Verify the Sources of Fluids in Complex Geologic -
What Does Science Tell Us About Fugitive Methane Emissions from Unconventional Gas?
www.csiro.au Fugitive emissions from unconventional gas What the latest scientific research is telling us about fugitive methane emissions from unconventional gas. July 2019 What does science tell us about fugitive methane emissions from unconventional gas? This factsheet sets out what the KEY POINTS science tells us about methane • Fugitive emissions are losses, leaks and other releases of methane to the atmosphere that emission sources from coal seam gas are associated with industries producing natural gas, oil and coal. They also include CO2 (CSG) wells, pipelines, compressors emissions associated with flaring of excess gas to the atmosphere. and other infrastructure associated • In Australia, fugitive emissions from oil and gas with CSG production; and their production are estimated to account for about 6.0% of greenhouse gas emissions. importance in contributing to • To accurately measure fugitive emissions, natural background biological and geological warming of the earth’s climate. sources must be separated from human sources. CSIRO studies aim to separate these sources. • CSIRO has a range of research programs What is methane and where does it come from? underway in Queensland, New South Wales, Methane, a colourless, odourless, non-toxic gas, originates from Western Australia and the Northern Territory two sources: using measuring and monitoring techniques, life-cycle analysis methods and industry activity • the decomposition of organic matter, such as in lakes, rivers, data to provide accurate and comprehensive wetlands and soils, or estimates of natural and and fugitive emissions • from deep beneath the earth’s surface where gaseous methane in Australia. has formed geochemically under elevated temperature and • A recent CSIRO study on GHG emissions from pressure conditions.