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Rheology Modification of Hydrogen Peroxide-Based Applications Using
Rheology Modification of Hydrogen Peroxide-Based Applications Using Cross-Linked Polyacrylic Acid Polymers* Julie Schmucker-Castner and Dilip Desai The BFGoodrich Company 1. Key Words: Hydrogen Peroxide, Hair Bleach, Two-Part Hair Color, Rheology Modification, Thickened Hydrogen Peroxide, Hydrogen Peroxide Gels, Hydrogen Peroxide Stability, Cross-Linked Polyacrylic Acid, Carbomer, Acrylates / C10-30 Alkyl Acrylate Crosspolymer 2. Summary: A fundamental study of the stability of hydrogen peroxide-based gels, thickened using cross-linked polyacrylic acid polymers, will be presented. Recent systematic experiments will demonstrate that excellent long-term stability of such gels can be achieved. The study evaluates different types of cross- linked polyacrylic acid polymers (as well as an associative acrylic polymer), several commercial sources of hydrogen peroxide, hydrogen peroxide concentrations and the effect of pH. Resulting viscosities from combinations of these variables will be presented, as well as the effects of accelerated aging on percent active peroxide and viscosity of the thickened peroxide gels. The results of this study will enable the formulator to determine the appropriate polymer and conditions necessary for optimal stability and rheological properties for hydrogen peroxide applications. This study will demonstrate that some cross-linked polyacrylic acid polymers are very compatible and stable with H2O2 and that these polymers do not affect the H2O2 stability under certain conditions. In addition, this study will show that certain cross-linked polyacrylic acid polymers can produce very viscous gels and yield higher viscosities in typical permanent hair color formulas compared to many commercially available products. Because of the excellent compatibility and stability demonstrated, cross-linked acrylic acid polymers are ideal rheological modifiers for hydrogen peroxide-based applications. -
Chapter 21 the Chemistry of Carboxylic Acid Derivatives
Instructor Supplemental Solutions to Problems © 2010 Roberts and Company Publishers Chapter 21 The Chemistry of Carboxylic Acid Derivatives Solutions to In-Text Problems 21.1 (b) (d) (e) (h) 21.2 (a) butanenitrile (common: butyronitrile) (c) isopentyl 3-methylbutanoate (common: isoamyl isovalerate) The isoamyl group is the same as an isopentyl or 3-methylbutyl group: (d) N,N-dimethylbenzamide 21.3 The E and Z conformations of N-acetylproline: 21.5 As shown by the data above the problem, a carboxylic acid has a higher boiling point than an ester because it can both donate and accept hydrogen bonds within its liquid state; hydrogen bonding does not occur in the ester. Consequently, pentanoic acid (valeric acid) has a higher boiling point than methyl butanoate. Here are the actual data: INSTRUCTOR SUPPLEMENTAL SOLUTIONS TO PROBLEMS • CHAPTER 21 2 21.7 (a) The carbonyl absorption of the ester occurs at higher frequency, and only the carboxylic acid has the characteristic strong, broad O—H stretching absorption in 2400–3600 cm–1 region. (d) In N-methylpropanamide, the N-methyl group is a doublet at about d 3. N-Ethylacetamide has no doublet resonances. In N-methylpropanamide, the a-protons are a quartet near d 2.5. In N-ethylacetamide, the a- protons are a singlet at d 2. The NMR spectrum of N-methylpropanamide has no singlets. 21.9 (a) The first ester is more basic because its conjugate acid is stabilized not only by resonance interaction with the ester oxygen, but also by resonance interaction with the double bond; that is, the conjugate acid of the first ester has one more important resonance structure than the conjugate acid of the second. -
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. -
Oxalic Acid As a Heterogeneous Ice Nucleus in the Upper Troposphere and Its Indirect Aerosol Effect” by B
Atmos. Chem. Phys. Discuss., 6, S1765–S1768, 2006 Atmospheric www.atmos-chem-phys-discuss.net/6/S1765/2006/ Chemistry ACPD c Author(s) 2006. This work is licensed and Physics 6, S1765–S1768, 2006 under a Creative Commons License. Discussions Interactive Comment Interactive comment on “Oxalic acid as a heterogeneous ice nucleus in the upper troposphere and its indirect aerosol effect” by B. Zobrist et al. B. Zobrist et al. Received and published: 13 July 2006 The authors would like to thank anonymous referee #1 for his/her constructive comments. We have addressed the referee’s concerns point-by-point below. Full Screen / Esc Succinic and Adipic acid as immersion IN: The solubility of these dicarboxylic acids is very low at temperatures of about 235 K, Printer-friendly Version as supported by the deliquescence measurements of Parsons et al. (JGR 109, D06212, 2004) which are close to 100 % RH. In our experiments, the droplets of Interactive Discussion these acids are completely liquid in the first cooling cycle with concentrations of Discussion Paper 7.3 wt% for succinic acid and 1.6 wt% for adipic acid, which is why they nucleate ice S1765 EGU homogeneously at temperatures below that of pure water. When the acids precipitate, the concentration of the remaining liquid corresponds to the equilibrium solubility at ACPD each temperature when the samples are cooled in the second cycle. Because of the 6, S1765–S1768, 2006 low solubility at lower temperatures we expect the observed rise in the homogeneous ice nucleation temperature when compared to the first cooling run. In fact, if we use the measured freezing temperatures and assume they are due to homogeneous ice Interactive nucleation, we can use water-activity-based ice nucleation theory to deduce the water Comment activity of the liquid part of the samples. -
Synthesis of Functionalized Polyamide 6 by Anionic Ring-Opening Polymerization Deniz Tunc
Synthesis of functionalized polyamide 6 by anionic ring-opening polymerization Deniz Tunc To cite this version: Deniz Tunc. Synthesis of functionalized polyamide 6 by anionic ring-opening polymerization. Poly- mers. Université de Bordeaux; Université de Liège, 2014. English. NNT : 2014BORD0178. tel- 01281327 HAL Id: tel-01281327 https://tel.archives-ouvertes.fr/tel-01281327 Submitted on 2 Mar 2016 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Logo Université de cotutelle THÈSE PRÉSENTÉE POUR OBTENIR LE GRADE DE DOCTEUR DE L’UNIVERSITÉ DE BORDEAUX ET DE L’UNIVERSITÉ DE LIEGE ÉCOLE DOCTORALEDE SCIENCES CHIMIQUES (Université de Bordeaux) ÉCOLE DOCTORALE DE CHIMIE (Université de Liège) SPÉCIALITÉ POLYMERES Par Deniz TUNC Synthesis of functionalized polyamide 6 by anionic ring-opening polymerization Sous la direction de Stéphane CARLOTTI et Philippe LECOMTE Soutenue le 30 octobre 2014 Membres du jury: M. PERUCH, Frédéric Directeur de recherche, Université de Bordeaux Président M. HOOGENBOOM, Richard Professeur, Ghent University Rapporteur M. MONTEIL, Vincent Chargé de recherche, Université Claude Bernard Rapporteur M. YAGCI, Yusuf Professeur, Istanbul Technical University Examinateur M. AMEDURI, Bruno Directeur de recherche, Institut Charles Gerhardt Examinateur M. SERVANT, Laurent Professeur, Université de Bordeaux Invité Preamble This PhD had been performed within the framework of the IDS FunMat joint doctoral programme. -
Influence of Ε-Caprolactam on Growth and Physiology of Environmental Bacteria
Ann Microbiol (2013) 63:1471–1476 DOI 10.1007/s13213-013-0610-4 ORIGINAL ARTICLE Influence of ε-caprolactam on growth and physiology of environmental bacteria Nandita N. Baxi Received: 14 July 2012 /Accepted: 22 January 2013 /Published online: 24 February 2013 # Springer-Verlag Berlin Heidelberg and the University of Milan 2013 Abstract ε-Caprolactam was found to have an effect on Introduction ecologically important soil bacteria. It inhibited the growth of several Bacillus sp. and Rhizobium sp. but cells of Microbial activity in soil has numerous functions contribut- Arthrobacter sp. were able to grow in the presence of capro- ing to soil fertility. It is involved in organic nutrient cycles, lactam. Sphingomonas sp. lost its inherent capacity to produce the release of minerals and fixation of nutrients from the air, extracellular polymer (EPS) if grown in medium containing rendering nutrients more accessible and easily transportable caprolactam. In the case of raw domestic sewage, the diversity to plant roots, prevention of aggressive plant pathogens of native bacteria was diminished in presence of caprolactam. taking hold, improving the ability of plants to withstand Polluted sea water yielded predominantly one type of disease effects, the decrease of inorganic fertilizer loss caprolactam-degrading bacteria of the genus Achromobacter. through erosion and leaching, short-term immobilization, These cells efficiently utilized up to 10 g caprolactam/L as the and decrease of persistence of pesticides in soils. However, sole source of carbon and nitrogen in synthetic medium even the soil biological ecosystem (manifested both by microbial in the presence of 20 g NaCl/L. Compared to cells of and enzymatic activities) can be significantly impaired by Arthrobacter sp., cells of Achromobacter sp. -
CO Route Cuts Acrylic Acid Costs
BEST INNOVATION BY AN SME since the 1980s but, to date, no one has been able to develop an economically feasible proc- ess. The thermoplastic has similar properties to polyethylene terephthalate (PET), but with significantly higher barrier properties. Novomer’s proprietary system is based on ho- mogeneous catalyst technology that was origi- nally discovered at New York-based Cornell University by Geoffrey Coates, Novomer’s co-founder and chairman of its scientific advisory board. The significance of the process is that it enables the use of a low-cost monomer, in this case carbon monoxide (CO), which is combined with ethylene oxide (EO) to make propriolactone. Novomer says that the use of inexpensive raw materials, such as CO and ethane-derived EO, and the catalyst’s selec- Superabsorbent polymer (SAP) made with Novomer’s catalyst has the same tivity, which is in excess performance as SAP made using the traditional propylene-based route of 99%, means that the Novomer “Our ultimate vision... is that low molecular weight PPL CO route could be shipped globally and converted to AA or acrylate esters upon demand” MIKE SLOWIK cuts acrylic Director of chemicals, Novomer cost of the process is potentially 40% lower than current available technologies. acid costs In addition, the process is expected to have a lower carbon and energy footprint because it operates at moderate temperatures, notably between 30-50oC. This compares with an Novomer, winner of the Best Innovation by an SME operating temperature of over 250oC in the existing AA production process. category, has widened its vision for the proprietary Novomer has raised about $30m so far in technology, which won last year’s Innovation with Best venture capital funding which it is using to part-finance construction of a continuous pi- Environmental Benefit category lot-scale process plant. -
APPENDIX G Acid Dissociation Constants
harxxxxx_App-G.qxd 3/8/10 1:34 PM Page AP11 APPENDIX G Acid Dissociation Constants § ϭ 0.1 M 0 ؍ (Ionic strength ( † ‡ † Name Structure* pKa Ka pKa ϫ Ϫ5 Acetic acid CH3CO2H 4.756 1.75 10 4.56 (ethanoic acid) N ϩ H3 ϫ Ϫ3 Alanine CHCH3 2.344 (CO2H) 4.53 10 2.33 ϫ Ϫ10 9.868 (NH3) 1.36 10 9.71 CO2H ϩ Ϫ5 Aminobenzene NH3 4.601 2.51 ϫ 10 4.64 (aniline) ϪO SNϩ Ϫ4 4-Aminobenzenesulfonic acid 3 H3 3.232 5.86 ϫ 10 3.01 (sulfanilic acid) ϩ NH3 ϫ Ϫ3 2-Aminobenzoic acid 2.08 (CO2H) 8.3 10 2.01 ϫ Ϫ5 (anthranilic acid) 4.96 (NH3) 1.10 10 4.78 CO2H ϩ 2-Aminoethanethiol HSCH2CH2NH3 —— 8.21 (SH) (2-mercaptoethylamine) —— 10.73 (NH3) ϩ ϫ Ϫ10 2-Aminoethanol HOCH2CH2NH3 9.498 3.18 10 9.52 (ethanolamine) O H ϫ Ϫ5 4.70 (NH3) (20°) 2.0 10 4.74 2-Aminophenol Ϫ 9.97 (OH) (20°) 1.05 ϫ 10 10 9.87 ϩ NH3 ϩ ϫ Ϫ10 Ammonia NH4 9.245 5.69 10 9.26 N ϩ H3 N ϩ H2 ϫ Ϫ2 1.823 (CO2H) 1.50 10 2.03 CHCH CH CH NHC ϫ Ϫ9 Arginine 2 2 2 8.991 (NH3) 1.02 10 9.00 NH —— (NH2) —— (12.1) CO2H 2 O Ϫ 2.24 5.8 ϫ 10 3 2.15 Ϫ Arsenic acid HO As OH 6.96 1.10 ϫ 10 7 6.65 Ϫ (hydrogen arsenate) (11.50) 3.2 ϫ 10 12 (11.18) OH ϫ Ϫ10 Arsenious acid As(OH)3 9.29 5.1 10 9.14 (hydrogen arsenite) N ϩ O H3 Asparagine CHCH2CNH2 —— —— 2.16 (CO2H) —— —— 8.73 (NH3) CO2H *Each acid is written in its protonated form. -
Production of Adipic Acid from Mixtures of Cyclohexanol-Cyclohexanone Using Polyoxometalate Catalysts
Makara J. Sci. 19/2 (2015), 85-90 doi: 10.7454/mss.v19i2.4778 Production of Adipic Acid from Mixtures of Cyclohexanol-Cyclohexanone using Polyoxometalate Catalysts Aldes Lesbani 1*, Sumiati 1, Mardiyanto 2, Najma Annuria Fithri 2, and Risfidian Mohadi 1 1. Department of Chemistry, Faculty of Mathematic and Natural Sciences, Universitas Sriwijaya, Indralaya (OI), Sumatera Selatan 30662, Indonesia 2. Department of Pharmacy, Faculty of Mathematic and Natural Sciences, Universitas Sriwijaya, Indralaya (OI), Sumatera Selatan 30662, Indonesia *E-mail: [email protected] Abstract Adipic acid production through catalytic conversion of cyclohexanol-cyclohexanone using polyoxometalate H 5[α-BW 12 O40 ] and H 4[α-SiW 12 O40 ] as catalysts was carried out systematically. Polyoxometalates H 5[α-BW 12 O40 ] and H 4[α-SiW 12 O40 ] were synthesized using an inorganic synthesis method and were characterized using Fourier transform infrared spectroscopy (FTIR). Adipic acid was formed from conversion of cyclohexanol-cyclohexanone and was characterized by using melting point measurement, identification of functional group using FTIR spectrophotometer, analysis of gas chromatography-mass spectrometry (GC-MS), and 1H and 13 C NMR (nuclear magnetic resonance) spectrophotometer. This research investigated the influence of reaction time and temperature on conversion. The results showed that adipic acid was formed successfully with a yield of 68% by using H 5[α-BW 12 O40 ] as catalyst at the melting point of 150-152 °C after optimization. In contrast, using H 4[α-SiW 12 O40 ] as catalyst, formation of adipic acid was only 3.7%. Investigation of time and temperature showed 9 h as the optimum reaction time and 90 °C as the optimum temperature for conversion of up to 68% adipic acid. -
Caprolactam 99/00-4
Caprolactam 99/00-4 March 2001 TABLE OF CONTENTS Page I EXECUTIVE SUMMARY - 1 - A. SYNOPSIS - 1 - B. TECHNOLOGY DEVELOPMENTS - 1 - 1. Enhancements to Conventional Technology - 2 - 2. Caprolactam from Alternative Sources - 2 - C. TECHNO-ECONOMICS - 5 - 1. Enhancements to Conventional Technology - 5 - 2. Routes Based on Butadiene - 5 - D. COMMERCIAL STATUS - 8 - 1. Consumption - 8 - 2. Supply/Demand Balance - 9 - 3. Trade - 9 - 4. Ammonium Sulfate - 10 - E. STRATEGIC ISSUES - 12 - 1. Cyclicality - 12 - 2. Nylon Feedstocks from One Source - 13 - F. NYLON RECYCLING - 14 - G. CONCLUSIONS - 15 - II INTRODUCTION - 16 - A. AIM OF THE STUDY - 1 - B. OVERVIEW - 17 - 1. Enhancements to Conventional Technology - 17 - 2. Caprolactam from Alternative Sources - 17 - C. CHEM SYSTEMS PRODUCTION COST METHODOLOGY - 20 - 1. Capital Cost Estimation - 20 - (a) Battery Limits Investment - 20 - (b) Off-Sites Investment - 21 - (c) Contractor Charges(2) Typically 15-25 Percent of Installed BL and OS Costs - 22 - (d) Project Contingency Allowance(2) - 22 - (e) Working Capital - 22 - (f) Other Project Costs(3) - 23 - (1) Start-Up/Commissioning Costs - 23 - (2) Miscellaneous Owner’s Costs - 23 - 2. Cost of Production Elements - 24 - (a) Battery Limits - 24 - (b) Production Costs - 25 - (1) Labor - 25 - TABLE OF CONTENTS (Continued) Page III CAPROLACTAM FROM AROMATIC-DERIVED FEEDSTOCKS - 26 - A. COMMERCIAL TECHNOLOGIES - 26 - 1. Overview - 26 - 2. Process Chemistry - 26 - (a) Cyclohexanone Synthesis - 26 - (b) Oxime Formation with Cyclohexanone Using Hydroxylamine -
Propane to Acrylic Acid
University of Pennsylvania ScholarlyCommons Department of Chemical & Biomolecular Senior Design Reports (CBE) Engineering 4-2013 Propane to Acrylic Acid Amanda Culp University of Pennsylvania Kevin Holmes University of Pennsylvania Rohan Nagrath University of Pennsylvania Dan Nessenson University of Pennsylvania Follow this and additional works at: https://repository.upenn.edu/cbe_sdr Part of the Biochemical and Biomolecular Engineering Commons Culp, Amanda; Holmes, Kevin; Nagrath, Rohan; and Nessenson, Dan, "Propane to Acrylic Acid" (2013). Senior Design Reports (CBE). 48. https://repository.upenn.edu/cbe_sdr/48 This paper is posted at ScholarlyCommons. https://repository.upenn.edu/cbe_sdr/48 For more information, please contact [email protected]. Propane to Acrylic Acid Abstract Acrylic acid is an essential polymer raw material for many industrial and consumer products. Currently, acrylic acid is manufactured from propylene, which is created as a by- product from fossil fuels manufacture and industrial cracking of heavy hydrocarbons. However, the discovery of new natural gas reserves presents new opportunities for the production of acrylic acid. A design feasibility study is presented to analyze the economics behind producing acrylic acid from the selective oxidation of propane to propylene over a mixed metal oxide catalyst, Mo1V0.30Te0.23Nb0.125Ox. The proposed plant is located in the U.S. Gulf Coast and produces 200MM lb/yr acrylic acid. Since the catalytic oxidation process has low propane conversion per pass, the process recycles unconverted propane and propylene back to the reactor to increase overall conversion. The acrylic acid is then separated and purified ot the glacial-grade industrial standard for polymer raw material of 99.7% acrylic acid by mass. -
Environmental Health Risk Assessment—Guidelines
Contents Figures .................................................................................................................................................................................. vi Tables ................................................................................................................................................................................... vii Objectives ............................................................................................................................................................................ viii Audience ............................................................................................................................................................................. viii Acknowledgments ................................................................................................................................................................. ix PART 1: BASIC CONCEPTS IN ENVIRONMENTAL HEALTH RISK ASSESSMENT ..................................................... 1 Chapter 1: Introduction to environmental health risk assessment .................................................................................................... 3 1.1 What is risk assessment? ............................................................................................................................................ 3 1.2 When to undertake risk assessment ..........................................................................................................................