Glossary: Wastewater Treatment and Collection System Terms
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Total Organic Carbon (TOC) Guidance Manual
September 2002 RG-379 (Revised) Total Organic Carbon (TOC) Guidance Manual Water Supply Division printed on recycled paper TEXAS COMMISSION ON ENVIRONMENTAL QUALITY Total Organic Carbon (TOC) Guidance Manual Prepared by Water Supply Division RG-379 (Revised) September 2002 Robert J. Huston, Chairman R. B. “Ralph” Marquez, Commissioner Kathleen Hartnett White, Commissioner Jeffrey A. Saitas, Executive Director Authorization to use or reproduce any original material contained in this publication—that is, not obtained from other sources—is freely granted. The commission would appreciate acknowledgment. Copies of this publication are available for public use through the Texas State Library, other state depository libraries, and the TCEQ Library, in compli- ance with state depository law. For more information on TCEQ publications call 512/239-0028 or visit our Web site at: www.tceq.state.tx.us/publications Published and distributed by the Texas Commission on Environmental Quality PO Box 13087 Austin TX 78711-3087 The Texas Commission on Environmental Quality was formerly called the Texas Natural Resource Conservation Commission. The TCEQ is an equal opportunity/affirmative action employer. The agency does not allow discrimination on the basis of race, color, religion, national origin, sex, disability, age, sexual orientation or veteran status. In compliance with the Americans with Disabilities Act, this document may be requested in alternate formats by contacting the TCEQ at 512/239-0028, Fax 239-4488, or 1-800-RELAY-TX (TDD), or by writing -
Estimation of Atmospheric Total Organic Carbon (TOC) – Paving The
Atmos. Chem. Phys. Discuss., https://doi.org/10.5194/acp-2018-1055 Manuscript under review for journal Atmos. Chem. Phys. Discussion started: 12 October 2018 c Author(s) 2018. CC BY 4.0 License. Estimation of atmospheric total organic carbon (TOC) – paving the path towards carbon budget closure Mingxi Yang1*, Zoë L. Fleming2& 5 1 Plymouth Marine Laboratory, Plymouth, United Kingdom 2 National Centre for Atmospheric Science (NCAS), Department of Chemistry, University of Leicester, UK, United Kingdom * Correspondence to M. Yang ([email protected]) & Now at Center for Climate and Resilience Research (CR2), Departamento de Geofísica, Universidad de Chile, Santiago, Chile 10 Abstract. The atmosphere contains a rich variety of reactive organic compounds, including gaseous volatile organic carbon (VOCs), carbonaceous aerosols, and other organic compounds at varying volatility. Here we present measurements of atmospheric non-methane total organic carbon plus carbon monoxide (TOC+CO) during August-September 2016 from a coastal 15 city in the southwest United Kingdom. TOC+CO was substantially elevated during the day on weekdays (occasionally over 2 ppm C) as a result of local anthropogenic activity. On weekends and holidays, with a mean (standard error) of 102 (8) ppb C, TOC+CO was lower and showed much less diurnal variability. Excluding weekday daytime, TOC+CO was significantly lower when winds were coming off the Atlantic Ocean than when winds were coming off land. By subtracting the estimated CO from TOC+CO, we constrain the mean (uncertainty) TOC in marine air to be around 19 (±≥8) ppb C during this period. A proton- 20 transfer-reaction mass spectrometer (PTR-MS) was deployed at the same time, detecting a large range of organic compounds (oxygenated VOCs, biogenic VOCs, aromatics, dimethyl sulfide). -
Water Treatment and Reverse Osmosis Systems
Pure Aqua, Inc.® Water© 2012 TreatmentPure Aqua ,and Inc. ReverseAll Right sOsmosis Reserve dSystems. Worldwide Experience Superior Technology About the Company Pure Aqua is a company with a strong philosophy and drive to develop and apply solutions to the world’s water treatment challenges. We believe that both our technology and experience will help resolve the growing shortage of clean water worldwide. Capabilities and Expertise As an ISO 9001:2008 certified company with over a decade of experience, Pure Aqua has secured its position as a leading manufacturer of reverse osmosis systems worldwide. Goals and Motivations Our goal is to provide environmentally sustainable systems and equipment that produce high quality water. We provide packaged systems and technical support for water treatment plants, industrial wastewater reuse, and brackish and seawater reverse osmosis plants. Having strong working relationships with Thus, we ensure our technological our suppliers gives us the capability to contribution to water preservation by provide cost effective and competitive supplying the means and making it highly water and wastewater treatment systems accessible. for a wide range of applications. Seawater Reverse Osmosis Systems System Overview Designed to convert seawater to potable water, desalination systems use high quality reverse osmosis seawater membranes. The process separates dissolved salts by only allowing pure water to pass through the membrane fabric. System Capacities Pure Aqua desalination systems are designed to provide high -
Package Plants Arrive on Site Virtually Ready to Operate and Built to Minimize the Day-To-Day Attention Required to Operate the Equipment
A NATIONAL DRINKING WATER CLEARINGHOUSE FACT SHEET Package Plants Summary Small water treatment systems often find it difficult to comply with the U.S. Environmental Protection Agency (EPA) regulations. Small communities often face financial problems in purchas- ing and maintaining conventional treatment systems. Their problem is further complicated if they do not have the services of a full-time, trained operator. The Surface Water Treatment Rule (SWTR) requirements have greatly increased interest in the possible use of package plants in many areas of the country. Package plants can also be applied to treat contaminants such as iron and manganese in groundwater via oxidation and filtration. ○○○○○○○○○○ Package Plants: Alternative to Conventional Treatment What is a package plant? How To Select a Package Plant Package technology offers an alternative to Package plant systems are most appropriate for in-ground conventional treatment technology. plant sizes that treat from 25,000 to 6,000,000 They are not altogether different from other gallons per day (GPD) (94.6 to 22,710 cubic treatment processes although several package ○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○○ meters per day). Influent water quality is the plant models contain innovative treatment most important consideration in determining elements, such as adsorptive clarifiers. The the suitability of a package plant application. primary distinction, however, between package Complete influent water quality records need plants and custom-designed plants is that to be examined to establish turbidity levels, package plants are treatment units assembled seasonal temperature fluctuations, and color in a factory, skid mounted, and transported level expectations. Both high turbidity and color to the site. may require coagulant dosages beyond many package plants design specifications. -
E.’S Responses ~(Continued)
: I’able K-3. ,Scnping stat~nts and EIS sectimns or .~E.’s responses ~(continued) COnunent scoping nuinber :Stateilmnt topic EIS section or DOE comnt h at this tti want to reiter&e that the Enviro~ntal l~act Statement should not represent. a legalistic charade ..but a sin. cere commitment to seek and evaluate pertinent in for~t ion. Obviously, any Envirocnnental. Assemnt- which led to the Find- ing of No Significant .l~act needs to be reviewed, evaluated and expanded upon, with full regard to the in~t of a broad range of interests, incl”di”g state agenciea,. the: academic comunit y, public interest groups, and private c iti-zens. We muld like to offer some co-”ts: on the in format io” euppl=ied by 00E relative to the probable contents. of the EIS. In the category of production alternatives: : It wuld seem L Need .Section 1.1 ., important tO. re-evaluate the ,need for i~reased protict ion,~nd %e Commnt D1 make every attempt to ::scale dom those need8. It is ine8ca~ able that the quest ion. af the.,need .to prodca plutoniun ia part of the greater ongoing natic,”al.?security debate. If it is indeed. essential that plutoniun: probct ion be stepped up, the Alternatives Saction 2.1 viable? alternatives should be thoroughly explored in the EIS. In the category of socioeconamics: A broad consideration of %cioeconomic .%ction 5.2.1 the state needs to be incorporated, beyond the immdiate jobs effects :-at SiU during construction and as .an ongoing operation. South Carolina has trenmndous potential for no-nuclear economic. -
Carbon Dynamics of Subtropical Wetland Communities in South Florida DISSERTATION Presented in Partial Fulfillment of the Require
Carbon Dynamics of Subtropical Wetland Communities in South Florida DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By Jorge Andres Villa Betancur Graduate Program in Environmental Science The Ohio State University 2014 Dissertation Committee: William J. Mitsch, Co-advisor Gil Bohrer, Co-advisor James Bauer Jay Martin Copyrighted by Jorge Andres Villa Betancur 2014 Abstract Emission and uptake of greenhouse gases and the production and transport of dissolved organic matter in different wetland plant communities are key wetland functions determining two important ecosystem services, climate regulation and nutrient cycling. The objective of this dissertation was to study the variation of methane emissions, carbon sequestration and exports of dissolved organic carbon in wetland plant communities of a subtropical climate in south Florida. The plant communities selected for the study of methane emissions and carbon sequestration were located in a natural wetland landscape and corresponded to a gradient of inundation duration. Going from the wettest to the driest conditions, the communities were designated as: deep slough, bald cypress, wet prairie, pond cypress and hydric pine flatwood. In the first methane emissions study, non-steady-state rigid chambers were deployed at each community sequentially at three different times of the day during a 24- month period. Methane fluxes from the different communities did not show a discernible daily pattern, in contrast to a marked increase in seasonal emissions during inundation. All communities acted at times as temporary sinks for methane, but overall were net -2 -1 sources. Median and mean + standard error fluxes in g CH4-C.m .d were higher in the deep slough (11 and 56.2 + 22.1), followed by the wet prairie (9.01 and 53.3 + 26.6), bald cypress (3.31 and 5.54 + 2.51) and pond cypress (1.49, 4.55 + 3.35) communities. -
Safe Use of Wastewater in Agriculture: Good Practice Examples
SAFE USE OF WASTEWATER IN AGRICULTURE: GOOD PRACTICE EXAMPLES Hiroshan Hettiarachchi Reza Ardakanian, Editors SAFE USE OF WASTEWATER IN AGRICULTURE: GOOD PRACTICE EXAMPLES Hiroshan Hettiarachchi Reza Ardakanian, Editors PREFACE Population growth, rapid urbanisation, more water intense consumption patterns and climate change are intensifying the pressure on freshwater resources. The increasing scarcity of water, combined with other factors such as energy and fertilizers, is driving millions of farmers and other entrepreneurs to make use of wastewater. Wastewater reuse is an excellent example that naturally explains the importance of integrated management of water, soil and waste, which we define as the Nexus While the information in this book are generally believed to be true and accurate at the approach. The process begins in the waste sector, but the selection of date of publication, the editors and the publisher cannot accept any legal responsibility for the correct management model can make it relevant and important to any errors or omissions that may be made. The publisher makes no warranty, expressed or the water and soil as well. Over 20 million hectares of land are currently implied, with respect to the material contained herein. known to be irrigated with wastewater. This is interesting, but the The opinions expressed in this book are those of the Case Authors. Their inclusion in this alarming fact is that a greater percentage of this practice is not based book does not imply endorsement by the United Nations University. on any scientific criterion that ensures the “safe use” of wastewater. In order to address the technical, institutional, and policy challenges of safe water reuse, developing countries and countries in transition need clear institutional arrangements and more skilled human resources, United Nations University Institute for Integrated with a sound understanding of the opportunities and potential risks of Management of Material Fluxes and of Resources wastewater use. -
Sedimentation and Clarification Sedimentation Is the Next Step in Conventional Filtration Plants
Sedimentation and Clarification Sedimentation is the next step in conventional filtration plants. (Direct filtration plants omit this step.) The purpose of sedimentation is to enhance the filtration process by removing particulates. Sedimentation is the process by which suspended particles are removed from the water by means of gravity or separation. In the sedimentation process, the water passes through a relatively quiet and still basin. In these conditions, the floc particles settle to the bottom of the basin, while “clear” water passes out of the basin over an effluent baffle or weir. Figure 7-5 illustrates a typical rectangular sedimentation basin. The solids collect on the basin bottom and are removed by a mechanical “sludge collection” device. As shown in Figure 7-6, the sludge collection device scrapes the solids (sludge) to a collection point within the basin from which it is pumped to disposal or to a sludge treatment process. Sedimentation involves one or more basins, called “clarifiers.” Clarifiers are relatively large open tanks that are either circular or rectangular in shape. In properly designed clarifiers, the velocity of the water is reduced so that gravity is the predominant force acting on the water/solids suspension. The key factor in this process is speed. The rate at which a floc particle drops out of the water has to be faster than the rate at which the water flows from the tank’s inlet or slow mix end to its outlet or filtration end. The difference in specific gravity between the water and the particles causes the particles to settle to the bottom of the basin. -
Troubleshooting Activated Sludge Processes Introduction
Troubleshooting Activated Sludge Processes Introduction Excess Foam High Effluent Suspended Solids High Effluent Soluble BOD or Ammonia Low effluent pH Introduction Review of the literature shows that the activated sludge process has experienced operational problems since its inception. Although they did not experience settling problems with their activated sludge, Ardern and Lockett (Ardern and Lockett, 1914a) did note increased turbidity and reduced nitrification with reduced temperatures. By the early 1920s continuous-flow systems were having to deal with the scourge of activated sludge, bulking (Ardem and Lockett, 1914b, Martin 1927) and effluent suspended solids problems. Martin (1927) also describes effluent quality problems due to toxic and/or high-organic- strength industrial wastes. Oxygen demanding materials would bleedthrough the process. More recently, Jenkins, Richard and Daigger (1993) discussed severe foaming problems in activated sludge systems. Experience shows that controlling the activated sludge process is still difficult for many plants in the United States. However, improved process control can be obtained by systematically looking at the problems and their potential causes. Once the cause is defined, control actions can be initiated to eliminate the problem. Problems associated with the activated sludge process can usually be related to four conditions (Schuyler, 1995). Any of these can occur by themselves or with any of the other conditions. The first is foam. So much foam can accumulate that it becomes a safety problem by spilling out onto walkways. It becomes a regulatory problem as it spills from clarifier surfaces into the effluent. The second, high effluent suspended solids, can be caused by many things. It is the most common problem found in activated sludge systems. -
Determining the Fraction of Organic Carbon RISC Nondefault Option
Indiana Department of Environmental Management Office of Land Quality 100 N. Senate Indianapolis, IN 46204-2251 GUIDANCE OLQ PH: (317) 232-8941 Indiana Department of Environmental Management Office of Land Quality Determining the Fraction of Organic Carbon RISC Nondefault Option Background Soil can be a complex mixture of mineral-derived compounds and organic matter. The ratios of each component can vary widely depending on the type of soil being investigated. Soil organic matter is a term used by agronomists for the total organic portion of the soil and is derived from decomposed plant matter, microorganisms, and animal residues. The decomposition process can create complex high molecular weight biopolymers (e.g., humic acid) as well as simpler organic compounds (decomposed lignin or cellulose). Only the simpler organic compounds contribute to the fraction of organic carbon. There is not a rigorous definition of the fraction of organic carbon (Foc). However, it can be thought of as the portion of the organic matter that is available to adsorb the organic contaminants of concern. The higher the organic carbon content, the more organic chemicals may be adsorbed to the soil and the less of those chemicals will be available to leach to the ground water. A nondefault option in the Risk Integrated System of Closure (RISC) is to use Foc in the Soil to Ground Water Partitioning Model to calculate a site specific migration to ground water closure level. In the Soil to Ground Water Partition Model, the coefficient, Kd, for organic compounds is the Foc multiplied by the chemical-specific soil organic carbon water partition coefficient, Koc. -
Defoamer Formulation Entschäumerzusammensetzung Composition Antimousse
(19) TZZ ¥ZZ_T (11) EP 2 430 095 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.: of the grant of the patent: C08L 33/06 (2006.01) B01D 19/04 (2006.01) 07.03.2018 Bulletin 2018/10 (86) International application number: (21) Application number: 10720061.0 PCT/US2010/033827 (22) Date of filing: 06.05.2010 (87) International publication number: WO 2010/132262 (18.11.2010 Gazette 2010/46) (54) DEFOAMER FORMULATION ENTSCHÄUMERZUSAMMENSETZUNG COMPOSITION ANTIMOUSSE (84) Designated Contracting States: • WILSON, Robert AL AT BE BG CH CY CZ DE DK EE ES FI FR GB Marietta, GA 30060 (US) GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO • ROSENCRANCE, Scott PL PT RO SE SI SK SM TR Douglasville, GA 30135 (US) • PREVIS, David (30) Priority: 15.05.2009 US 466637 King William, VA 23086 (US) (43) Date of publication of application: (74) Representative: Potter Clarkson LLP 21.03.2012 Bulletin 2012/12 The Belgrave Centre Talbot Street (73) Proprietor: Kemira Chemicals Inc. Nottingham NG1 5GG (GB) Atlanta GA 30339 (US) (56) References cited: (72) Inventors: GB-A- 2 094 330 US-A- 5 152 925 • MARTIN, James Bonaire, GA 31005 (US) Note: Within nine months of the publication of the mention of the grant of the European patent in the European Patent Bulletin, any person may give notice to the European Patent Office of opposition to that patent, in accordance with the Implementing Regulations. Notice of opposition shall not be deemed to have been filed until the opposition fee has been paid. -
A Diurnal Carbon Engine Explains 13C-Enriched Carbonates
A diurnal carbon engine explains 13C-enriched carbonates without increasing the global production of oxygen Emily C. Geymana,1 and Adam C. Maloofa aDepartment of Geosciences, Princeton University, Princeton, NJ 08544 Edited by Donald E. Canfield, Institute of Biology and Nordic Center for Earth Evolution, University of Southern Denmark, Odense M., Denmark, and approved October 8, 2019 (received for review May 21, 2019) In the past 3 billion years, significant volumes of carbonate processes can be constrained by visualizing the carbon evolution with high carbon-isotopic (δ13C) values accumulated on shallow of banktop seawater in a Deffeyes diagram (9) (Fig. 2B), since continental shelves. These deposits frequently are interpreted each mechanism induces a characteristic change in DIC and total as records of elevated global organic carbon burial. However, alkalinity (TA) (Table 1). Observations of TOC (5) and DIC vs. through the stoichiometry of primary production, organic carbon TA (7) from the GBB constrain the relative sizes of the net car- burial releases a proportional amount of O2, predicting unrealis- bonate, gas-exchange, and organic fluxes to be 62, 37, and <1%, tic rises in atmospheric pO2 during the 1 to 100 million year-long respectively (Fig. 2). Although the net burial of organic matter positive δ13C excursions that punctuate the geological record. is close to zero, the flux of carbon between organic matter and This carbon–oxygen paradox assumes that the δ13C of shallow the DIC pool over the course of a single diurnal (24-h) cycle water carbonates reflects the δ13C of global seawater-dissolved can exceed the gross atmospheric and carbonate fluxes by over inorganic carbon (DIC).