Ethene, Propene, Butene and Isoprene Emissions from a Ponderosa Pine Forest Measured by Relaxed Eddy Accumulation
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
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. -
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. -
Butenes Separation, Supp. A
PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California 94025 Abstract Process Economics Program Report No. 71A BUTTLENES (October 1982) Demand is fast increasing for lsobutylene, especially that used in manufacturing methyl tertiary-butyl ether, and for high purity butene-1 to use as a copolymer in linear low density polyethylene. Because of their wide availability, mixed butane-butylene streams from oleflns plants and petroleum refineries are being increasingly fed to plants to separate butylenes for use in chemicals. This first supplement to Report No. 71 updates demand projections, production capacities, and separation techniques for high purity butene-1 and lsobutylene. The processes that are now available for separating and purifying both butene-1 and lsobutylene from mixed butyl- ene streams are evaluated and compared. Other procedures for obtaining butylenes, such as dehydrogenatlon, lsomerleatlon, and disproportion&ion, are not updated in this report. PEP’81 JLC Report No. 71A - BUTYLENES SUPPLEMENT A by JOHN L. CHADWICK I I October 1982 f-F0 0 A private report by the m PROCESS ECONOMICS PROGRAM 0 Menlo Park, California 94025 0 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICALECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLDPETROCHEMICALS Program covers major hkdrocarbons and their derivatives on a worldwide basis. In addition, the SRI DIRECTORYOF CHEMICALPRODUCERS services provide detailed lists of chemical producers by company, prod- uct, and plant for the United States and Western Europe. ii CONTENTS 1 INTRODUCTION . 1 2 SUMMARY . -
Ethylene Dichloride (Edc) Handbook
ETHYLENE DICHLORIDE (EDC) HANDBOOK OXYCHEM TECHNICAL INFORMATION 11/2014 Dallas-based Occidental Chemical Corporation is a leading North American manufacturer of basic chemicals, vinyls and performance chemicals directly and through various affiliates (collectively, OxyChem). OxyChem is also North America's largest producer of sodium chlorite. As a Responsible Care® company, OxyChem's global commitment to safety and the environment goes well beyond compliance. OxyChem's Health, Environment and Safety philosophy is a positive motivational force for our employees, and helps create a strong culture for protecting human health and the environment. Our risk management programs and methods have been, and continue to be, recognized as some of the industry's best. OxyChem offers an effective combination of industry expertise, experience, on line business tools, quality products and exceptional customer service. As a member of the Occidental Petroleum Corporation family, OxyChem represents a rich history of experience, top-notch business acumen, and sound, ethical business practices. 1 Table of Contents Page Introduction to Ethylene Dichloride ............................................................................................................ 3 Manufacturing .................................................................................................................................................. 3 Ethylene Dichloride (EDC) — Uses ................................................................................................................ -
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. -
Toxicological Profile for Ethylbenzene
ETHYLBENZENE 151 5. PRODUCTION, IMPORT/EXPORT, USE, AND DISPOSAL 5.1 PRODUCTION Ethylbenzene is primarily produced by the alkylation of benzene with ethylene in liquid-phase slurry reactors promoted with aluminum chloride catalysts or by vapor-phase reaction of benzene with dilute ethylene-containing feedstock with a boron trifluoride catalyst supported on alumina (Cannella 2007; Clayton and Clayton 1981; HSDB 2009; Welch et al. 2005; Ransley 1984). Newer versions of the method employ synthetic zeolites in fixed-bed reactors as catalysts for alkylation in the liquid phase or narrow pore synthetic zeolites in fixed-bed reactors in the vapor phase (Welch et al. 2005). Other methods of manufacturing ethylbenzene include preparation from acetophenone, dehydrogenation of naphthenes, catalytic cyclization and aromatization, separation from mixed xylenes via fractionation, reaction of ethylmagnesium bromide and chlorobenzene, extraction from coal oil, and recovery from benzene-toluene-xylene (BTX) processing(Clayton and Clayton 1981; HSDB 2009; Ransley 1984; Welch et al. 2005). Commercial grades of ethylbenzene may contain small amounts of m-xylene, p-xylene, cumene, and toluene (HSDB 2009). Ethylbenzene is traditionally ranked as one of the top 50 chemicals produced in the United States. Table 5-1 shows the historical production volumes of ethylbenzene from 1983 to 2005 (C&EN 1994a, 1994b, 1995, 2006; Kirschner 1995). Table 5-2 lists the facilities in each state that manufacture or process ethylbenzene, the intended use, and the range of maximum amounts of ethylbenzene that are stored on site. There are currently 3,755 facilities that produce, process, or use ethylbenzene in the United States. The data listed in Table 5-2 are derived from the Toxics Release Inventory (TRI06 2008). -
The Arene–Alkene Photocycloaddition
The arene–alkene photocycloaddition Ursula Streit and Christian G. Bochet* Review Open Access Address: Beilstein J. Org. Chem. 2011, 7, 525–542. Department of Chemistry, University of Fribourg, Chemin du Musée 9, doi:10.3762/bjoc.7.61 CH-1700 Fribourg, Switzerland Received: 07 January 2011 Email: Accepted: 23 March 2011 Ursula Streit - [email protected]; Christian G. Bochet* - Published: 28 April 2011 [email protected] This article is part of the Thematic Series "Photocycloadditions and * Corresponding author photorearrangements". Keywords: Guest Editor: A. G. Griesbeck benzene derivatives; cycloadditions; Diels–Alder; photochemistry © 2011 Streit and Bochet; licensee Beilstein-Institut. License and terms: see end of document. Abstract In the presence of an alkene, three different modes of photocycloaddition with benzene derivatives can occur; the [2 + 2] or ortho, the [3 + 2] or meta, and the [4 + 2] or para photocycloaddition. This short review aims to demonstrate the synthetic power of these photocycloadditions. Introduction Photocycloadditions occur in a variety of modes [1]. The best In the presence of an alkene, three different modes of photo- known representatives are undoubtedly the [2 + 2] photocyclo- cycloaddition with benzene derivatives can occur, viz. the addition, forming either cyclobutanes or four-membered hetero- [2 + 2] or ortho, the [3 + 2] or meta, and the [4 + 2] or para cycles (as in the Paternò–Büchi reaction), whilst excited-state photocycloaddition (Scheme 2). The descriptors ortho, meta [4 + 4] cycloadditions can also occur to afford cyclooctadiene and para only indicate the connectivity to the aromatic ring, and compounds. On the other hand, the well-known thermal [4 + 2] do not have any implication with regard to the reaction mecha- cycloaddition (Diels–Alder reaction) is only very rarely nism. -
Removal of NO and SO2 by Pulsed Corona Discharge Process
Korean J. Chem. Eng., 18(3), 308-316 (2001) Removal of NO and SO2 by Pulsed Corona Discharge Process Young Sun Mok†, Ho Won Lee, Young Jin Hyun, Sung Won Ham*, Jae Hak Kim** and In-Sik Nam** Department of Chemical Engineering, Cheju National University, Ara, Cheju 690-756, Korea *Department of Chemical Engineering, Kyungil University, Hayang, Kyungbuk 712-701, Korea **Department of Chemical Engineering, Pohang University of Science & Technology, Pohang, Kyungbuk 790-784, Korea (Received 6 September 2000 • accepted 9 March 2001) − Abstract Overall examination was made on the removal of NO and SO2 by pulsed corona discharge process. The mechanism for the removal of NO was found to largely depend on the gas composition. In the absence of oxygen, most of the NO removed was reduced to N2; on the other hand, oxidation of NO to NO2 was dominant in the presence of oxygen even when the content was low. Water vapor was an important ingredient for the oxidation of NO2 to nitric acid rather than that of NO to NO2. The removal of NO only slightly increased with the concentration of ammonia while the effect of ammonia on the removal of SO2 was very significant. The energy density (power delivered/feed gas flow rate) can be a measure for the degree of removal of NO. Regardless of the applied voltage and the flow rate of the feed gas stream, the amount of NO removed was identical at the same energy density. The production of N2O increased with the pulse repetition rate, and the presence of NH3 and SO2 enhanced it. -
INF.20 Economic Commission for Europe Inland Transport Committee Definition Of
INF.20 Economic Commission for Europe Inland Transport Committee Working Party on the Transport of Dangerous Goods 6 March 2012 Joint Meeting of the RID Committee of Experts and the Working Party on the Transport of Dangerous Goods Bern, 19–23 March 2012 Item 5(a) of the provisional agenda Proposals for amendments to RID/ADR/ADN: pending issues Definition of LPG Transmitted by the Government of Switzerland We have observed contradictions in the definition of LPG adopted by the Joint Meeting at its Autumn 2010 session (ECE/TRANS/WP.15/AC.1/120, Annex II) as well as in the German translation we have discussed in Erfurt during the Conference of translation and edition of the German ADR. The actual definitions in each language are the following: ""Gaz de pétrole liquéfié (GPL)", un gaz liquéfié à faible pression contenant un ou plusieurs hydrocarbures légers qui sont affectés aux numéros ONU 1011, 1075, 1965, 1969 ou 1978 seulement et qui est principalement constitué de propane, de propène, de butane, des isomères du butane, de butène avec des traces d’autres gaz d’hydrocarbures. “‘Liquefied Petroleum Gas (LPG)’ means a low pressure liquefied gas composed of one or more light hydrocarbons which are assigned to UN Nos. 1011, 1075, 1965, 1969 or 1978 only and which consists mainly of propane, propene, butane, butane isomers, butene with traces of other hydrocarbon gases. „Flüssiggas (LPG)*: Unter geringem Druck verflüssigtes Gas, das aus einem oder mehreren leichten Kohlenwasserstoffen besteht, die nur der UN-Nummer 1011, 1075, 1965, 1969 oder 1978 zugeordnet sind und das hauptsächlich aus Propan, Propen, Butan, Butan-Isomeren und Buten mit Spuren anderer Kohlenwasserstoffgase besteht.“ One important point is different between French from one side and English and German from the other side, that is that in French the repetition of the “de” in the enumeration of possible gases brings to the conclusion that the main constituent of the LPG is one of the listed gases. -
Supplement of Compilation and Evaluation of Gas Phase Diffusion Coefficients of Reactive Trace Gases in the Atmosphere
Supplement of Atmos. Chem. Phys., 15, 5585–5598, 2015 http://www.atmos-chem-phys.net/15/5585/2015/ doi:10.5194/acp-15-5585-2015-supplement © Author(s) 2015. CC Attribution 3.0 License. Supplement of Compilation and evaluation of gas phase diffusion coefficients of reactive trace gases in the atmosphere: Volume 2. Diffusivities of organic compounds, pressure-normalised mean free paths, and average Knudsen numbers for gas uptake calculations M. J. Tang et al. Correspondence to: M. J. Tang ([email protected]) and M. Kalberer ([email protected]) The copyright of individual parts of the supplement might differ from the CC-BY 3.0 licence. Table of Contents 1 Alkanes and cycloalkanes ............................................................................................ 1 1.1 CH 4 (methane), C 2H6 (ethane), and C 3H8 (propane) ............................................. 1 1.2 C 4H10 (butane, methyl propane) ............................................................................ 3 1.3 C 5H12 (n-pentane, methyl butane, dimethyl butane) ............................................. 5 1.4 C 6H14 (n-hexane, 2,3-dimethyl butane) ................................................................ 7 1.5 C 7H16 (n-heptane, 2,4-dimethyl pentane).............................................................. 9 1.6 C 8H18 (n-octane, 2,2,4-trimethyl pentane) .......................................................... 11 1.7 C 9H20 (n-nonane), C 10 H22 (n-decane, 2,3,3-trimethyl heptane) and C 12 H26 (n- dodecane) ................................................................................................................. -
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