Environmental Chloroform Flux and That 90% of Emissions Are Natural in Origin
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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. -
A Fast-Response Methodological Approach to Assessing and Managing
Ecological Engineering 85 (2015) 47–55 Contents lists available at ScienceDirect Ecological Engineering jo urnal homepage: www.elsevier.com/locate/ecoleng A fast-response methodological approach to assessing and managing nutrient loads in eutrophic Mediterranean reservoirs a,∗ a a Bachisio Mario Padedda , Nicola Sechi , Giuseppina Grazia Lai , a b a a Maria Antonietta Mariani , Silvia Pulina , Cecilia Teodora Satta , Anna Maria Bazzoni , c c a Tomasa Virdis , Paola Buscarinu , Antonella Lugliè a University of Sassari, Department of Architecture, Design and Urban Planning, Via Piandanna 4, 07100 Sassari, Italy b University of Cagliari, Department of Life and Environmental Sciences, via T. Fiorelli 1, 09126 Cagliari, Italy c EN.A.S. Ente Acque della Sardegna, Settore della limnologia degli invasi, Viale Elmas 116, 09122 Cagliari, Italy a r a t i b s c l e i n f o t r a c t Article history: With many lakes and other inland water bodies worldwide being increasingly affected by eutrophication Received 13 July 2015 resulting from excess nutrient input, there is an urgent need for improved monitoring and prediction Received in revised form 8 September 2015 methods of nutrient load effects in such ecosystems. In this study, we adopted a catchment-based Accepted 19 September 2015 approach to identify and estimate the direct effect of external nutrient loads originating in the drainage basin on the trophic state of a Mediterranean reservoir. We also evaluated the trophic state variations Keywords: related to the theoretical manipulation of nutrient inputs. The study was conducted on Lake Cedrino, a Eutrophication typical warm monomictic reservoir, between 2010 and 2011. -
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. -
Department of Natural Resources Division 60—Public Drinking Water Program Chapter 2—Definitions
Rules of Department of Natural Resources Division 60—Public Drinking Water Program Chapter 2—Definitions Title Page 10 CSR 60-2.010 Installation, Extension, Testing and Operation of Public Water Supplies (Rescinded October 11, 1979) ..................................................3 10 CSR 60-2.015 Definitions .......................................................................................3 10 CSR 60-2.020 Grants for Public Water Supply Districts, Sewer Districts, Rural Community Water Supply and Sewer Systems and Certain Municipal Sewer Systems (Moved to 10 CSR-13.010).................................7 Rebecca McDowell Cook (7/31/00) CODE OF STATE REGULATIONS 1 Secretary of State Chapter 2—Definitions 10 CSR 60-2 Title 10—DEPARTMENT OF liquids, gases or other substances into the ified operator classification of the certifica- NATURAL RESOURCES public water system from any source(s). tion program under the provisions of 10 CSR Division 60—Public Drinking 2. Backflow hazard. Any facility which, 60-14.020. Water Program because of the nature and extent of activities 2. Certificate of examination. A certifi- Chapter 2—Definitions on the premises or the materials used in con- cate issued to a person who passes a written nection with the activities or stored on the examination but does not meet the experience 10 CSR 60-2.010 Installation, Extension, premises, would present an actual or potential requirements for the classification of exami- Testing and Operation of Public Water health hazard to customers of the public water nation taken. Supplies system or would threaten to degrade the water 3. Chief operator. The person designat- (Rescinded October 11, 1979) quality of the public water system should ed by the owner of a public water system to backflow occur. -
CHEMICAL STORAGE SEGREGATION GUIDELINES Incompatible Chemicals Should Always Be Handled and Stored So That They Do Not Accidentally Come in Contact with Each Other
Laboratory Safety Reminders January 2007 ♦ Mount Holyoke College – Environmental Health and Safety CHEMICAL STORAGE SEGREGATION GUIDELINES Incompatible chemicals should always be handled and stored so that they do not accidentally come in contact with each other. This list is not complete, nor are all compatibilities shown. These materials can react to produce excessive heat, harmful vapors, and/or other deadly reactions. Always know the hazards and incompatibilities of a chemical before using it. Chemicals Avoid Accidental Contact With Acetic acid Chromic acid, nitric acid, permanganates, peroxides Hydroxyl-containing compounds such as perchloric acid, Acetic anhydride ethylene glycol Concentrated nitric acid and sulfuric acid mixtures, peroxides (i.e. Acetone peracetic acid solution, hydrogen peroxide) Acetylene Chlorine, bromine, copper, silver, fluorine, mercury Alkali, alkaline earth and strongly electropositive metals (powered Carbon dioxide, carbon tetrachloride and other chlorinated aluminum, magnesium, sodium, hydrocarbons potassium) Mercury, chlorine, calcium hypochlorite, iodine, bromine, hydrogen Ammonia (anhydrous) fluoride Acids, metal powders, flammable liquids, chlorates, nitrates, sulfur, Ammonium nitrate finely divided organics, combustibles Aniline Nitric acid, hydrogen peroxide Arsenical compounds Any reducing agent Azides Acids Ammonia, acetylene, butadiene, butane, other petroleum gases, Bromine sodium carbide, turpentine, benzene, finely divided metals Calcium oxide Water Carbon activated Calcium hypochlorite, other -
Measurements and Fluxes of Volatile Chlorinated Organic Compounds (Vocl) from Natural Terrestrial Sources
Technical Report TR-18-09 February 2019 Measurements and fluxes of volatile chlorinated organic compounds (VOCl) from natural terrestrial sources Measurement techniques and spatio-temporal variability of flux estimates SVENSK KÄRNBRÄNSLEHANTERING AB SWEDISH NUCLEAR FUEL AND WASTE MANAGEMENT CO Box 3091, SE-169 03 Solna Phone +46 8 459 84 00 Teresia Svensson skb.se SVENSK KÄRNBRÄNSLEHANTERING ISSN 1404-0344 SKB TR-18-09 ID 1695279 February 2019 Measurements and fluxes of volatile chlorinated organic compounds (VOCl) from natural terrestrial sources Measurement techniques and spatio-temporal variability of flux estimates Teresia Svensson, Linköpings Universitet Keywords: Chlorine, Soil, Emission, Chloroform, Uptake, VOCl, Surface ecosystem, Biosphere, SE-SFL. This report concerns a study which was conducted for Svensk Kärnbränslehantering AB (SKB). The conclusions and viewpoints presented in the report are those of the author. SKB may draw modified conclusions, based on additional literature sources and/or expert opinions. A pdf version of this document can be downloaded from www.skb.se. © 2019 Svensk Kärnbränslehantering AB Abstract Volatile organic compounds (VOCs) and especially chlorinated VOCs (VOCls) are regarded as en viron mental risk substances in water bodies due to their toxic characteristics. Even in the atmo sphere they highly impact atmospheric chemistry, e.g. degrading the ozone layer. Several studies have convincingly identified a number of natural VOCl sources thereby challenging the view of VOCls as only produced by humans. Yet, fundamental knowledge is still missing concerning the emission, distribution and the natural abundance of VOCls, especially regarding the high spatial and temporal variability of emissions from terrestrial sources. In the nuclear industry, Cl36 is a dosedominating radionuclide in some waste, and this adds to the need to better understand the processes, transport and fate of chlorine in the biosphere. -
Removal of NO and SO2 by Pulsed Corona Discharge Process
Korean J. Chem. Eng., 18(3), 308-316 (2001) Removal of NO and SO2 by Pulsed Corona Discharge Process Young Sun Mok†, Ho Won Lee, Young Jin Hyun, Sung Won Ham*, Jae Hak Kim** and In-Sik Nam** Department of Chemical Engineering, Cheju National University, Ara, Cheju 690-756, Korea *Department of Chemical Engineering, Kyungil University, Hayang, Kyungbuk 712-701, Korea **Department of Chemical Engineering, Pohang University of Science & Technology, Pohang, Kyungbuk 790-784, Korea (Received 6 September 2000 • accepted 9 March 2001) − Abstract Overall examination was made on the removal of NO and SO2 by pulsed corona discharge process. The mechanism for the removal of NO was found to largely depend on the gas composition. In the absence of oxygen, most of the NO removed was reduced to N2; on the other hand, oxidation of NO to NO2 was dominant in the presence of oxygen even when the content was low. Water vapor was an important ingredient for the oxidation of NO2 to nitric acid rather than that of NO to NO2. The removal of NO only slightly increased with the concentration of ammonia while the effect of ammonia on the removal of SO2 was very significant. The energy density (power delivered/feed gas flow rate) can be a measure for the degree of removal of NO. Regardless of the applied voltage and the flow rate of the feed gas stream, the amount of NO removed was identical at the same energy density. The production of N2O increased with the pulse repetition rate, and the presence of NH3 and SO2 enhanced it. -
INF.20 Economic Commission for Europe Inland Transport Committee Definition Of
INF.20 Economic Commission for Europe Inland Transport Committee Working Party on the Transport of Dangerous Goods 6 March 2012 Joint Meeting of the RID Committee of Experts and the Working Party on the Transport of Dangerous Goods Bern, 19–23 March 2012 Item 5(a) of the provisional agenda Proposals for amendments to RID/ADR/ADN: pending issues Definition of LPG Transmitted by the Government of Switzerland We have observed contradictions in the definition of LPG adopted by the Joint Meeting at its Autumn 2010 session (ECE/TRANS/WP.15/AC.1/120, Annex II) as well as in the German translation we have discussed in Erfurt during the Conference of translation and edition of the German ADR. The actual definitions in each language are the following: ""Gaz de pétrole liquéfié (GPL)", un gaz liquéfié à faible pression contenant un ou plusieurs hydrocarbures légers qui sont affectés aux numéros ONU 1011, 1075, 1965, 1969 ou 1978 seulement et qui est principalement constitué de propane, de propène, de butane, des isomères du butane, de butène avec des traces d’autres gaz d’hydrocarbures. “‘Liquefied Petroleum Gas (LPG)’ means a low pressure liquefied gas composed of one or more light hydrocarbons which are assigned to UN Nos. 1011, 1075, 1965, 1969 or 1978 only and which consists mainly of propane, propene, butane, butane isomers, butene with traces of other hydrocarbon gases. „Flüssiggas (LPG)*: Unter geringem Druck verflüssigtes Gas, das aus einem oder mehreren leichten Kohlenwasserstoffen besteht, die nur der UN-Nummer 1011, 1075, 1965, 1969 oder 1978 zugeordnet sind und das hauptsächlich aus Propan, Propen, Butan, Butan-Isomeren und Buten mit Spuren anderer Kohlenwasserstoffgase besteht.“ One important point is different between French from one side and English and German from the other side, that is that in French the repetition of the “de” in the enumeration of possible gases brings to the conclusion that the main constituent of the LPG is one of the listed gases. -
Regression Relations and Long-Term Water-Quality Constituent
Prepared in cooperation with the City of Wichita Regression Relations and Long-Term Water-Quality Constituent Concentrations, Loads, Yields, and Trends in the North Fork Ninnescah River, South-Central Kansas, 1999–2019 Scientific Investigations Report 2021–5006 U.S. Department of the Interior U.S. Geological Survey Cover. Photograph showing North Fork Ninnescah River downstream from the continuous water- quality monitor installation, taken at the North Fork Ninnescah River above Cheney Reservoir (U.S. Geological Survey [USGS] site 07144780) on July 8, 2020, by David Eason (USGS hydrologic technician). Back cover. Photograph showing sandy channel and streamflow conditions at 150 cubic feet per second upstream from the continuous water-quality monitor installation, taken at the North Fork Ninnescah River above Cheney Reservoir (USGS site 07144780) on November 26, 2018, by USGS personnel. Regression Relations and Long-Term Water-Quality Constituent Concentrations, Loads, Yields, and Trends in the North Fork Ninnescah River, South-Central Kansas, 1999–2019 By Ariele R. Kramer, Brian J. Klager, Mandy L. Stone, and Patrick J. Eslick-Huff Prepared in cooperation with the City of Wichita Scientific Investigations Report 2021–5006 U.S. Department of the Interior U.S. Geological Survey U.S. Geological Survey, Reston, Virginia: 2021 For more information on the USGS—the Federal source for science about the Earth, its natural and living resources, natural hazards, and the environment—visit https://www.usgs.gov or call 1–888–ASK–USGS. For an overview of USGS information products, including maps, imagery, and publications, visit https://store.usgs.gov/. Any use of trade, firm, or product names is for descriptive purposes only and does not imply endorsement by the U.S. -
Transmittal of Final "Guidance for State Implementation of Water Quality Standards for CWA Section 303(C) (2) (B)"
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY WASHINGTON. D.C. 20460 OFFICEOF WATER MEMORANDUM SUBJECT: Transmittal of Final "Guidance for State Implementation of Water Quality Standards for CWA Section 303(c) (2) (B)" FROM: Rebecca W. Hanmer, Acting Assistant Administrator for Water (WH-556) TO: Water Management Division Directors Regions I-X Directors State Water Pollution Control Agencies Attached is the final guidance on State adoption of criteria for priority toxic pollutants. We prepared this guidance to help States comply with the new requirements of the 1987 amendments to the Clean Water Act. We have made only minor changes to the September 2, 1988 draft which was distributed to you earlier. The guidance focuses specifically on the new effort to control toxics in water quality standards. It does not supersede other elements of the standards program which address conventional and non-conventional pollutants as well as priority toxic pollutants. These other elements are described in other Office of Water guidance such as the Water Quality Standards Handbook and continue in full force and effect. Some commenters on the draft expressed a concern that the guidance places an unnecessary burden on States to demonstrate a need to regulate toxics before State criteria are adopted. This comment related primarily to Option 2 which provides for a more target red approach than Option 1. We wish to clarify that no such requirement for the States to develop a demonstration of need is included in or intended by the guidance. We do urge States, as a minimum, to use their identifications of impacted segments under Section 304(l) as a starting point for identifying locations where toxic pollutants are of concern and in need of coverage in State standards. -
Plasma-Pd/Γ-Al203 Catalytic System for Methane, Toluene and Propene Oxidation: Effect of Temperature and Plasma Input Power
22nd International Symposium on Plasma Chemistry July 5-10, 2015; Antwerp, Belgium Plasma-Pd/γ-Al203 catalytic system for methane, toluene and propene oxidation: effect of temperature and plasma input power T. Pham Huu1, 2, P. Da Costa3, S. Loganathan1 and A. Khacef1 1 GREMI-UMR 6744, CNRS-Université d'Orléans, 14 rue d’Issoudun, P.O. Box 6744, FR-45067 Orléans Cedex 02, France 2 Institute of Applied Material Science, Vietnam Academy of Science and Technology, 1 Mac Dinh Chi, HCMC, Vietnam 3 Sorbonne Universités, UPMC Paris 6, Institut Jean Le Rond d’Alembert, CNRS UMR 7190, 2 place de la gare de ceinture, FR-78210 Saint Cyr l’école, France Abstract: A pulsed non-thermal plasma and 1 wt% Pd/γ-Al2O3 catalyst was used to investigate the CH4, C3H6, and C7H8 oxidation in air. Effects of temperature and specific input energy on the VOCs conversion were studied. The plasma-catalyst interaction revealed the benefit effect on the VOCs oxidation even at low temperature leading to high CO2 selectivity. The synergistic effect of combining plasma with catalyst in one-stage configuration is observed only for toluene. Keywords: non-thermal plasma, Pd/γ-Al203, synergistic effect, methane, propene, toluene, oxidation 1. Introduction 2. Experimental Volatile organic compounds (VOCs) emitted from The plasma reactor is a cylindrical DBD gives the various industrial and domestic processes are important possibility to combine the catalyst with plasma reactor in sources of air pollution and therefore, become a serious single stage (IPC) or two-stage (PPC) configuration as problem for damaging the human health and the shown in Fig.