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Hydrogen Transfer and Activation of Propane and Methane on ZSM5-Based Catalysts
Catalysis Letters 21 (1993) 55-70 55 Hydrogen transfer and activation of propane and methane on ZSM5-based catalysts Enrique Iglesia 1 and Joseph E. Baumgartner Corporate Research Laboratories, Exxon Research and Engineering, Route 22 East, Annandale, NJ08801, USA Received 12 April 1993; accepted 4 June 1993 Hydrogen exchange between undeuterated and perdeuterated light alkanes (CD4-C3Hs, C3Ds-C3Hs) occurs on H-ZSM5 and on Ga- and Zn-exchanged H-ZSM5 at 773 K. Alkane conversion to aromatics occurs much more slowly because it is limited by rate of disposal of H-atoms formed in C-H scission steps and not by C-H bond activation. Kinetic coupling of these C-H activation steps with hydrogen transfer to acceptor sites (Ga n+, Znm+) and ulti- mately to stoichiometric hydrogen acceptors (H+, CO2, 02, CO) often increases alkane activa- tion rates and the selectivity to unsaturated products. Reactions of 13CH4/C3H8 mixtures at 773 K lead only to unlabelled alkane, alkene, and aromatic products, even though exchange between CD4 and C3H8 occurs at these reaction conditions. This suggests that the non- oxidative conversion of CH4 to higher hydrocarbons on solid acids is limited by elementary steps that occur after the initial activation of C-H bonds. Keywords: Hydrogen transfer; light alkane reactions; deuterium cross-exchange reactions; alkane aromatization 1. Introduction Recent studies suggest that electrophilic activation of light alkanes occurs on superacid catalysts [1] and on Hg-based organometallic complexes [2] at low tem- peratures, and on weaker solid acids at higher temperatures [3-9], apparently via heterolytic cleavage of C-H bonds or intermediate partial oxidation of methane to methanol. -
Phosphine and Ammonia Photochemistry in Jupiter's
40th Lunar and Planetary Science Conference (2009) 1201.pdf PHOSPHINE AND AMMONIA PHOTOCHEMISTRY IN JUPITER’S TROPOSPHERE. C. Visscher1, A. D. Sperier2, J. I. Moses1, and T.C. Keane3. 1Lunar and Planetary Institute, USRA, 3600 Bay Area Blvd., Houston, TX 77058-1113 2Baylor University, Waco, TX 76798, 3Department of Chemistry and Physics, The Sage Colleges, Troy, NY 12180, ([email protected], [email protected]) Introduction: The last comprehensive photo- tions involving the amino radical (NH2) play a larger chemical model for Jupiter’s troposphere was pre- role. We note that this is the first photochemical sented by Edgington et al. [1,2], based upon the work model to include P2H as an intermediate species in PH3 of Atreya et al. [3] and Kaye and Strobel [4-6]. Since photolysis. The equivalent N2Hx species are believed these early studies, numerous laboratory experiments to be important in the combustion chemistry of nitro- have led to an improvement in our understanding of gen compounds [15]. PH3, NH3-PH3, and NH3-C2H2 photochemistry [7-13]. Furthermore, recent Galileo, Cassini, and Earth-based observations have better defined the abundance of key atmospheric constituents as a function of altitude and latitude in Jupiter’s troposphere. These new results provide an opportunity to test and improve theoretical models of Jovian atmospheric chemistry. We have therefore developed a photochemical model for Jupi- ter’s troposphere considering the updated experimental and observational constraints. Using the Caltech/JPL KINETICS code [14] for our photochemical models, our basic approach is two- fold. The validity of our selected chemical reaction list is first tested by simulating the laboratory experiments of PH3, NH3-PH3, and NH3-C2H2 photolysis with pho- tochemical “box” models. -
ITP Chemicals: from Natural Gas to Ethylene Via Methane
. INDUSTRIAL TECHNOLOGIES PROGRAM From Natural Gas to Ethylene via Methane Homologation and Ethane Oxidative Dehydrogenation New catalysts promise higher selectivity, Benefits for Our Industry and Our throughput, and economic competitiveness Nation As an alternative to thermal cracking, Ethylene is an important building block This technique has not yet been implemented oxydehydrogenation will save more than 640 in the production of many common and because of high capital investment in existing trillion British thermal units (Btu) per year commercially important materials, such as equipment and techniques. while reducing emissions of many pollutants. plastics and chemicals. Currently, ethylene is This project seeks to develop catalysts that New ethylene plants will save 50 percent in produced in a highly energy-intensive two-step will enable direct production of ethylene capital costs over plants installing cracking process. Ethane is firstrecovered from natural by the oxydehydrogenation of crude ethane furnaces. gas and refinery streams through catalytic found in natural gas. This exothermic process cracking and hydrocracking processes, and will offer high selectivity and throughput of then it is thermally cracked in the presence of ethylene from ethane-concentrated gas streams steam to produce ethylene. A more efficient in addition to saving energy and reducing Applications in Our Nation’s but not yet commercialized alternative to emissions. It will also lower capital costs this method is catalytic oxydehydrogenation, Industry through the use crude ethane, which is cheaper which directly produces ethylene from crude than ethane purified through other processes. Catalytic oxydehydrogenation will find ethane found in natural gas in a single step. immediate application in the petrochemicals industry, which uses ethylene as a primary O2 feedstock for manufacturing plastics and Ethane- Depleted C B chemicals. -
Environlmental ASSESSMENT METHYL CHLORIDE VIA
DOEEA-1157 ENVIRONlMENTAL ASSESSMENT METHYL CHLORIDE VIA OXYHYDROCHLOFUNATION OF METHANE: A BUILDING BLOCK FOR CHEMICALS AND FUELS FROM NATURAL GAS DOW CORNING CORPORATION CARROLLTON, KENTUCKY SEPTEMBER 1996 U.S. DEPARTMENT OF ENERGY PITTSBURGH ENERGY TECHNOLOGY CENTER CUM ~~~~~~~~ DOEEA-1157 ENVIRONlMENTAL ASSESSMENT METHYL CHLORIDE VIA OXYHYDROCHLORINATION OF METHANE: A BUILDING BLOCK FOR CHEMICALS AND FUELS FROM NATURAL GAS DOW CORNING CORPORATION CARROLLTON, KENTUCKY SEPTEMBER 1996 U.S. DEPARTMENT OF ENERGY PITTSBURGH ENERGY TECHNOLOGY CENTER Portions of this document may be illegible in electronic image products. Image are produced from the best available original document. &E/,Etq --,/s7 FINDING OF NO SIGNIFICANT IMPACT FOR THE PROPOSED METHYL CHLORIDE VIA OXYHYDROCHLORINATION OF METHANE PROJECT AGENCY: U.S. Department of Energy (DOE) ACTION: Finding of No Significant Impact (FONSI) SUMMARY: DOE has prepared an Environmental Assessment (EA) (DOE/EA-1157) for a project proposed by Dow Corning Corporation to demonstrate a novel method for producing methyl chloride (CH,Cl). The project would involve design, construction, and operation of an engineering-scale oxyhydrochlorination (OHC) faci 1 i ty where methane, oxygen, and hydrogen chloride (HC1) would be reacted in a fixed-bed reactor in the presence of highly selective, stable catalysts. Unconverted methane, light hydrocarbons and HC1 would be recovered and recycled back to the OHC reactor. The methyl chloride would be absorbed in a solvent, treated by solvent stripping and then purified by distillation. Testing of the proposed OHC process would be conducted at Dow Corning's production plant in Carrollton, Carroll County, Kentucky, over a 23-month period. Based on the analyses in the EA, the DOE has determined that the proposed action is not a major Federal action significantly affecting the quality of the human environment as defined by the National Environmental Policy Act (NEPA) of 1969. -
Catalytic Reaction of Carbon Dioxide with Methane on Supported Noble Metal Catalysts
catalysts Review Catalytic Reaction of Carbon Dioxide with Methane on Supported Noble Metal Catalysts András Erd˝ohelyi Institute of Physical Chemistry and Materials Science, University of Szeged, Rerrich Béla tér 1, H-6720 Szeged, Hungary; [email protected]; Tel.: +36-62-343-638; Fax: +36-62-546-482 Abstract: The conversion of CO2 and CH4, the main components of the greenhouse gases, into synthesis gas are in the focus of academic and industrial research. In this review, the activity and stability of different supported noble metal catalysts were compared in the CO2 + CH4 reaction on. It was found that the efficiency of the catalysts depends not only on the metal and on the support but on the particle size, the metal support interface, the carbon deposition and the reactivity of carbon also influences the activity and stability of the catalysts. The possibility of the activation and dissociation of CO2 and CH4 on clean and on supported noble metals were discussed separately. CO2 could dissociate on metal surfaces, this reaction could proceed via the formation of carbonate on the support, or on the metal–support interface but in the reaction the hydrogen assisted dissociation of CO2 was also suggested. The decrease in the activity of the catalysts was generally attributed to carbon deposition, which can be formed from CH4 while others suggest that the source of the surface carbon is CO2. Carbon can occur in different forms on the surface, which can be transformed into each other depending on the temperature and the time elapsed since their formation. Basically, two reaction mechanisms was proposed, according to the mono-functional mechanism the activation of both CO2 and CH4 occurs on the metal sites, but in the bi-functional mechanism the CO2 is activated on the support or on the metal–support interface and the CH on the metal. -
ETHYLENE from METHANE (January 1994)
Abstract Process Economics Program Report No. 208 ETHYLENE FROM METHANE (January 1994) This report evaluates two routes for the production of ethylene from methane: the direct synthesis based on the oxidative coupling of methane, and the less direct chemistry of converting methanol (which is derived from methane via synthesis gas) in the presence of an aluminophosphate molecular sieve catalyst. Our evaluations indicate that at the present state of development, the economics of both routes are unattractive when compared with the steam pyrolysis of hydrocarbons. We analyze the results of our evaluations to define the technical targets that must be attained for success. We also present a comprehensive technical review that examines not only the two routes evaluated, but also some of the more promising alternative approaches, such as synthesis gas conversion via a modified Fischer-Tropsch process, ethanol synthesis by the homologation of methanol, and ethylene production via methyl chloride. This report will be of interest to petrochemical companies that produce or consume ethylene and to energy-based companies (or equivalent government organizations in various countries) that have access to or control large resources of methane-rich natural gas. PEP’91 SCN CONTENTS 1 INTRODUCTION 1-1 2 SUMMARY 2-1 TECHNICAL REVIEW 2-1 Oxidative Coupling 2-1 Methanol Conversion to Ethylene 2-3 Modified Fischer-Tropsch (FT) Process 2-3 Methanol Homologation 2-3 Conversion via Methyl Chloride 2-4 SRI’S PROCESS CONCEPTS 2-4 Ethylene from Methane by Oxidative -
Phosphine Safety Data Sheet (180KB)
Phosphine Safety Data Sheet P-4643 This SDS conforms to U.S. Code of Federal Regulations 29 CFR 1910.1200, Hazard Communication. Date of issue: 01/01/1980 Revision date: 08/31/2018 Supersedes: 10/24/2016 SECTION: 1. Product and company identification 1.1. Product identifier Product form : Substance Substance name : Phosphine CAS-No. : 7803-51-2 Formula : PH3 Other means of identification : Hydrogen phosphide, Phosphorous hydride, Phosphorous trihydride, Phosphorated hydrogen 1.2. Relevant identified uses of the substance or mixture and uses advised against Use of the substance/mixture : Industrial use; Use as directed. 1.3. Details of the supplier of the safety data sheet Praxair, Inc. 10 Riverview Drive Danbury, CT 06810-6268 - USA T 1-800-772-9247 (1-800-PRAXAIR) - F 1-716-879-2146 www.praxair.com 1.4. Emergency telephone number Emergency number : Onsite Emergency: 1-800-645-4633 CHEMTREC, 24hr/day 7days/week — Within USA: 1-800-424-9300, Outside USA: 001-703-527-3887 (collect calls accepted, Contract 17729) SECTION 2: Hazard identification 2.1. Classification of the substance or mixture GHS-US classification Pyr. Gas H250 Flam. Gas 1 H220 Press. Gas (Liq.) H280 Acute Tox. 1 (Inhalation:gas) H330 Skin Corr. 1B H314 Eye Dam. 1 H318 Aquatic Acute 1 H400 2.2. Label elements GHS-US labeling Hazard pictograms (GHS-US) : GHS02 GHS04 GHS05 GHS06 GHS09 Signal word (GHS-US) : Danger Hazard statements (GHS-US) : H220 - EXTREMELY FLAMMABLE GAS H250 - CATCHES FIRE SPONTANEOUSLY IF EXPOSED TO AIR H280 - CONTAINS GAS UNDER PRESSURE; MAY EXPLODE IF HEATED H314 - Causes severe skin burns and eye damage H330 - FATAL IF INHALED H400 - VERY TOXIC TO AQUATIC LIFE CGA-HG04 - MAY FORM EXPLOSIVE MIXTURES WITH AIR CGA-HG11 - SYMPTOMS MAY BE DELAYED Precautionary statements (GHS-US) : P202 - Do not handle until all safety precautions have been read and understood. -
NATURE [APRIL 9, 1932 Having for Comparison a Standard Benzene Bulb
546 NATURE [APRIL 9, 1932 having for comparison a standard benzene bulb. filter transmitting 250-280 p.p. was used in these ex The powder was then melted, and recrystallised by periments. The effect was shown to have its origin heating the bulb in an electric heater to about 270° C. in the phosphine molecule, but in view of the fact and very slowly cooling it. After noting the defl.exion that phosphine itself does not absorb in the region due to the bulb with the resolidified bismuth, that of 250-280 p.p., it would seem that the incidental presence the container alone was determined by breaking it of mercury vapour resulted in the phosphine being open and dissolving out the metal with nitric acid. decomposed by excited mercury atoms into hydrogen Experiments with similar bulbs and bismuth regulus atoms and probably PH or PH2 radicals, which pro showed no change of defl.exion after heat treatment. duce the Hinshelwood-Clusius effect. Hinshelwood But when bismuth powder was melted and recrystal and Clusius concluded that the active material was lised, the diamagnetic susceptibility rose nearly to the present in the gas phase, but on repeating their ex regulus value. Many samples of colloidal bismuth periment by exposing the mixture in one tube and gave similar results. determining the explosion pressure immediately after These observations indicate that the fall in the in another similar tube, the effect was not observed. susceptibility value with reduction of particle size in That is, the effect is most probably a wall phenomenon, the case of bismuth is a genuine effect. -
The Methane CO2 Equivalence 1
Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Earth Syst. Dynam. Discuss., 3, 1–29, 2012 www.earth-syst-dynam-discuss.net/3/1/2012/ Earth System doi:10.5194/esdd-3-1-2012 Dynamics ESDD © Author(s) 2012. CC Attribution 3.0 License. Discussions 3, 1–29, 2012 This discussion paper is/has been under review for the journal Earth System The methane CO Dynamics (ESD). Please refer to the corresponding final paper in ESD if available. 2 equivalence O. Boucher Comparison of physically- and Title Page Abstract Introduction economically-based CO2-equivalences for methane Conclusions References Tables Figures O. Boucher J I Laboratoire de Met´ eorologie´ Dynamique, Institut Pierre Simon Laplace, UMR8539, CNRS – Universite´ Pierre et Marie Curie, 4 place Jussieu, 75252 Paris Cedex 05, France J I Received: 4 January 2012 – Accepted: 9 January 2012 – Published: 13 January 2012 Back Close Correspondence to: O. Boucher ([email protected]) Full Screen / Esc Published by Copernicus Publications on behalf of the European Geosciences Union. Printer-friendly Version Interactive Discussion 1 Discussion Paper | Discussion Paper | Discussion Paper | Discussion Paper | Abstract ESDD There is a controversy on the role methane (and other short-lived species) should play in climate mitigation policies and no consensus on what an optimal methane 3, 1–29, 2012 CO2-equivalence should be. We revisit this question by discussing the relative mer- 5 its of physically-based (i.e. Global Warming Potential or GWP and Global Temperature The methane CO2 change Potential or GTP) and socio-economically-based climate metrics. To this effect equivalence we use a simplified Global Damage Potential (GDP) that was introduced by earlier au- O. -
Methane Emissions in the United States: Sources, Solutions & Opportunities for Reductions
Methane Emissions in the United States: Sources, Solutions & Opportunities for Reductions May 23, 2019 Presentation Overview • U.S. methane emissions & sources • Why methane matters • Methane mitigation by emission source • Spotlight on Renewable Natural Gas • Helpful tools and resources 2 U.S. Greenhouse Gas Emission Sources Source: Inventory of U.S. Greenhouse Gas Emissions and Sinks: 1990-2017 3 2017 U.S. Methane Emissions, by Source Other Coal Mining 38.3 MMTCO2e 55.7 MMTCO2e Coal Mining 8% Wastewater Treatment 14.2 MMTCO2e Oil and Natural Gas Systems 31% Landfills 107.7 MMTCO2e Oil and Natural Total Methane Gas Systems Agriculture 36% Emissions 203.3 MMTCO2e 656.3 MMTCO2e Waste 19% Enteric Fermentation Other 6% 175.4 MMTCO2e Manure Management 61.7 MMTCO2e Source: Inventory of U.S. Greenhouse Gas Emissions and Sinks: 1990-2017 4 Why Methane Matters Positive Outcomes of Capturing and Using Methane Methane Emissions Better air and water quality Trap 28 times more Methane Mitigation heat than carbon dioxide over 100 years Improved human health Opportunity to capture Contribute to ground- and convert methane Increased worker safety level ozone pollution to useful energy Enhanced energy security Create industrial safety problem Economic growth Reduced odors 5 Methane Mitigation by Emission Source • Coal Mines • Oil and Natural Gas Systems • Agriculture (Manure Management and Enteric Fermentation) • Waste (Wastewater Treatment and Landfills) 6 8% 55.7 MMTCO2e Coal Mines Total 656.3 Methane is released from MMTCO2e coal and surrounding rock ▪ Coal strata due to mining activities. In abandoned mines and surface mines, methane might also escape to the atmosphere through natural fissures or other diffuse sources. -
GLOBAL METHANE ASSESSMENT Summary for Decision Makers Copyright © United Nations Environment Programme, 2021
GLOBAL METHANE ASSESSMENT Summary for Decision Makers Copyright © United Nations Environment Programme, 2021 This publication may be reproduced in whole or in part and in any form for educational or non-profit purposes without special permission from the copyright holder, provided acknowledgement of the source is made. The United Nations Environment Programme would appreciate receiving a copy of any publication that uses this publication as a source. No use of this publication may be made for resale or for any other commercial purpose whatsoever without prior permission in writing from the United Nations Environment Programme. DISCLAIMER 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 delimitation of its frontiers or boundaries. Moreover, the views expressed do not necessarily represent the decision or the stated policy of the United Nations Environment Programme, nor does citing of trade names or commercial processes constitute endorsement. Suggested citation: United Nations Environment Programme and Climate and Clean Air Coalition (2021). Global Methane Assessment: Benefits and Costs of Mitigating Methane Emissions. Nairobi: United Nations Environment Programme. ISBN: 978-92-807-3854-4 Job No: DTI/2352/PA Global Methane Assessment / ACKNOWLEDGEMENTS 3 ACKNOWLEDGEMENTS ASSESSMENT CHAIR Drew Shindell AUTHORS A. R. Ravishankara, Johan C.I. Kuylenstierna, Eleni Michalopoulou, Lena Höglund- Isaksson, Yuqiang Zhang, Karl Seltzer, Muye Ru, Rithik Castelino, Greg Faluvegi, Vaishali Naik, Larry Horowitz, Jian He, Jean-Francois Lamarque, Kengo Sudo, William J. -
Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol
Heriot-Watt University Research Gateway Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol Citation for published version: Kapateh, MH, Chapoy, A, Burgass, RW & Tohidi Kalorazi, B 2016, 'Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol', Journal of Chemical and Engineering Data, vol. 61, no. 1, pp. 666-673. https://doi.org/10.1021/acs.jced.5b00793 Digital Object Identifier (DOI): 10.1021/acs.jced.5b00793 Link: Link to publication record in Heriot-Watt Research Portal Document Version: Peer reviewed version Published In: Journal of Chemical and Engineering Data General rights Copyright for the publications made accessible via Heriot-Watt Research Portal 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 Heriot-Watt University has made every reasonable effort to ensure that the content in Heriot-Watt Research Portal 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: 24. Sep. 2021 Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol Mahdi H Kapateh, Antonin Chapoy*, Rod Burgass, Bahman Tohidi Hydrates, Flow Assurance & Phase Equilibria, Institute of Petroleum Engineering, Heriot Watt University, EH14 4AS 1 Abstract Knowledge of hydrate inhibitor distribution is essential for the economic operation of gas transportation and processing.