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Report of the Advisory Group to Recommend Priorities for the IARC Monographs During 2020–2024
IARC Monographs on the Identification of Carcinogenic Hazards to Humans Report of the Advisory Group to Recommend Priorities for the IARC Monographs during 2020–2024 Report of the Advisory Group to Recommend Priorities for the IARC Monographs during 2020–2024 CONTENTS Introduction ................................................................................................................................... 1 Acetaldehyde (CAS No. 75-07-0) ................................................................................................. 3 Acrolein (CAS No. 107-02-8) ....................................................................................................... 4 Acrylamide (CAS No. 79-06-1) .................................................................................................... 5 Acrylonitrile (CAS No. 107-13-1) ................................................................................................ 6 Aflatoxins (CAS No. 1402-68-2) .................................................................................................. 8 Air pollutants and underlying mechanisms for breast cancer ....................................................... 9 Airborne gram-negative bacterial endotoxins ............................................................................. 10 Alachlor (chloroacetanilide herbicide) (CAS No. 15972-60-8) .................................................. 10 Aluminium (CAS No. 7429-90-5) .............................................................................................. 11 -
New Synthesis Routes for Production of Ε-Caprolactam by Beckmann
New synthesis routes for production of ε-caprolactam by Beckmann rearrangement of cyclohexanone oxime and ammoximation of cyclohexanone over different metal incorporated molecular sieves and oxide catalysts Von der Fakultät für Mathematik, Informatik und Naturwissenschaften der RWTH Aachen University zur Erlangung des akademischen Grades eines Doktors der Naturwissenschaften genehmigte Dissertation vorgelegt von Anilkumar Mettu aus Guntur/Indien Berichter: Universitätprofessor Dr. Wolfgang F. Hölderich Universitätprofessor Dr. Carsten Bolm Tag der mündlichen Prüfung: 29.01.2009 Diese Dissertation ist auf den Internetseiten der Hochschulbibliothek online verfügbar. Dedicated to my Parents This work reported here has been carried out at the Institute for Chemical Technolgy and Heterogeneous Catalysis der Fakultät für Mathematik, Informatik und Naturwissenschaften in the University of Technology, RWTH Aachen under supervision of Prof. Dr. Wolfgang F. Hölderich between June 2005 and August 2008. ACKNOWLEDGEMENTS I would like to express my deepest sence of gratitude to my supervisor Prof. Dr. rer. nat. W. F. Hölderich for giving me the opportunity to do my doctoral study in his group. His guidance and teaching classes have allowed me to grow and learn my subject during my Ph.d. He has provided many opportunities for me to increase my abilities as a researcher and responsibilities as a team member. I am grateful for the financial support of this work from Sumitomo Chemicals Co., Ltd, Niihama, Japan (Part One) and Uhde Inventa-Fischer GmBH, Berlin (Part Two). Our collaborators at Sumitomo Chemicals Co., Ltd (Dr. C. Stoecker) and Uhde Inventa- Fischer GmBH (Dr. R. Schaller and Dr. A. Pawelski) provided thoughtful guidance and suggestions for each project. -
United States Patent O Patented Sept
2,719,] 16 United States Patent O Patented Sept. 27, 1955 i 2 mation of a resinous coating to a substantial degree. The amount of inhibitor employed should give effective‘ 2,719,116 action and will in most instances be small compared with PHOTOCHEMICAL PREPARATION OF OXIIVIES the amount of cyclic, hydro-aromatic compound present in the reactor. In general, the minimum amount of in Bernard B. Brown, Grand Island, N. Y., assignor to 01in hibitor to be employed will be at least about 0.5% by. Mathieson Chemical Corporation, a corporation of Virginia weight based upon the hydro-aromatic compound pres ent in the reactor. The maximum amount of acid to No Drawing. Application March 19, 1954, utilize will also vary with the particular acid selected Serial No. 417,490 10 but ordinarily little advantage will be derived if the amount employed is more than that which is soluble in 9 Claims. (Cl. 204—-158) the reacting mixture. I have found through several reactions conducted in the presence of my inhibitors that it is preferable to This invention relates to improvements in a method employ a saturated solution of the inhibitor in the re for the manufacturing of oximes of cyclic ketones. These acting mixture. A saturated solution of formic acid in oximes are valuable intermediates for the manufacturing cyclohexane will contain from about 0.85 to 1.25% by of superpolyamides. weight depending upon the temperature of the reaction In the copending application of Christoph Grundmann, and the extent of mixing. In some instances when the Serial No. -
The Pennsylvania State University the Graduate School AN
The Pennsylvania State University The Graduate School AN EXAMINATION OF ANALYTICAL METHODS TOWARDS THE COMPLETE ANALYSIS OF CONTAMINANTS OF EMERGING CONCERN IN WASTEWATER AND WASTEWATER IMPACTED SURFACE WATER, SOILS, AND CROPS. A Dissertation in Chemistry by Kyra A. Murrell © 2020 Kyra A. Murrell Submitted in Partial Fulfillment of the Requirements for the Degree of Doctor of Philosophy August 2020 The dissertation of Kyra A. Murrell was reviewed and approved by the following: Frank L. Dorman Associate Professor of Biochemistry and Molecular Biology Dissertation Co-Advisor Co-Chair of Committee Miriam Freedman Associate Professor of Chemistry, Meteorology and Atmospheric Science Dissertation Co-Adviser Co-Chair of Committee Paul Cremer J. Lloyd Huck Professor of Chemistry and of Biochemistry and Molecular Biology Christine Keating Distinguished Professor of Chemistry Jack Watson Professor of Soil Science, Soil Physics, Biogeochemistry Philip Bevilacqua Distinguished Professor of Chemistry and Biochemistry and Molecular Biology Department Head, Chemistry iii ABSTRACT The presence of contaminants of emerging concern (CECs) in the environment is a growing field of research for analytical environmental scientists. CECs are a class of anthropogenic pollutants not regulated by governmental agencies, and their potential deleterious environmental and human impacts are largely unknown. One of the main sources of CEC entry into the aquatic environment is wastewater treatment plant (WWTP) effluent as the treated water is often released into bodies of water, such as river and streams. Because most WWTPs were not designed to remove organic micropollutants, many CECs are poorly removed in traditional WWTPs and persist in the treated effluent waters. As a model system for study, the University Park WWTP treats the wastewater from the Penn State main campus. -
PEP Review 2015-06 Polyamide (Nylon) 6 and 66 Process Summary
IHS CHEMICAL PEP Review 2015-06 Polyamide (Nylon) 6 and 66 Process Summary July 2015 ihs.com PEP Review Process Economics Program Dipti Dave Senior Analyst II IHS CHEMICAL | Process Economics Program Review 2015-06 PEP Review 2015-06 Polyamide (Nylon) 6 and 66 Process Summary Dipti Dave, Senior Analyst II Abstra ct Polyamide 6 and 66 (or Nylon 6 and 66) are the most common types of polyamide available commercially. The total volume for the Nylon 6 and 66 polymerization market is 7.2 million tons in 2014, up from 6.4 million tons in 2010. Nylon 6 and 66 polymerization produces either chips or resin in uniform pellets. The chips or resin are further processed into two major applications: fibers or engineering thermoplastics (ETP). The fibers may also be directly produced from the molten state of the polymer, bypassing chip/resin production. The majority of the Nylon chip or resin production accounts for 92% of total polymerization, while fiber production (directly from melting) accounts for 8% market share. Demand is expected to grow at an average annual growth rate (AAGR) of 2.4% for Nylon 6 ETP and fiber. The AAGR for Nylon 66 ETP and fiber demand is 2.6%. Capacity additions have been taking place mostly in China. The Nylon processes have been reviewed by IHS Chemical Process Economics Program (PEP) since its inception in 1962. In this process summary, we review the key features for Nylon 6 and 66 production processes, and discuss recent technology developments and update the process economics for the following Nylon 6 and 66 stand-alone and integrated processes presented: 1. -
Synthesis and Characterization of In-Situ Nylon-6/Epoxy Blends
Synthesis and Characterization of in-situ Nylon-6/Epoxy Blends A thesis submitted to the Division of Research and Advanced Studies University of Cincinnati In partial fulfillment of the requirements for the degree of Master of Science 2016 In the Materials Science and Engineering Program, The Department of Mechanical and Materials Engineering By Anushree Deshpande B.E Polymer, University of Pune, 2011 Committee Members: Dr. Jude O. Iroh (Chair) Dr. Relva C. Buchanan Dr. Raj M. Manglik 1 ABSTRACT Epoxy is a thermosetting polymer known for its excellent adhesion, thermal stability, chemical resistance and mechanical properties. However, one of the major drawbacks of epoxies is its inherent brittleness. In order to overcome this drawback, incorporation of a thermoplastic as a second phase has proven to improve the impact strength without affecting the mechanical properties of epoxy. Researchers in the past have studied polyamide/epoxy blends in terms of blend compatibility, thermo-mechanical properties and morphology via solution blending. The current research effort employs in-situ polymerization to synthesize polyamide/epoxy blends. Blends of various compositions were synthesized by introducing Ɛ-Caprolactam (monomer of nylon-6) in the prepolymer of epoxy. All blend fractions were cured by exposing them to the same time and temperature conditions; and characterized using Dynamic Mechanical Analysis (DMA), Fourier Transform Infrared Spectroscopy (FTIR), Brookfield Viscometry, Scanning Electron Microscopy (SEM) and Thermogravimetric Analysis (TGA). DMA results show an overall increase in glass transition temperature and storage modulus in the rubbery region. FTIR results reveal maximum epoxy curing up to 15 wt% monomer loading, beyond which the plateauing of the epoxy conversion is recognized. -
Carpet Recycling
1 TheThe ParticipantParticipant willwill gaingain knowledgeknowledge inin thethe following:following: › Drivers for Carpet Recycling › General Categories of carpet recycling › Differences in Various types of recycling › Market Values of Various Recycled Products › Demand for Recycled materials from Carpet › Understanding Capital needs of Recycling › Present & Anticipated recycling capacities › Present & New Recycling technologies › Challenges & Opportunities 2 3 BroadBroad ListList ofof Drivers:Drivers: › Carpet Manufacturers › LEED building Standards –Need P. Consumer for high value/Specifications › NSF 140 › High value of P.C. content › Platinum Level highly prized: Requires Min. Post consumer content. › Platinum Level requires P.C. Carpet recycling at CARE Goal levels – Escalate every year. › Professional Specifying Commercial Community demands Sustainability › Reward most Sustainable companies with increased business: or NO business › Recycling and P. Consumer recycled content is large factor › Large National Accounts demanding sustainable initiatives: › Wal‐Mart, Home Depot, etc. › Good Old healthy competition. 4 BroadBroad ListList ofof Drivers:Drivers: › Entrepreneurs: › Willing to risk Capital for carpet recycling › They are beginning to see fairly good business model › Beginning to make money from carpet recycling › They are essential link in the value chain of processing › High Oil prices › Keeps Virgin Nylon very expensive › Cost Spread between virgin and P. Consumer is wide › Makes P. Consumer very attractive for cost savings -
Synergistic Effects of Nano-Silica on Aluminum Diethylphosphinate
Original Article High Performance Polymers 2016, Vol. 28(2) 140–146 ª The Author(s) 2015 Synergistic effects of nano-silica on Reprints and permission: sagepub.co.uk/journalsPermissions.nav aluminum diethylphosphinate/ DOI: 10.1177/0954008315572493 polyamide 66 system for fire retardancy hip.sagepub.com Zhaoshun Zhan1,2, Bin Li1,2, Miaojun Xu1 and Zhanhu Guo3 Abstract Nano-silica had been used as a synergistic agent for the preparation of aluminum diethylphosphinate (AlPi) flame retardant polyamide 66 (PA66/AlPi) and PA66/AlPi/nano-silica composites through twin-screw extrusion. The limiting oxygen index (LOI), used to characterize the minimum amount of oxygen needed to sustain a candle-like flame, revealed that the PA66/ 10%AlPi/1%nano-silica composites exhibited an excellent flame retardant efficiency with a high LOI value of 32.3%. The vertical flame test (UL-94) revealed that the PA66/10%AlPi/1%nano-silica composites passed the V-0 rating without drop melting. Cone calorimeter test revealed that the heat release rate and total heat rate for the PA66/10%AlPi/1%nano-silica composites were significantly decreased by 51.1 and 16.8%, respectively, compared with those of pure PA66. The thermogravimetric analysis showed that the PA66/10%AlPi/1%nano-silica composites had vast chars of 8.1% even at 800C, indicating that nano-silica could promote the char formation of the PA66 composites. Scanning electron micro- scopy indicated a solid and tough residue of the burned PA66/10%AlPi/1%nano-silica composites as compared with the very loose and brickle residue of the burned pure PA66, indicating that a suitable amount of nano-silica played a synergistic effect in the flame retardancy. -
Nylon 6 and Caprolactam
PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California Abstract 94025 Process Economics Program Report No. 418 CAPROLACTAM AND NYLON 6 (March 1988) This report reviews the technology for the production of caprolactam and its polymer, nylon 6. A total of three major caprolactam manufacturing and one nylon 6 manufacturing routes are evaluated in detail: l Caprolactam from cyclohexane via cyclohexanone by oxidation, oximation, and Beckmann rearrangement l Caprolactam from phenol via cyclohexanone by hydrogenation, oximation, and Beckmann rearrangement l Caprolactam from toluene via cyclohexanone carboxylic acid by oxidation, hydro- genation , nitrosation, and rearrangement l Nylon 6 from caprolactam by hydrolysis, poly addition, and polycondensation. Economics for three alternative processes using the first route, one process each using the second and third routes, and two alternative processes using the forth route are presented. As of January 1987, the world production capacity for caprolactam was about 7,000 million lblyr (3.157 thousand metric tonslyr) , and that for nylon 6 is more than 4,786 million Ib/yr (2,173 thousand metric tonslyr) . PEP’87 Vu-Ren Chin Report No. 41 B NYLON 6 AND CAPROLACTAM SUPPLEMENT B by YU-REN CHIN with contributions by KUEN-TIAN CHANG REN-BEN CHEN KUN-HO LIU February 1988 A private report by the PROCESS ECONOMICS PROGRAM Menlo Park, California 94025 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLD PETBOCHEMICALS Program covers major hydrocarbons and their.derivativeson a worldwide basis. -
WO 2015/087099 Al 18 June 2015 (18.06.2015) W P O P C T
(12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization International Bureau (10) International Publication Number (43) International Publication Date WO 2015/087099 Al 18 June 2015 (18.06.2015) W P O P C T (51) International Patent Classification: AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, C08L 77/02 (2006.01) C08K 5/3492 (2006.01) BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DK, DM, C08L 77/06 (2006.01) C08K 5/5313 (2006.01) DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, C08K 3/32 (2006.01) C08L 23/08 (2006.01) HN, HR, HU, ID, IL, IN, IR, IS, JP, KE, KG, KN, KP, KR, KZ, LA, LC, LK, LR, LS, LT, LU, LY, MA, MD, ME, (21) International Application Number: MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, PCT/IB20 13/00275 1 OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, (22) International Filing Date: SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, TM, 12 December 2013 (12. 12.2013) TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW. (25) Filing Language: English (84) Designated States (unless otherwise indicated, for every (26) Publication Language: English kind of regional protection available): ARIPO (BW, GH, (71) Applicant: ITALMATCH CHEMICALS S.p.A. [IT/IT]; GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, SZ, TZ, UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, TJ, Via Pietro Chiesa, 7/1 3 - Torri Piane, 1- 16149 San Benigno (Genova) (ΓΓ). -
Caprolactam, Supplement A
Report No. 7-A CAPROLACTAM SUPPLEMENT A by HAROLD C. RIES March 1868 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA I CONTENTS 1 INTRODUCTION . 1 2 SUMMARY.......................... 3 3 INDUSTRY STATUS. 17 4 CAPROLACTAM BY THE PHOTONITROSATION OF CYCLOHEXANE .... 27 Chemistry ......................... 27 Review of Processes .................... 29 Photochemical Lamps ................... 30 PNC Reactors ...................... 33 PNC Processes ...................... 35 Nitrosyl Chloride Production .............. 37 Caprolactam Purification ................ 38 8 Process Description .................... 42 Nitrosyl Chloride Production .............. 44 Photonitrosation of Cyclohexane ............. 45 Rearrangement ...................... 47 Caprolactam Purification ................ 48 Ammonium Sulfate Recovery ................ 49 Process Discussion .................... 68 Costs ........................... 72 Capital Investment ................... 72 Production Costs .................... 81 5 CYCLOHEXANONE FROM CYCLOHEXANE .............. 87 Review of Processes .................... a7 Cyclohexane Oxidation .................. 87 Dehydrogenation of Cyclohexanol ............. 87 Stamicarbon Process ................... 90 Process Description .................... 92 Cyclohexane Oxidation (I.F.P. Process) ......... 92 Cyclohexanone from Mixed Oil .............. 96 costs ........................... 97 E Capital Investment ................... 97 100 8 Production Costs .................... 8 iii CONTENTS -
FDM Nylon 12
FREQUENTLY ASKED QUESTIONS FDM Nylon 12 1. What is nylon? Nylons were the first engineering thermoplastics. They have been around for 85 years and are one of the most widely used materials for traditional thermoplastic manufacturing today. Nylons falls into the polyamide (PA) class of materials. This is a material class that includes both natural substances (silk and wool) and synthetic materials (thermoplastics). All nylon materials are polyamides, but all synthetic polyamides aren’t nylons. Since nylon is such a recognizable material name, on our literature and in conversations, we will use it as the preferred term. 2. What nylon material is Stratasys offering? FDM® Nylon 12™ (unfilled) is the first nylon material that can be 3D printed with fused deposition modeling (FDM) technology. It has been highly demanded by our customers and complements our current FDM materials portfolio. Unique part capabilities and properties include: • Snap-fit and press-fit inserts: tough small clips, bosses, posts and holes • High fatigue resistance: parts exposed to repeat loading cycles, stress and vibration • Good impact strength: parts resistant to shock from being dropped or abrupt forces • Moderate temperate resistance: HDT of up to 82°C (after annealing) • Good chemical resistance: resistant to moderate solvents, alcohols and chemicals Application best fits include: • Panels, covers, housings with snap-fit clips, bosses and other small features • Environmental control ducting and venting • Components of products with high vibration, repetitive stress or fatigue • Drill guides, cutting fixtures and prototypes with friction fit press-in inserts • Prototypes and end-use parts requiring tough bosses or threaded inserts THE 3D PRINTING SOLUTIONS COMPANY™ FREQUENTLY ASKED QUESTIONS FDM Nylon 12 Target industries include: • Automotive: interior panels, environmental control ducting • White goods: panels, covers, vibration resistant components • Home appliance and consumer electronics: covers, panels and facades • Aerospace: tooling, manufacturing aids, jigs and fixtures 3.