Evaluation of the Precision of High-Performance Liquid Chromatography for Wheat Cultivar Identification'
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Environmental Quality: in Situ Air Sparging
EM 200-1-19 31 December 2013 Environmental Quality IN-SITU AIR SPARGING ENGINEER MANUAL AVAILABILITY Electronic copies of this and other U.S. Army Corps of Engineers (USACE) publications are available on the Internet at http://www.publications.usace.army.mil/ This site is the only repository for all official USACE regulations, circulars, manuals, and other documents originating from HQUSACE. Publications are provided in portable document format (PDF). This document is intended solely as guidance. The statutory provisions and promulgated regulations described in this document contain legally binding requirements. This document is not a legally enforceable regulation itself, nor does it alter or substitute for those legal provisions and regulations it describes. Thus, it does not impose any legally binding requirements. This guidance does not confer legal rights or impose legal obligations upon any member of the public. While every effort has been made to ensure the accuracy of the discussion in this document, the obligations of the regulated community are determined by statutes, regulations, or other legally binding requirements. In the event of a conflict between the discussion in this document and any applicable statute or regulation, this document would not be controlling. This document may not apply to a particular situation based upon site- specific circumstances. USACE retains the discretion to adopt approaches on a case-by-case basis that differ from those described in this guidance where appropriate and legally consistent. This document may be revised periodically without public notice. DEPARTMENT OF THE ARMY EM 200-1-19 U.S. Army Corps of Engineers CEMP-CE Washington, D.C. -
Producing Nitrogen Via Pressure Swing Adsorption
Reactions and Separations Producing Nitrogen via Pressure Swing Adsorption Svetlana Ivanova Pressure swing adsorption (PSA) can be a Robert Lewis Air Products cost-effective method of onsite nitrogen generation for a wide range of purity and flow requirements. itrogen gas is a staple of the chemical industry. effective, and convenient for chemical processors. Multiple Because it is an inert gas, nitrogen is suitable for a nitrogen technologies and supply modes now exist to meet a Nwide range of applications covering various aspects range of specifications, including purity, usage pattern, por- of chemical manufacturing, processing, handling, and tability, footprint, and power consumption. Choosing among shipping. Due to its low reactivity, nitrogen is an excellent supply options can be a challenge. Onsite nitrogen genera- blanketing and purging gas that can be used to protect valu- tors, such as pressure swing adsorption (PSA) or membrane able products from harmful contaminants. It also enables the systems, can be more cost-effective than traditional cryo- safe storage and use of flammable compounds, and can help genic distillation or stored liquid nitrogen, particularly if an prevent combustible dust explosions. Nitrogen gas can be extremely high purity (e.g., 99.9999%) is not required. used to remove contaminants from process streams through methods such as stripping and sparging. Generating nitrogen gas Because of the widespread and growing use of nitrogen Industrial nitrogen gas can be produced by either in the chemical process industries (CPI), industrial gas com- cryogenic fractional distillation of liquefied air, or separa- panies have been continually improving methods of nitrogen tion of gaseous air using adsorption or permeation. -
Ethanol Production from Hydrolyzed Kraft Pulp by Mono- and Co-Cultures of Yeasts: the Challenge of C6 and C5 Sugars Consumption
energies Article Ethanol Production from Hydrolyzed Kraft Pulp by Mono- and Co-Cultures of Yeasts: The Challenge of C6 and C5 Sugars Consumption Rita H. R. Branco, Mariana S. T. Amândio, Luísa S. Serafim and Ana M. R. B. Xavier * CICECO–Aveiro Institute of Materials, Chemistry Department, University of Aveiro, Campus Universitario de; Santiago, 3810-193 Aveiro, Portugal; [email protected] (R.H.R.B.); [email protected] (M.S.T.A.); luisa.serafi[email protected] (L.S.S.) * Correspondence: [email protected]; Tel.: +351-234-370-716 Received: 27 December 2019; Accepted: 4 February 2020; Published: 8 February 2020 Abstract: Second-generation bioethanol production’s main bottleneck is the need for a costly and technically difficult pretreatment due to the recalcitrance of lignocellulosic biomass (LCB). Chemical pulping can be considered as a LCB pretreatment since it removes lignin and targets hemicelluloses to some extent. Chemical pulps could be used to produce ethanol. The present study aimed to investigate the batch ethanol production from unbleached Kraft pulp of Eucalyptus globulus by separate hydrolysis and fermentation (SHF). Enzymatic hydrolysis of the pulp resulted in a glucose yield of 96.1 3.6% and a xylose yield of 94.0 7.1%. In an Erlenmeyer flask, fermentation of the ± ± hydrolysate using Saccharomyces cerevisiae showed better results than Scheffersomyces stipitis. At both the Erlenmeyer flask and bioreactor scale, co-cultures of S. cerevisiae and S. stipitis did not show significant improvements in the fermentation performance. The best result was provided by S. cerevisiae alone in a bioreactor, which fermented the Kraft pulp hydrolysate with an ethanol yield of 0.433 g g 1 and a volumetric ethanol productivity of 0.733 g L 1 h 1, and a maximum ethanol · − · − · − concentration of 19.24 g L 1 was attained. -
"Determination of Total Organic Carbon and Specific UV
EPA Document #: EPA/600/R-05/055 METHOD 415.3 DETERMINATION OF TOTAL ORGANIC CARBON AND SPECIFIC UV ABSORBANCE AT 254 nm IN SOURCE WATER AND DRINKING WATER Revision 1.1 February, 2005 B. B. Potter, USEPA, Office of Research and Development, National Exposure Research Laboratory J. C. Wimsatt, The National Council On The Aging, Senior Environmental Employment Program NATIONAL EXPOSURE RESEARCH LABORATORY OFFICE OF RESEARCH AND DEVELOPMENT U.S. ENVIRONMENTAL PROTECTION AGENCY CINCINNATI, OHIO 45268 415.3 - 1 METHOD 415.3 DETERMINATION OF TOTAL ORGANIC CARBON AND SPECIFIC UV ABSORBANCE AT 254 nm IN SOURCE WATER AND DRINKING WATER 1.0 SCOPE AND APPLICATION 1.1 This method provides procedures for the determination of total organic carbon (TOC), dissolved organic carbon (DOC), and UV absorption at 254 nm (UVA) in source waters and drinking waters. The DOC and UVA determinations are used in the calculation of the Specific UV Absorbance (SUVA). For TOC and DOC analysis, the sample is acidified and the inorganic carbon (IC) is removed prior to analysis for organic carbon (OC) content using a TOC instrument system. The measurements of TOC and DOC are based on calibration with potassium hydrogen phthalate (KHP) standards. This method is not intended for use in the analysis of treated or untreated industrial wastewater discharges as those wastewater samples may damage or contaminate the instrument system(s). 1.2 The three (3) day, pooled organic carbon detection limit (OCDL) is based on the detection limit (DL) calculation.1 It is a statistical determination of precision, and may be below the level of quantitation. -
Article Metric to 'Green' Chemistry – Which Are the Best?
View Article Online / Journal Homepage / Table of Contents for this issue Metrics to ‘green’ chemistry—which are the best? David J. C. Constable,a Alan D. Curzonsb and Virginia L. Cunninghama a GlaxoSmithKline Pharmaceuticals, 2200 Renaissance Boulevard, King of Prussia, PA 19406, USA. E-mail: [email protected] b GlaxoSmithKline Pharmaceuticals, Southdownview Way, Worthing, West Sussex, UK BN14 8NQ Received 26th June 2002 First published as an Advance Article on the web 17th October 2002 A considerable amount has been written about the use of metrics to drive business, government and communities towards more sustainable practices. A number of metrics have also been proposed over the past 5U10 years to make chemists aware of the need to change the methods used for chemical syntheses and chemical processes. This paper explores several metrics commonly used by chemists and compares and contrasts these metrics with a new metric known as reaction mass efficiency. The paper also uses an economic analysis of four commercial pharmaceutical processes to understand the relationship between metrics and the most important cost drivers in these processes. Selected metrics used in the past autoclaved cell mass have some environmental impacts of one kind or another that would need to be evaluated and ad- A considerable number of publications have been written about dressed. the use of metrics to drive business, government and commu- nities towards more sustainable practices. The reader is referred elsewhere for a discussion of what metrics have -
The LC Handbook Guide to LC Columns and Method Development Contents
Agilent CrossLab combines the innovative laboratory services, software, and consumables competencies of Agilent Technologies and provides a direct connection to a global team of scientific and technical experts who deliver vital, actionable insights at every level of the lab environment. Our insights maximize performance, reduce complexity, and drive improved economic, operational, and scientific outcomes. Only Agilent CrossLab offers the unique combination of innovative products and comprehensive solutions to generate immediate results and lasting impact. We partner with our customers to create new opportunities across the lab, around the world, and every step of the way. More information at www.agilent.de/crosslab Learn more The LC Handbook – Guide to LC Columns and Method Development www.agilent.com/chem/lccolumns Buy online www.agilent.com/chem/store Find an Agilent customer center or authorized distributor www.agilent.com/chem/contactus U.S. and Canada 1-800-227-9770 [email protected] Europe [email protected] Asia Pacific [email protected] The LC India [email protected] Handbook Information, descriptions and specifications in this publication are subject to change without notice. Agilent Technologies shall not Guide to LC Columns and be liable for errors contained herein or for incidental or consequential damages in connection with the furnishing, performance or use of this material. Method Development © Agilent Technologies, Inc. 2016 Published in USA, February 1, 2016 Publication Number 5990-7595EN -
Method for Removing Iodine from Nitric Acid
3,803,295 United States Patent Office Patented Apr. 9, 1974 using a diluent carrier isotope as taught by the prior art 3 803 295 was unacceptable for achieving satisfactory iodine re- METHOD FOR REMOVING IODINE FROM moval. NITRIC ACID SUMMARY OF THE INVENTION George I. Gathers and Calvin J. Shipman, Knoxville, Tenn., assignors to the United States of America as 5 It is thus an object of this invention to provide a proc- represented by the United States Atomic Energy Com- ess whereby radioactive iodine may be effectively and mission efficiently removed from nitric acid solutions to concen- No Drawing, Continuation-in-part of application Ser. No. trations which are acceptable for reprocessing require- 231,820, Mar. 6, 1972. This application Dec. 21, 1972, ments. Ser. No. 317,455 10 Int. CI. COlb 7114, 21/44 This object as well as other objects is accomplished U.S. CI. 423—390 8 Claims according to this invention by separating radioactive iodine from nitric acid solutions using isotopic dilution, ozone sparging, and distillation while sparging with a gas ABSTRACT OF THE DISCLOSURE which will reduce nitric acid to an oxide of nitrogen. 15 A method for removing small amounts of radioactive DETAILED DESCRIPTION iodine from nitric acid solution by isotopically diluting the iodine, sparging the solution with ozone, and distilling According to this invention it has been found that the iodine from solution. sparging an isotopically diluted solution with an ozone mixture prior to distillation, produces a solution in which 20 the radioactive iodine is effectively removed upon distil- CROSS REFERENCE TO RELATED APPLICATIONS lation. -
Thermal Diffusion Shock Waves in a Linear Temperature Field And
Thermal Diffusion Shock Waves in a Linear Temperature Field and Comparison of Ultrasonic Distillation to Sparging of Liquid Mixtures by Hyeyun Jung M.Sc., Brown University 2007 B.Sc., Seoul National University 2004 A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy in The Department of Physics at Brown University PROVIDENCE, RHODE ISLAND May 2012 © Copyright 2012 by Hyeyun Jung This dissertation by Hyeyun Jung is accepted in its present form by The Department of Physics as satisfying the dissertation requirement for the degree of Doctor of Philosophy. Date Gerald Diebold, Ph.D., Advisor Recommended to the Graduate Council Date James Valles, Ph.D., Reader Date Xinsheng Sean Ling, Ph.D., Reader Approved by the Graduate Council Date Peter M. Weber, Dean of the Graduate School iii Vita Hyeyun Jung was born on November 29, 1980 in Daegu, Republic of Korea. She com- pleted her secondary education at Wonhwa Girls High School in Daegu in February of 1999. She then attended Seoul National University. She obtained a Bachelor of Science in Chemical Engineering and Physics in February of 2004. In September 2004, she began graduate studies in the Department of Physics at Brown University. She carried out her doctoral research under the supervision of Dr. Gerald J. Diebold. Her publications include: 1. Hyeyun Jung, Vitaly Gusev, Hyoungsu Baek, Yaqi Wang, and Gerald J. Diebold, "Ludwig-Soret Effect in a Linear Temperature Field: Theory and Experiments for Distributions at Long Times", Physics Letters A 375(19), 1917-1920, 2011 2. Hye Yun Jung, Han Jung Park, Joseph M. -
5310 Total Organic Carbon (Toc)*
TOTAL ORGANIC CARBON (TOC) (5310)/Introduction 5-19 5310 TOTAL ORGANIC CARBON (TOC)* 5310 A. Introduction 1. General Discussion ular, organic compounds may react with disinfectants to produce potentially toxic and carcinogenic compounds. The organic carbon in water and wastewater is composed of a To determine the quantity of organically bound carbon, the or- variety of organic compounds in various oxidation states. Some ganic molecules must be broken down and converted to a single of these carbon compounds can be oxidized further by biological molecular form that can be measured quantitatively. TOC methods or chemical processes, and the biochemical oxygen demand utilize high temperature, catalysts, and oxygen, or lower tempera- (BOD), assimilable organic carbon (AOC), and chemical oxygen tures (Ͻ100°C) with ultraviolet irradiation, chemical oxidants, or demand (COD) methods may be used to characterize these combinations of these oxidants to convert organic carbon to carbon fractions. Total organic carbon (TOC) is a more convenient and dioxide (CO2). The CO2 may be purged from the sample, dried, and direct expression of total organic content than either BOD, AOC, transferred with a carrier gas to a nondispersive infrared analyzer or or COD, but does not provide the same kind of information. If a coulometric titrator. Alternatively, it may be separated from the repeatable empirical relationship is established between TOC sample liquid phase by a membrane selective to CO2 into a high- and BOD, AOC, or COD for a specific source water then TOC purity water in which corresponding increase in conductivity is can be used to estimate the accompanying BOD, AOC, or COD. -
Compendium Method TO-15
EPA/625/R-96/010b Compendium of Methods for the Determination of Toxic Organic Compounds in Ambient Air Second Edition Compendium Method TO-15 Determination Of Volatile Organic Compounds (VOCs) In Air Collected In Specially-Prepared Canisters And Analyzed By Gas Chromatography/ Mass Spectrometry (GC/MS) Center for Environmental Research Information Office of Research and Development U.S. Environmental Protection Agency Cincinnati, OH 45268 January 1999 Method TO-15 Acknowledgements This Method was prepared for publication in the Compendium of Methods for the Determination of Toxic Organic Compounds in Ambient Air, Second Edition (EPA/625/R-96/010b), which was prepared under Contract No. 68-C3-0315, WA No. 3-10, by Midwest Research Institute (MRI), as a subcontractor to Eastern Research Group, Inc. (ERG), and under the sponsorship of the U.S. Environmental Protection Agency (EPA). Justice A. Manning, John O. Burckle, and Scott Hedges, Center for Environmental Research Information (CERI), and Frank F. McElroy, National Exposure Research Laboratory (NERL), all in the EPA Office of Research and Development, were responsible for overseeing the preparation of this method. Additional support was provided by other members of the Compendia Workgroup, which include: • John O. Burckle, EPA, ORD, Cincinnati, OH • James L. Cheney, Corps of Engineers, Omaha, NB • Michael Davis, U.S. EPA, Region 7, KC, KS • Joseph B. Elkins Jr., U.S. EPA, OAQPS, RTP, NC • Robert G. Lewis, U.S. EPA, NERL, RTP, NC • Justice A. Manning, U.S. EPA, ORD, Cincinnati, OH • William A. McClenny, U.S. EPA, NERL, RTP, NC • Frank F. McElroy, U.S. EPA, NERL, RTP, NC • Heidi Schultz, ERG, Lexington, MA • William T. -
High Performance Liquid Chromatography Method Development and Chemometric Analysis of Ecstasy and Cocaine
institlüld ictterkcnny TeicneoUiochti institute lyit (.«Ulf C*»n«lon of Technology High performance liquid chromatography method development and chemometric analysis of ecstasy and cocaine Kim McFadden Supervisors Dr. B. F. Carney, Letterkenny Institute of Technology Dr. D. O'Driscoll, Forensic Science Laboratory, Dublin Submitted to Higher bducation and Training Awards Council (HETAC) in fulfilment for the requirements for the degree of Doctor of Philosophy HPLC method development & chemomelric analysis of ecstasy & cocaine Declaration I hereby declare that the work herein, submitted for Ph.D. in Analytical Science at Letterkenny Institute of Technology, is the result of my own investigation, except where reference is made to published literature. I also certify that the material submitted in this thesis has not been previously submitted for any other qualification. Kim McFadden 1 HPLC method development & chemometric analysis of ecstasy & cocaine Table of Contents Declaration 1 Abstract 5 List of Abbreviations 7 List of Figures 10 List of Tables 14 List of Presentations and Publications 16 Acknowledgments 18 Chapter 1: Literature review. 19 1.1. Introduction. 20 1.2. Drugs of abuse. 21 1.2.1. Narcotics. 22 1.2.2. Depressants. 24 1.2.3. Stimulants. 24 1.2.4. Hallucinogens. 25 1.2.5. Ecstasy. 26 1.2.6. Cocaine. 31 1.3. Current analytical techniques for forensic drug analysis. 34 1.3.1. Spectrometric methods. 34 1.3.2. Chromatographic methods. 36 1.4. Fundamentals of High Performance Liquid Chromatography. 40 1.4.1. Chromatographic interactions. 40 1.4.2. Mobile phase. 41 1.4.3. The column. 42 1.4.4. -
Air-Sparging Remediation: a Study on Heterogeneity and Air-Mobility
AIR SPARGING REMEDIATION: A STUDY ON HETEROGENEITY AND AIR MOBILITY REDUCTION 1S.S. Di Julio and 2A.S. Drucker 1California State University, Northridge, Northridge, CA 91330; 1Phone: (805) 667-2496, 1Fax: (805) 667-7062, 1E-mail: [email protected]; 2NFESC, US Navy; 2Phone: (805) 982-4847, 2E-mail: [email protected]. ABSTRACT Contaminated groundwater is a widespread problem often requiring innovative technology to remediate. The purpose of this paper is to present the laboratory results of air sparging models. Initial tests used very fine porous media (glass beads-packed column) to represent a relatively homogeneous soil samples. Subsequent testing employed budded core samples taken from a site of interest to represent more realistic, heterogeneous samples. 1,1,1 Trichloroethane (TCA) was used as the dissolved contaminant to represent BTEX/ gasoline contamination; however, results obtained here can be applied to any NAPL-dissolved phase. A technique based on foam injection is proposed and is demonstrated to reduce air mobility. This reduction in air mobility has potential to improve contaminant removal. Laboratory results are compared with predictions of a numerical model, which is an advection-diffusion air sparge simulation model. Sensitivity analysis of the numerical model provides the range of some key parameters used to screen/evaluate air sparging as the remediation method for a given contaminated site of interest. Eventual scaleup of the model to an actual site application can be justified by the favorable results presented in this paper. Key words: remediation, air sparging, NAPL, foam BACKGROUND scopic capillary air channeling is estimated by The efficiency of air sparging as a ground- Clayton (1998) to occur at air-entry pressure of water remediation process depends to a large about 15 to 20 cm of water.