Pahs in Coal Tar Sealants: Policy Analyses and Design Abigail Rose Ames
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Minutes of the IUPAC Chemical Nomenclature and Structure Representation Division (VIII) Committee Meeting Boston, MA, USA, August 18, 2002
Minutes of the IUPAC Chemical Nomenclature and Structure Representation Division (VIII) Committee Meeting Boston, MA, USA, August 18, 2002 Members Present: Dr Stephen Heller, Prof Herbert Kaesz, Prof Dr Alexander Lawson, Prof G. Jeffrey Leigh, Dr Alan McNaught (President), Dr. Gerard Moss, Prof Bruce Novak, Dr Warren Powell (Secretary), Dr William Town, Dr Antony Williams Members Absent: Dr. Michael Dennis, Prof Michael Hess National representatives Present: Prof Roberto de Barros Faria (Brazil) The second meeting of the Division Committee of the IUPAC Division of Chemical Nomenclature and Structure Representation held in the Great Republic Room of the Westin Hotel in Boston, Massachusetts, USA was convened by President Alan McNaught at 9:00 a.m. on Sunday, August 18, 2002. 1.0 President McNaught welcomed the members to this meeting in Boston and offered a special welcome to the National Representative from Brazil, Prof Roberto de Barros Faria. He also noted that Dr Michael Dennis and Prof Michael Hess were unable to be with us. Each of the attendees introduced himself and provided a brief bit of background information. Housekeeping details regarding breaks and lunch were announced and an invitation to a reception from the U. S. National Committee for IUPAC on Tuesday, August 20 was noted. 2.0 The agenda as circulated was approved with the addition of a report from Dr Moss on the activity on his website. 3.0 The minutes of the Division Committee Meeting in Cambridge, UK, January 25, 2002 as posted on the Webboard (http://www.rsc.org/IUPAC8/attachments/MinutesDivCommJan2002.rtf and http://www.rsc.org/IUPAC8/attachments/MinutesDivCommJan2002.pdf) were approved with the following corrections: 3.1 The name Dr Gerard Moss should be added to the members present listing. -
An Empirical Study on Laboratory Coke Oven-Based Coal Blending for Coking with Tar Residue, Chemical Engineering Transactions, 71, 385-390 DOI:10.3303/CET1871065 386
385 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 71, 2018 The Italian Association of Chemical Engineering Online at www.aidic.it/cet Guest Editors: Xiantang Zhang, Songrong Qian, Jianmin Xu Copyright © 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-68-6; ISSN 2283-9216 DOI: 10.3303/CET1871065 An Empirical Study on Laboratory Coke Oven-based Coal Blending for Coking with Tar Residue Wenqiu Liu Hebei Energy College of Vocation and Technology, Tangshan 063004, China [email protected] Tar residue is the solid waste produced in coking plants or gas generators. Utilizing tar residue as additive in coal blending for coking is an effective approach for coal coking in our country, not only improving the yield and nature of coking products, but also realizing the recycling of tar residue. In this paper, tar residue is used as additive in coal blending for coking experiments, and combined with experiments on the crucible coke, small coke oven and industrial coke oven, the influences of the addition amount of tar residue on coke yield, coke reactivity and coke strength after reaction are further analyzed. As the experiment results reveal, compared to the experiment results of crucible coke and small coke ovens, the coke yield, coke reactivity and coke strength after reaction of industrial coke ovens are all bigger, leading to potential industrialization of coal blending for coking. Moreover, the influence of the amount of tar residue on the coal tar yield rate and gas yield is the same as that of coke reactivity and coke strength after reaction. 1. Introduction With the rapid development of economy, the fast growth of iron and steel industry has led China's coke industry to accomplish extraordinary achievements (Si et al., 2017). -
Polycyclic Aromatic Hydrocarbon Structure Index
NIST Special Publication 922 Polycyclic Aromatic Hydrocarbon Structure Index Lane C. Sander and Stephen A. Wise Chemical Science and Technology Laboratory National Institute of Standards and Technology Gaithersburg, MD 20899-0001 December 1997 revised August 2020 U.S. Department of Commerce William M. Daley, Secretary Technology Administration Gary R. Bachula, Acting Under Secretary for Technology National Institute of Standards and Technology Raymond G. Kammer, Director Polycyclic Aromatic Hydrocarbon Structure Index Lane C. Sander and Stephen A. Wise Chemical Science and Technology Laboratory National Institute of Standards and Technology Gaithersburg, MD 20899 This tabulation is presented as an aid in the identification of the chemical structures of polycyclic aromatic hydrocarbons (PAHs). The Structure Index consists of two parts: (1) a cross index of named PAHs listed in alphabetical order, and (2) chemical structures including ring numbering, name(s), Chemical Abstract Service (CAS) Registry numbers, chemical formulas, molecular weights, and length-to-breadth ratios (L/B) and shape descriptors of PAHs listed in order of increasing molecular weight. Where possible, synonyms (including those employing alternate and/or obsolete naming conventions) have been included. Synonyms used in the Structure Index were compiled from a variety of sources including “Polynuclear Aromatic Hydrocarbons Nomenclature Guide,” by Loening, et al. [1], “Analytical Chemistry of Polycyclic Aromatic Compounds,” by Lee et al. [2], “Calculated Molecular Properties of Polycyclic Aromatic Hydrocarbons,” by Hites and Simonsick [3], “Handbook of Polycyclic Hydrocarbons,” by J. R. Dias [4], “The Ring Index,” by Patterson and Capell [5], “CAS 12th Collective Index,” [6] and “Aldrich Structure Index” [7]. In this publication the IUPAC preferred name is shown in large or bold type. -
Estimation of Enthalpy of Bio-Oil Vapor and Heat Required For
Edinburgh Research Explorer Estimation of Enthalpy of Bio-Oil Vapor and Heat Required for Pyrolysis of Biomass Citation for published version: Yang, H, Kudo, S, Kuo, H-P, Norinaga, K, Mori, A, Masek, O & Hayashi, J 2013, 'Estimation of Enthalpy of Bio-Oil Vapor and Heat Required for Pyrolysis of Biomass', Energy & Fuels, vol. 27, no. 5, pp. 2675-2686. https://doi.org/10.1021/ef400199z Digital Object Identifier (DOI): 10.1021/ef400199z Link: Link to publication record in Edinburgh Research Explorer Document Version: Early version, also known as pre-print Published In: Energy & Fuels General rights Copyright for the publications made accessible via the Edinburgh Research Explorer is retained by the author(s) and / or other copyright owners and it is a condition of accessing these publications that users recognise and abide by the legal requirements associated with these rights. Take down policy The University of Edinburgh has made every reasonable effort to ensure that Edinburgh Research Explorer content complies with UK legislation. If you believe that the public display of this file breaches copyright please contact [email protected] providing details, and we will remove access to the work immediately and investigate your claim. Download date: 04. Oct. 2021 Estimation of Enthalpy of Bio-oil Vapor and Heat Required for Pyrolysis of Biomass Hua Yang,† Shinji Kudo,§ Hsiu-Po Kuo,‡ Koyo Norinaga, ξ Aska Mori, ξ Ondřej Mašek,|| and Jun-ichiro Hayashi †, ξ, §, * †Interdisciplinary Graduate School of Engineering Sciences, Kyushu University, -
Coal Characteristics
CCTR Indiana Center for Coal Technology Research COAL CHARACTERISTICS CCTR Basic Facts File # 8 Brian H. Bowen, Marty W. Irwin The Energy Center at Discovery Park Purdue University CCTR, Potter Center, 500 Central Drive West Lafayette, IN 47907-2022 http://www.purdue.edu/dp/energy/CCTR/ Email: [email protected] October 2008 1 Indiana Center for Coal Technology Research CCTR COAL FORMATION As geological processes apply pressure to peat over time, it is transformed successively into different types of coal Source: Kentucky Geological Survey http://images.google.com/imgres?imgurl=http://www.uky.edu/KGS/coal/images/peatcoal.gif&imgrefurl=http://www.uky.edu/KGS/coal/coalform.htm&h=354&w=579&sz= 20&hl=en&start=5&um=1&tbnid=NavOy9_5HD07pM:&tbnh=82&tbnw=134&prev=/images%3Fq%3Dcoal%2Bphotos%26svnum%3D10%26um%3D1%26hl%3Den%26sa%3DX 2 Indiana Center for Coal Technology Research CCTR COAL ANALYSIS Elemental analysis of coal gives empirical formulas such as: C137H97O9NS for Bituminous Coal C240H90O4NS for high-grade Anthracite Coal is divided into 4 ranks: (1) Anthracite (2) Bituminous (3) Sub-bituminous (4) Lignite Source: http://cc.msnscache.com/cache.aspx?q=4929705428518&lang=en-US&mkt=en-US&FORM=CVRE8 3 Indiana Center for Coal Technology Research CCTR BITUMINOUS COAL Bituminous Coal: Great pressure results in the creation of bituminous, or “soft” coal. This is the type most commonly used for electric power generation in the U.S. It has a higher heating value than either lignite or sub-bituminous, but less than that of anthracite. Bituminous coal -
Coal Tar Pitch – Its Past, Present and Future in Commercial Roofing by Joe Mellott
- 1 - Coal Tar Pitch – Its Past, Present and Future in Commercial Roofing By Joe Mellott Coal tar remains a desired and strong source of technology within the roofing industry, as innovative coal tar products significantly reduce associated health hazards and environmental impact. To help you better understand the role that coal tar continues to play in the commercial roofing market, this article will explore: • The history of coal tar • Its associated hazards • Hot and cold coal tar adhesive technologies • Modified coal tar pitch membrane technologies • Coal tar’s sustainability attributes A Brief History of Coal Tar In order to understand what coal tar pitch is, it’s important to understand its origins and refinement methods. Coal tar can be refined from a number of sources including coal, wood, peat, petroleum, and other organic materials. The tar is removed by burning or heating the base substance and selectively distilling fractions of the burned chemical. Distillation involves heating the substance to a point where different fractions of the substance become volatile. The fractions are then collected by condensing the fraction at a specific temperature. A base substance can be split into any number of fractions through distillation. A good example of industrial distillation is the oil refining process. Through distillation, crude oil can be separated into fractions that include gasoline, jet fuel, motor oil bases, and other specialty chemicals. Fractionation or distillation is a tried-and-true method for breaking a substance into different parts of its composition. One of the first uses of coal tar was in the maritime industry. Trees stumps were burned and the tar fractions were collected through distillation of the tar. -
Spherical Graphite Produced by Waste Semi-Coke with Enhanced Properties As
Electronic Supplementary Material (ESI) for Sustainable Energy & Fuels. This journal is © The Royal Society of Chemistry 2019 Spherical graphite produced by waste semi-coke with enhanced properties as anode material for Li-ion batteries Ming Shi, Zige Tai, Na Li, Kunyang Zou, Yuanzhen Chen, Junjie Sun, Yongning Liu* State Key Laboratory for Mechanical Behavior of Materials, School of Material Science and Engineering, Xi’an Jiaotong University, Xi’an 710049, PR China *Corresponding author E-mail address: [email protected] Fax: +86 29 8266 3453; Tel: +86 29 8266 4602 Fig. 1 N2 absorption/desorption profiles of (a) pristine semi-coke (SC); (b) synthetic graphite without Si (PG); and (c) synthetic graphite with 10% Si at 2300 °C (SG). Table 1 The percentage of impurity of pristine SC and SG (10% Si at 2300 °C). Content percentage / wt % samples B Si Al Ca Fe K Na Mg SC <0.1 4.25 5.5 3.3 0.8 0.3 0.09 <0.1 SG <0.1 1.01 1.9 0.1 <0.1 0.02 0.03 <0.1 Table 2 The SG capacity values with that of similar materials published in the literature. Materials Specific Capacity Rate capability Cyclic retention Ref. [mA h g-1] [mA h g-1] Spherical graphite produced 347.06 at 0.05C 329.8 at 0.1C; 317.4 at 97.7% at 0.5C after This by waste semi-coke 0.5 C and 262.3 at 1C 700 cycles work Iron‐catalyzed graphitic 306 at 0.1C 150 at rate of 2C Over 90 % after 200 1 materials from biomass cycles Carbonaceous composites 312 at 0.2C 149 at 1 C; 78 at 5C - 2 prepared by the mixture of graphite, cokes, and petroleum pitch. -
Lecture 32: Coke Production
NPTEL – Chemical – Chemical Technology II Lecture 32: Coke production 32.1 Introduction Coal is used as fuel for electric power generation, industrial heating and steam generation, domestic heating, rail roads and for coal processing. Coal composition is denoted by rank. Rank increases with the carbon content and decreases with increasing oxygen content. Many of the products made by hydrogenation, oxidation, hydrolysis or fluorination are important for industrial use. Stable, low cost, petroleum and natural gas supplies has arose interest in some of the coal products as upgraded fuels to reduce air pollution as well as to take advantage of greater ease of handling of the liquid or gaseous material and to utilize existing facilities such as pipelines and furnaces. 32.2 Coking of coal Raw material is Bituminous coal. It appears to have specific internal surfaces in the range of 30 to 100m2/g. Generally one ton of bituminous coal produces 1400 lb of coke. 10 gallons of tar. Chemical reaction:- 4(C3H4)n nC6H6 + 5nC + 3nH2 + nCH4 Coal Benzene Coke Lighter hydrocarbon Joint initiative of IITs and IISc – Funded by MHRD Page 1 of 9 NPTEL – Chemical – Chemical Technology II Process flow sheet: Illustrated in Figure. Figure 32.1 Flow sheet of coking of coal 32.3 Functional role of each unit (Figure 32.1): (a) Coal crusher and screening: At first Bituminous coal is crushed and screened to a certain size. Preheating of coal (at 150-250˚C) is done to reduce coking time without loss of coal quality. Briquetting increases strength of coke produced and to make non - coking or poorly coking coals to be used as metallurgical coke. -
Projectprofile
EPSILON CARBON PRIVATE LIMITED ECPL CoalTar Distillation -300,000tpa Karnataka ProjectProfile General TheEpsilon CarbonprivateLimited is aspiring to emergeasadynamiccompanyin India in the field of coal tar processing for manufacture ofvarious value added products. The proposed green-field Coal tar distillation plant coupledwith solidpitchmeltingunitisproposedtosetupwith Coal tar processing capacity of 300,000tpaat Toranagallu in Bellary district of Karnataka. Process Description: The coal tar are separated by distillation process. Coal tar containing several chemical compounds with major being Coal tar pitch,Naphthalene,Wash Oil, Light Oil, Phenol Oil & Anthracene oil. Following are major manufacturing of process & Products: 1. Coal Tar pitch (Binder Grade Pitch) 2. Zero QI /Impregnated Pitch 3. Naphthalene &Naphthalene sulfonate formaldehyde (NSF) 4. Oils- Carbon Black Oil (CBO) ,Light oil, Phenol oil, Wash oil , Anthracene oil By Products: 5. Sodium Phenolate 6. Ammonical water 1. Binder Grade Pitch: Soft Pitch from the bottom of pitch column is sent to pitch column for further processing to modified pitch to increase QI content and blended with required high QI pitch to produce binder grade pitch for aluminum industry. 2. Impregnated Pitch : Blending of coal tar and wash oil in specific ratio, dehydration up to 180℃ to separate moisture content in coal tar. The dehydrated mixture is transferred to settling tank for reduction of QI. (Settling tank provide draw-off valve for QI sampling). QI value less material transfer to further distillation (Removal of Oils) to produce Impregnated Pitch. Project Profile for 300,000 tpa Coal Tar Distillation plant EPSILON CARBON PRIVATE LIMITED ECPL CoalTar Distillation -300,000tpa Karnataka ProjectProfile 3. Carbon Black Oil(CBO): Blending of Soft Pitch from the bottom of pitch column and Anthracene oil in specific ratio with required specific gravity to produce carbon black oil for tyre industry. -
Interpreting Tar Patterns at Former Manufactured Gas Plant Sites
1 Interpreting Tar Patterns at Former Manufactured Gas Plant Sites Brian L. Murphy, Ph.D. • INEF, Penn State • June 10, 2013 2 Why focus on tar? . Dense, nonaqueous-phase liquid (DNAPL) that can sink into the saturated zone and contaminate groundwater – Expensive to remediate . Insurance coverage litigation – How tar got there? (Expected and intended?) – When tar got there? (During coverage period?) – Is it still moving? (During coverage period?) 3 Outline . What is manufactured gas plant (MGP) tar? . How “tarry” is it? . How fast does it move? – Distance and time scales . How to interpret boring logs in terms of tar motion . How can you identify source locations at a site where tar has migrated? 4 Nomenclature . “Tar” generally = Density > Water . “Oil” generally = Density < Water . “Coal tar” = Tar from different processes – Coal gasification – Water gas – Carbureted water gas – Oil gas Which may not involve the use of coal at all! 5 Different Processes for Manufacturing Gas . Coal gas: Heat coal in the absence of oxygen . Water gas (blue gas): Steam sprayed on incandescent coke H2O+C→CO+H2 . Carbureted water gas: Petroleum is cracked and added to water gas—most popular Lowe process . Oil gas: Cracked petroleum for low molecular weight gases 6 Initial Coal Gas Period . 1812: First commercial plant chartered, London . First U.S. gas companies incorporated – 1817 Baltimore – 1823 New York – 1829 Boston 7 Advent of Water Gas . 1873: Lowe Carbureted Water Gas (CWG) Process patented; water gas provided superior illumination – 1884: Patents sold to United Gas Improvement Company – 1892: Lowe’s patents begin to expire . 1900: CWG accounts for 75% of U.S. -
Temperature-Induced Oligomerization of Polycyclic Aromatic Hydrocarbons
www.nature.com/scientificreports OPEN Temperature-induced oligomerization of polycyclic aromatic hydrocarbons at ambient Received: 7 June 2017 Accepted: 10 July 2017 and high pressures Published: xx xx xxxx Artem D. Chanyshev 1,2, Konstantin D. Litasov1,2, Yoshihiro Furukawa3, Konstantin A. Kokh1,2 & Anton F. Shatskiy1,2 Temperature-induced oligomerization of polycyclic aromatic hydrocarbons (PAHs) was found at 500–773 K and ambient and high (3.5 GPa) pressures. The most intensive oligomerization at 1 bar and 3.5 GPa occurs at 740–823 K. PAH carbonization at high pressure is the fnal stage of oligomerization and occurs as a result of sequential oligomerization and polymerization of the starting material, caused by overlapping of π-orbitals, a decrease of intermolecular distances, and fnally the dehydrogenation and polycondensation of benzene rings. Being important for building blocks of life, PAHs and their oligomers can be formed in the interior of the terrestrial planets with radii less than 2270 km. High-pressure transformations of polycyclic aromatic hydrocarbons (PAHs) and benzene become extremely important due to wide applications for example in graphene- and graphene-based nanotechnology1–3, synthesis of organic superconductors4, 5, petroleum geoscience, origin of organic molecules in Universe and origin of life. In particular, PAHs were found in many space objects: meteorites6–8, cometary comae9, interstellar clouds and planetary nebulas10–12. Although the prevalent hypothesis for the formation of these PAHs is irradiation-driven polymerization of smaller hydrocarbons13, alternative explanation could be shock fragmentation of carbonaceous solid material11. PAH-bearing carbonaceous material could contribute to the delivery of extraterrestrial organic materials to the prebiotic Earth during the period of heavy bombardment of the inner Solar System from 4.5 to 3.8 Ga ago14–16. -
Summary of Information for ABC for Polycyclic Aromatic Hydrocarbons
Air Toxics Science Advisory Committee Summary of Information for ABC for Polycyclic Aromatic Hydrocarbons September 16, 2015 ATSAC Meeting #10 Presenter: Sue MacMillan, DEQ ATSAC lead Sue MacMillan | Oregon Department of Environmental Quality 26 Individual PAHs to Serve as Basis of ABC for Total PAHs Acenaphthene Cyclopenta(c,d)pyrene Acenaphthylene Dibenzo(a,h)anthracene Anthracene Dibenzo(a,e)pyrene Anthanthrene Dibenzo(a,h)pyrene Benzo(a)pyrene Dibenzo(a,i)pyrene Naphthalene Benz(a)anthracene Dibenzo(a,l)pyrene has separate Benzo(b)fluoranthene Fluoranthene ABC. Benzo(k)fluoranthene Fluorene Benzo( c)pyrene Indeno(1,2,3-c,d)pyrene Benzo(e)pyrene Phenanthrene Benzo(g,h,i)perylene Pyrene Benzo(j)fluoranthene 5-Methylchrysene Chrysene 6-Nitrochrysene Use of Toxic Equivalency Factors for PAHs • Benzo(a)pyrene serves as the index PAH, and has a documented toxicity value to which other PAHs are adjusted • Other PAHs adjusted using Toxic Equivalency Factors (TEFs), aka Potency Equivalency Factors (PEFs). These values are multipliers and are PAH-specific. • Once all PAH concentrations are adjusted to account for their relative toxicity as compared to BaP, the concentrations are summed • This summed concentration is then compared to the toxicity value for BaP, which is used as the ABC for total PAHs. Source of PEFs for PAHs • EPA provides a range of values of PEFs for each PAH • Original proposal suggested using upper-bound value of each PEF range as the PEF to use for adjustment of our PAHs • Average PEF value for each PAH is a better approximation of central tendency, and is consistent with the use of PEFs by other agencies • Result of using average, rather than upper-bound PEFs: slightly lower summed concentrations for adjusted PAHs, thus less apt to exceed ABC for total PAHs Documents can be provided upon request in an alternate format for individuals with disabilities or in a language other than English for people with limited English skills.