Critical Review of Volatile Organic Compound Analysis in Breath and in Vitro Cell Culture for Detection of Lung Cancer
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Transport of Dangerous Goods
ST/SG/AC.10/1/Rev.16 (Vol.I) Recommendations on the TRANSPORT OF DANGEROUS GOODS Model Regulations Volume I Sixteenth revised edition UNITED NATIONS New York and Geneva, 2009 NOTE The designations employed and the presentation of the material in this publication do not imply the expression of any opinion whatsoever on the part of the Secretariat of the United Nations concerning the legal status of any country, territory, city or area, or of its authorities, or concerning the delimitation of its frontiers or boundaries. ST/SG/AC.10/1/Rev.16 (Vol.I) Copyright © United Nations, 2009 All rights reserved. No part of this publication may, for sales purposes, be reproduced, stored in a retrieval system or transmitted in any form or by any means, electronic, electrostatic, magnetic tape, mechanical, photocopying or otherwise, without prior permission in writing from the United Nations. UNITED NATIONS Sales No. E.09.VIII.2 ISBN 978-92-1-139136-7 (complete set of two volumes) ISSN 1014-5753 Volumes I and II not to be sold separately FOREWORD The Recommendations on the Transport of Dangerous Goods are addressed to governments and to the international organizations concerned with safety in the transport of dangerous goods. The first version, prepared by the United Nations Economic and Social Council's Committee of Experts on the Transport of Dangerous Goods, was published in 1956 (ST/ECA/43-E/CN.2/170). In response to developments in technology and the changing needs of users, they have been regularly amended and updated at succeeding sessions of the Committee of Experts pursuant to Resolution 645 G (XXIII) of 26 April 1957 of the Economic and Social Council and subsequent resolutions. -
1 Transformer Oil 2 Residual Fuel Oil 3 Diesel Oil Heavy 4
1 TRANSFORMER OIL 2 RESIDUAL FUEL OIL 3 DIESEL OIL HEAVY 4 SPINDLE OIL MIXTURES CONTAINING 5 CRUDE OIL 6 MOTOR OIL 7 ROAD OIL 8 FUEL OIL NO.4 9 FUEL OIL NO.5 10 FUEL OIL NO.6 LUBRICATING OILS AND 11 BLENDING STOCKS 12 PENETRATING OIL 13 TURBINE OIL 3 14 ROOFERS FLUX 15 CRUDE OIL 16 STRAIGHT RUN RESIDUE OCTAMETHYLCYCLOTETRA 17 SILOXANE BENZENEPROPANOIC ACID, 3,5- 1,1- 3,5-BIS(1,1-DIMETHYLETHYL 18 4- ), -C7-C9 4-HYDROXY-C7-C9ALCOHOL S BRANCHED AND LINEAR 19 1- -1- 1-PHENYL-1-XYLYL ETHANE BENZENETRICARBOXYLIC 20 ACID, TRIOCTYL ESTER 21 CASTOR OIL IMIDAZOLIUM COMPOUNDS, 1- -4,5- -1- 1-BENZYL-4,5-DIHYDRO-1-(H 22 -2- YDROXYETHYL)-2-NORCOC O ALKYL, CHLORIDES 4 2-PROPENOIC ACID 2- POLYMER WITH 4- 1,1- 4-(1,1-DIMETHYLETHYL)PHE 2,5- NOL,FORMALDEHYDE, 23 2- 2,5-FURANDIONE, 65% / 2-METHYLOXIRANE AND OXIRANE (65% IN NAPHTHA/XYLENE) 24 n-PENTYL PROPIONATE 25 -2- 2-ETHYLHEXYL ACRYLATE 26 DECYL ACRYLATE 27 RAPESEED OIL RAPESEED OIL (low erucic acid 4% 28 containing less than 4% free fatty acids) RAPE SEED OIL FATTY ACID 29 METHYL ESTERS ALCOHOLS (C12-C13), C12-C13 30 PRIMARY, LINEAR AND ESSENTIALLY LINEAR 31 C13+ ALCOHOLS (C13+) 5 ALCOHOLS (C14-C18), C14-C18 32 PRIMARY, LINEAR AND ESSENTIALLY LINEAR ALCOHOLS (C8-C11), C8-C11 33 PRIMARY, LINEAR AND ESSENTIALLY LINEAR ACID OIL MIXTURE FROM SOYABEAN, CORN (maize) 34 AND SUNFLOWER OIL REFINING NAPHTHALENE CRUDE 35 (MOLTEN) 36 SOYABEAN OIL SOYBEAN OIL FATTY ACID 37 METHYL ESTER 38 BUTYLBENZENE (all isomers) 39 TALLOW 40 TALLOW FATTY ACID (2- BIS(2-ETHYLHEXYL) 41 ) TEREPHTHALATE 42 -(2- ) DI-(2-ETHYLHEXYL) -
Catalytic Pyrolysis of Plastic Wastes for the Production of Liquid Fuels for Engines
Electronic Supplementary Material (ESI) for RSC Advances. This journal is © The Royal Society of Chemistry 2019 Supporting information for: Catalytic pyrolysis of plastic wastes for the production of liquid fuels for engines Supattra Budsaereechaia, Andrew J. Huntb and Yuvarat Ngernyen*a aDepartment of Chemical Engineering, Faculty of Engineering, Khon Kaen University, Khon Kaen, 40002, Thailand. E-mail:[email protected] bMaterials Chemistry Research Center, Department of Chemistry and Center of Excellence for Innovation in Chemistry, Faculty of Science, Khon Kaen University, Khon Kaen, 40002, Thailand Fig. S1 The process for pelletization of catalyst PS PS+bentonite PP ) t e PP+bentonite s f f o % ( LDPE e c n a t t LDPE+bentonite s i m s n HDPE a r T HDPE+bentonite Gasohol 91 Diesel 4000 3500 3000 2500 2000 1500 1000 500 Wavenumber (cm-1) Fig. S2 FTIR spectra of oil from pyrolysis of plastic waste type. Table S1 Compounds in oils (%Area) from the pyrolysis of plastic wastes as detected by GCMS analysis PS PP LDPE HDPE Gasohol 91 Diesel Compound NC C Compound NC C Compound NC C Compound NC C 1- 0 0.15 Pentane 1.13 1.29 n-Hexane 0.71 0.73 n-Hexane 0.65 0.64 Butane, 2- Octane : 0.32 Tetradecene methyl- : 2.60 Toluene 7.93 7.56 Cyclohexane 2.28 2.51 1-Hexene 1.05 1.10 1-Hexene 1.15 1.16 Pentane : 1.95 Nonane : 0.83 Ethylbenzen 15.07 11.29 Heptane, 4- 1.81 1.68 Heptane 1.26 1.35 Heptane 1.22 1.23 Butane, 2,2- Decane : 1.34 e methyl- dimethyl- : 0.47 1-Tridecene 0 0.14 2,2-Dimethyl- 0.63 0 1-Heptene 1.37 1.46 1-Heptene 1.32 1.35 Pentane, -
General Disclaimer One Or More of the Following Statements May Affect
General Disclaimer One or more of the Following Statements may affect this Document This document has been reproduced from the best copy furnished by the organizational source. It is being released in the interest of making available as much information as possible. This document may contain data, which exceeds the sheet parameters. It was furnished in this condition by the organizational source and is the best copy available. This document may contain tone-on-tone or color graphs, charts and/or pictures, which have been reproduced in black and white. This document is paginated as submitted by the original source. Portions of this document are not fully legible due to the historical nature of some of the material. However, it is the best reproduction available from the original submission. Produced by the NASA Center for Aerospace Information (CASI) NASA CR - 159480 EXXON/GRUS. 1KWD. 78 NIGH PERFORMANCE, HIGH DENSITY HYDROCARBON FUELS J. W. Frankenfeld, T. W. Hastings, M. Lieberman and W. F. Taylor EXXON RESEARCH AND ENGINEERING COMPANY prepared for NATIONAL AERONAUTICS AND SPACE ADMINISTRATION (NASA-CR-159''PO) HIGH PEPPOFMANCF, HIGH V79-20267 DENSTTv HYDR I-CARBON FTIELS (Exxon P.esearch and Engineering Co.) 239 rp HC A11/MF A01 CSCL 21D 'Inclas G3/28 19456 NASA Lewis Research Center Contract NAS 3-20394 Qnr{l,,Y^ ^'Pr I€ ^i NASA CR - 159480 EXXON/GRUS . 1KWD . 78 L: HIGH PERFORMANCE, HIGH DENSITY HYDROCARBON FUELS J. W. Frankenfeld, T. W. Hastings, M. Lieberman and W. F. Taylor EXXON RESEARCH AND ENGINEERING COMPANY prepared for NATIONAL AERONAUTICS AND SPACE ADMINISTRATION NASA Lewis Research Center Contract NAS 3-20394 FOREWARD The research described in this report was performed at Exxon Research and Engineering Company, Linden, New Jersey and Contract NAS 320394 with Mr. -
Dibasic Acids for Nylon Manufacture
- e Report No. 75 DIBASIC ACIDS FOR NYLON MANUFACTURE by YEN-CHEN YEN October 1971 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA CONTENTS INTRODUCTION, ....................... 1 SUMMARY .......................... 3 General Aspects ...................... 3 Technical Aspects ..................... 7 INDUSTRY STATUS ...................... 15 Applications and Consumption of Sebacic Acid ........ 15 Applications and Consumption of Azelaic Acid ........ 16 Applications of Dodecanedioic and Suberic Acids ...... 16 Applications of Cyclododecatriene and Cyclooctadiene .... 17 Producers ......................... 17 Prices ........................... 18 DIBASIC ACIDS FOR MANUFACTURE OF POLYAMIDES ........ 21 CYCLOOLIGOMERIZATIONOF BUTADIENE ............. 29 Chemistry ......................... 29 Ziegler Catalyst ..................... 30 Nickel Catalyst ..................... 33 Other Catalysts ..................... 34 Co-Cyclooligomerization ................. 34 Mechanism ........................ 35 By-products and Impurities ................ 37 Review of Processes .................... 38 A Process for Manufacture of Cyclododecatriene ....... 54 Process Description ................... 54 Process Discussion .................... 60 Cost Estimates ...................... 60 A Process for Manufacture of Cyclooctadiene ........ 65 Process Description ................... 65 Process Discussion .................... 70 Cost Estimates ...................... 70 A Process for Manufacture of Cyclodecadiene -
Analysis of Volatile Organic Compounds in Exhaled Breath for Lung Cancer Diagnosis Using a Sensor System
The University of Manchester Research Analysis of volatile organic compounds in exhaled breath for lung cancer diagnosis using a sensor system DOI: 10.1016/j.snb.2017.08.057 Document Version Accepted author manuscript Link to publication record in Manchester Research Explorer Citation for published version (APA): Chang, J-E., Lee, D-S., Ban, S-W., Oh, J., Jung, M. Y., Kim, S-H., Park, S., Persaud, K., & Jheon, S. (2017). Analysis of volatile organic compounds in exhaled breath for lung cancer diagnosis using a sensor system. Sensors and Actuators B: Chemical: international journal devoted to research and development of physical and chemical transducers, 255(1), 800-807. https://doi.org/10.1016/j.snb.2017.08.057 Published in: Sensors and Actuators B: Chemical: international journal devoted to research and development of physical and chemical transducers Citing this paper Please note that where the full-text provided on Manchester Research Explorer is the Author Accepted Manuscript or Proof version this may differ from the final Published version. If citing, it is advised that you check and use the publisher's definitive version. General rights Copyright and moral rights for the publications made accessible in the Research Explorer are retained by the authors and/or other copyright owners and it is a condition of accessing publications that users recognise and abide by the legal requirements associated with these rights. Takedown policy If you believe that this document breaches copyright please refer to the University of Manchester’s Takedown Procedures [http://man.ac.uk/04Y6Bo] or contact [email protected] providing relevant details, so we can investigate your claim. -
Synthetic Turf Scientific Advisory Panel Meeting Materials
California Environmental Protection Agency Office of Environmental Health Hazard Assessment Synthetic Turf Study Synthetic Turf Scientific Advisory Panel Meeting May 31, 2019 MEETING MATERIALS THIS PAGE LEFT BLANK INTENTIONALLY Office of Environmental Health Hazard Assessment California Environmental Protection Agency Agenda Synthetic Turf Scientific Advisory Panel Meeting May 31, 2019, 9:30 a.m. – 4:00 p.m. 1001 I Street, CalEPA Headquarters Building, Sacramento Byron Sher Auditorium The agenda for this meeting is given below. The order of items on the agenda is provided for general reference only. The order in which items are taken up by the Panel is subject to change. 1. Welcome and Opening Remarks 2. Synthetic Turf and Playground Studies Overview 4. Synthetic Turf Field Exposure Model Exposure Equations Exposure Parameters 3. Non-Targeted Chemical Analysis Volatile Organics on Synthetic Turf Fields Non-Polar Organics Constituents in Crumb Rubber Polar Organic Constituents in Crumb Rubber 5. Public Comments: For members of the public attending in-person: Comments will be limited to three minutes per commenter. For members of the public attending via the internet: Comments may be sent via email to [email protected]. Email comments will be read aloud, up to three minutes each, by staff of OEHHA during the public comment period, as time allows. 6. Further Panel Discussion and Closing Remarks 7. Wrap Up and Adjournment Agenda Synthetic Turf Advisory Panel Meeting May 31, 2019 THIS PAGE LEFT BLANK INTENTIONALLY Office of Environmental Health Hazard Assessment California Environmental Protection Agency DRAFT for Discussion at May 2019 SAP Meeting. Table of Contents Synthetic Turf and Playground Studies Overview May 2019 Update ..... -
The Enthalpy of Formation of Organic Compounds with “Chemical Accuracy”
chemengineering Article Group Contribution Revisited: The Enthalpy of Formation of Organic Compounds with “Chemical Accuracy” Robert J. Meier Pro-Deo Consultant, 52525 Heinsberg, North-Rhine Westphalia, Germany; [email protected] Abstract: Group contribution (GC) methods to predict thermochemical properties are of eminent importance to process design. Compared to previous works, we present an improved group contri- bution parametrization for the heat of formation of organic molecules exhibiting chemical accuracy, i.e., a maximum 1 kcal/mol (4.2 kJ/mol) difference between the experiment and model, while, at the same time, minimizing the number of parameters. The latter is extremely important as too many parameters lead to overfitting and, therewith, to more or less serious incorrect predictions for molecules that were not within the data set used for parametrization. Moreover, it was found to be important to explicitly account for common chemical knowledge, e.g., geminal effects or ring strain. The group-related parameters were determined step-wise: first, alkanes only, and then only one additional group in the next class of molecules. This ensures unique and optimal parameter values for each chemical group. All data will be made available, enabling other researchers to extend the set to other classes of molecules. Keywords: enthalpy of formation; thermodynamics; molecular modeling; group contribution method; quantum mechanical method; chemical accuracy; process design Citation: Meier, R.J. Group Contribution Revisited: The Enthalpy of Formation of Organic Compounds with “Chemical Accuracy”. 1. Introduction ChemEngineering 2021, 5, 24. To understand chemical reactivity and/or chemical equilibria, knowledge of thermo- o https://doi.org/10.3390/ dynamic properties such as gas-phase standard enthalpy of formation DfH gas is a necessity. -
Vapor Pressures and Vaporization Enthalpies of the N-Alkanes from C31 to C38 at T ) 298.15 K by Correlation Gas Chromatography
BATCH: je3a29 USER: ckt69 DIV: @xyv04/data1/CLS_pj/GRP_je/JOB_i03/DIV_je030236t DATE: March 15, 2004 1 Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from 2 C31 to C38 at T ) 298.15 K by Correlation Gas Chromatography 3 James S. Chickos* and William Hanshaw 4 Department of Chemistry and Biochemistry, University of MissourisSt. Louis, St. Louis, Missouri 63121, USA 5 6 The temperature dependence of gas-chromatographic retention times for henitriacontane to octatriacontane 7 is reported. These data are used in combination with other literature values to evaluate the vaporization 8 enthalpies and vapor pressures of these n-alkanes from T ) 298.15 to 575 K. The vapor pressure and 9 vaporization enthalpy results obtained are compared with existing literature data where possible and 10 found to be internally consistent. The vaporization enthalpies and vapor pressures obtained for the 11 n-alkanes are also tested directly and through the use of thermochemical cycles using literature values 12 for several polyaromatic hydrocarbons. Sublimation enthalpies are also calculated for hentriacontane to 13 octatriacontane by combining vaporization enthalpies with temperature adjusted fusion enthalpies. 14 15 Introduction vaporization enthalpies of C21 to C30 to include C31 to C38. 54 The vapor pressures and vaporization enthalpies of these 55 16 Polycyclic aromatic hydrocarbons (PAHs) are important larger n-alkanes have been evaluated using the technique 56 17 environmental contaminants, many of which exhibit very of correlation gas chromatography. This technique relies 57 18 low vapor pressures. In the gas phase, they exist mainly entirely on the use of standards in assessment. Standards 58 19 sorbed to aerosol particles. -
Measurements of Higher Alkanes Using NO Chemical Ionization in PTR-Tof-MS
Atmos. Chem. Phys., 20, 14123–14138, 2020 https://doi.org/10.5194/acp-20-14123-2020 © Author(s) 2020. This work is distributed under the Creative Commons Attribution 4.0 License. Measurements of higher alkanes using NOC chemical ionization in PTR-ToF-MS: important contributions of higher alkanes to secondary organic aerosols in China Chaomin Wang1,2, Bin Yuan1,2, Caihong Wu1,2, Sihang Wang1,2, Jipeng Qi1,2, Baolin Wang3, Zelong Wang1,2, Weiwei Hu4, Wei Chen4, Chenshuo Ye5, Wenjie Wang5, Yele Sun6, Chen Wang3, Shan Huang1,2, Wei Song4, Xinming Wang4, Suxia Yang1,2, Shenyang Zhang1,2, Wanyun Xu7, Nan Ma1,2, Zhanyi Zhang1,2, Bin Jiang1,2, Hang Su8, Yafang Cheng8, Xuemei Wang1,2, and Min Shao1,2 1Institute for Environmental and Climate Research, Jinan University, 511443 Guangzhou, China 2Guangdong-Hongkong-Macau Joint Laboratory of Collaborative Innovation for Environmental Quality, 511443 Guangzhou, China 3School of Environmental Science and Engineering, Qilu University of Technology (Shandong Academy of Sciences), 250353 Jinan, China 4State Key Laboratory of Organic Geochemistry and Guangdong Key Laboratory of Environmental Protection and Resources Utilization, Guangzhou Institute of Geochemistry, Chinese Academy of Sciences, 510640 Guangzhou, China 5State Joint Key Laboratory of Environmental Simulation and Pollution Control, College of Environmental Sciences and Engineering, Peking University, 100871 Beijing, China 6State Key Laboratory of Atmospheric Boundary Physics and Atmospheric Chemistry, Institute of Atmospheric Physics, Chinese -
Supporting Information for Modeling the Formation and Composition Of
Supporting Information for Modeling the Formation and Composition of Secondary Organic Aerosol from Diesel Exhaust Using Parameterized and Semi-explicit Chemistry and Thermodynamic Models Sailaja Eluri1, Christopher D. Cappa2, Beth Friedman3, Delphine K. Farmer3, and Shantanu H. Jathar1 1 Department of Mechanical Engineering, Colorado State University, Fort Collins, CO, USA, 80523 2 Department of Civil and Environmental Engineering, University of California Davis, Davis, CA, USA, 95616 3 Department of Chemistry, Colorado State University, Fort Collins, CO, USA, 80523 Correspondence to: Shantanu H. Jathar ([email protected]) Table S1: Mass speciation and kOH for VOC emissions profile #3161 3 -1 - Species Name kOH (cm molecules s Mass Percent (%) 1) (1-methylpropyl) benzene 8.50×10'() 0.023 (2-methylpropyl) benzene 8.71×10'() 0.060 1,2,3-trimethylbenzene 3.27×10'(( 0.056 1,2,4-trimethylbenzene 3.25×10'(( 0.246 1,2-diethylbenzene 8.11×10'() 0.042 1,2-propadiene 9.82×10'() 0.218 1,3,5-trimethylbenzene 5.67×10'(( 0.088 1,3-butadiene 6.66×10'(( 0.088 1-butene 3.14×10'(( 0.311 1-methyl-2-ethylbenzene 7.44×10'() 0.065 1-methyl-3-ethylbenzene 1.39×10'(( 0.116 1-pentene 3.14×10'(( 0.148 2,2,4-trimethylpentane 3.34×10'() 0.139 2,2-dimethylbutane 2.23×10'() 0.028 2,3,4-trimethylpentane 6.60×10'() 0.009 2,3-dimethyl-1-butene 5.38×10'(( 0.014 2,3-dimethylhexane 8.55×10'() 0.005 2,3-dimethylpentane 7.14×10'() 0.032 2,4-dimethylhexane 8.55×10'() 0.019 2,4-dimethylpentane 4.77×10'() 0.009 2-methylheptane 8.28×10'() 0.028 2-methylhexane 6.86×10'() -
Vapor Pressures and Vaporization Enthalpies of the N-Alkanes from 2 C21 to C30 at T ) 298.15 K by Correlation Gas Chromatography
BATCH: je1a04 USER: jeh69 DIV: @xyv04/data1/CLS_pj/GRP_je/JOB_i01/DIV_je0301747 DATE: October 17, 2003 1 Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from 2 C21 to C30 at T ) 298.15 K by Correlation Gas Chromatography 3 James S. Chickos* and William Hanshaw 4 Department of Chemistry and Biochemistry, University of MissourisSt. Louis, St. Louis, Missouri 63121 5 6 The temperature dependence of gas chromatographic retention times for n-heptadecane to n-triacontane 7 is reported. These data are used to evaluate the vaporization enthalpies of these compounds at T ) 298.15 8 K, and a protocol is described that provides vapor pressures of these n-alkanes from T ) 298.15 to 575 9 K. The vapor pressure and vaporization enthalpy results obtained are compared with existing literature 10 data where possible and found to be internally consistent. Sublimation enthalpies for n-C17 to n-C30 are 11 calculated by combining vaporization enthalpies with fusion enthalpies and are compared when possible 12 to direct measurements. 13 14 Introduction 15 The n-alkanes serve as excellent standards for the 16 measurement of vaporization enthalpies of hydrocarbons.1,2 17 Recently, the vaporization enthalpies of the n-alkanes 18 reported in the literature were examined and experimental 19 values were selected on the basis of how well their 20 vaporization enthalpies correlated with their enthalpies of 21 transfer from solution to the gas phase as measured by gas 22 chromatography.3 A plot of the vaporization enthalpies of 23 the n-alkanes as a function of the number of carbon atoms 24 is given in Figure 1.