Heats of Combustion, Formation, and Insomerization of Ten C4 Hydrocarbons
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Analysis of Trace Hydrocarbon Impurities in 1,3-Butadiene Using Optimized Rt®-Alumina BOND/MAPD PLOT Columns by Rick Morehead, Jan Pijpelink, Jaap De Zeeuw, Tom Vezza
Petroleum & Petrochemical Applications Analysis of Trace Hydrocarbon Impurities in 1,3-Butadiene Using Optimized Rt®-Alumina BOND/MAPD PLOT Columns By Rick Morehead, Jan Pijpelink, Jaap de Zeeuw, Tom Vezza Abstract Identifying and quantifying trace impurities in 1,3-butadiene is critical in producing high quality synthetic rubber products. Stan- dard analytical methods employ alumina PLOT columns which yield good resolution for low molecular weight hydrocarbons, but suffer from irreproducibility and poor sensitivity for polar hydrocarbons. In this study, Rt®-Alumina BOND/MAPD PLOT columns were used to separate both common light polar contaminants, including methyl acetylene and propadiene, as well as 4-vinylcy- clohexene, which is a high molecular weight impurity that normally requires a second test on an alternative column. By using an extended temperature program that employs the full thermal range of the column, 4-vinylcyclohexene, as well as all of the typical low molecular weight impurities in 1,3-butadiene, can be analyzed in a single test. Introduction 1,3-butadiene is typically isolated from products of the naphtha steam cracking process. Prior to purification, 1,3-butadiene can be contaminated with significant amounts of isobutene as well as other C4 isomers. In addition to removing these C4 isomeric contaminants during purification, it is also important that 1,3-butadiene be free of propadiene and methyl acetylene, which can interfere with catalytic polymerization. Alumina PLOT columns are the most commonly used GC column for this application, but the determination of polar hydrocarbon impurities at trace levels can be quite challenging and is highly dependent on the deactiva- tion of the alumina surface. -
Ammonia, Anhydrous Ama
AMMONIA, ANHYDROUS AMA CAUTIONARY RESPONSE INFORMATION 4. FIRE HAZARDS 7. SHIPPING INFORMATION 4.1 Flash Point: 7.1 Grades of Purity: Commercial, industrial, Common Synonyms Liquefied compressed Colorless Ammonia odor Not flammable under conditions likely to refrigeration, electronic, and metaflurgical Liquid ammonia gas be encountered grades all have purity greater than 99.5% 4.2 Flammable Limits in Air: 15.50%- 7.2 Storage Temperature: Ambient for pressurized 27.00% ammonia; low temperature for ammonia at Floats and boils on water. Poisonous, visible vapor cloud is produced. 4.3 Fire Extinguishing Agents: Stop flow of atmospheric pressure Avoid contact with liquid and vapor. Keep people away. gas or liquid. Let fire burn. 7.3 Inert Atmosphere: No requirement Wear goggles, self-contained breathing apparatus, and rubber overclothing (including gloves). 4.4 Fire Extinguishing Agents Not to Be 7.4 Venting: Safety relief 250 psi for ammonia Stop discharge if possible. Used: None under pressure. Pressure-vacuum for Stay upwind and use water spray to ``knock down'' vapor. 4.5 Special Hazards of Combustion ammonia at atmospheric pressure. Call fire department. Products: Not pertinent Isolate and remove discharged material. 7.5 IMO Pollution Category: Currently not available 4.6 Behavior in Fire: Not pertinent Notify local health and pollution control agencies. 7.6 Ship Type: 2 4.7 Auto Ignition Temperature: 1204°F Protect water intakes. 7.7 Barge Hull Type: 2 4.8 Electrical Hazards: Class I, Group D Combustible. 4.9 Burning Rate: 1 mm/min. Fire 8. HAZARD CLASSIFICATIONS Wear goggles, self-contained breathing apparatus, and rubber over- 4.10 Adiabatic Flame Temperature: Currently clothing (including gloves). -
HEATS of COMBUSTION of DIAMOND and of GRAPHITE by Ralph S
r---------------___........,._ . _____~ ~_ U. S. DEPARTMENT OF COMMERCE NATIONAL BUREAU OF STANDARDS RESEARCH PAPER RP1140 Part of Journal of Research of the }.{ational Bureau of Standards, Volume 21, October 1938 HEATS OF COMBUSTION OF DIAMOND AND OF GRAPHITE By Ralph S. Jessup ABSTRACT Measurements were made of the heats of combustion of one artificial graphite, two natural graphites, and two samples of diamond. The bomb calorimeter used was calibrated electrically and by means of benzoic acid. The amount of reaction in each combustion experiment was determined from the mass of carbon dioxide formed. This method of determining the amount of reaction automatically eliminates the effect of unburned carbon and of some impurities. It was found, however, that results for different samples did not agree unless the samples were purified. Two methods of purification were used: (a) heating in vacuo to 1,800° C and (b) treatment with hydrochloric and hydrofluoric acids and subsequent heating in vacuo to 200° C to remove traces of the acids. Both methods yielded graphite containing only small amounts of impurities. The mean value obtained for the heat of combustion (-/lH) of the purified graphites in oxygen at 25° C and a constant pressure of 1 atmosphere to form gaseous carbon dioxide at the same temperature and pressure was 393.396 international kilojoules per mole (44.010 g of CO2). The maximum deviation of the mean value for anyone of the purified samples from this value was 0.021 percent. The two samples of diamond, purified by treatment with aqueous hydrochloric and hydrofluoric acids and subsequently heated in vacuo to about 570° C, had average particle sizes of 2.5 I'- and 39.5 1'-, respectively, and yielded the following respective mean values for the heat of combustion (-/lH) at 25° C and 1 atmos phere, in oxygen to form gaseous carbon dioxide: 395.771 and 395.287 interna tional kilojoules per mole. -
(C4-Naphthalene) Environmental Hazard Summary
ENVIRONMENTAL CONTAMINANTS ENCYCLOPEDIA C4-NAPHTHALENE ENTRY Note: This entry is for C4 Naphthalenes only. For naphthalene(s) in general, see Naphthalene entry. July 1, 1997 COMPILERS/EDITORS: ROY J. IRWIN, NATIONAL PARK SERVICE WITH ASSISTANCE FROM COLORADO STATE UNIVERSITY STUDENT ASSISTANT CONTAMINANTS SPECIALISTS: MARK VAN MOUWERIK LYNETTE STEVENS MARION DUBLER SEESE WENDY BASHAM NATIONAL PARK SERVICE WATER RESOURCES DIVISIONS, WATER OPERATIONS BRANCH 1201 Oakridge Drive, Suite 250 FORT COLLINS, COLORADO 80525 WARNING/DISCLAIMERS: Where specific products, books, or laboratories are mentioned, no official U.S. government endorsement is intended or implied. Digital format users: No software was independently developed for this project. Technical questions related to software should be directed to the manufacturer of whatever software is being used to read the files. Adobe Acrobat PDF files are supplied to allow use of this product with a wide variety of software, hardware, and operating systems (DOS, Windows, MAC, and UNIX). This document was put together by human beings, mostly by compiling or summarizing what other human beings have written. Therefore, it most likely contains some mistakes and/or potential misinterpretations and should be used primarily as a way to search quickly for basic information and information sources. It should not be viewed as an exhaustive, "last-word" source for critical applications (such as those requiring legally defensible information). For critical applications (such as litigation applications), it is best to use this document to find sources, and then to obtain the original documents and/or talk to the authors before depending too heavily on a particular piece of information. Like a library or many large databases (such as EPA's national STORET water quality database), this document contains information of variable quality from very diverse sources. -
BUTADIENE AS a CHEMICAL RAW MATERIAL (September 1998)
Abstract Process Economics Program Report 35D BUTADIENE AS A CHEMICAL RAW MATERIAL (September 1998) The dominant technology for producing butadiene (BD) is the cracking of naphtha to pro- duce ethylene. BD is obtained as a coproduct. As the growth of ethylene production outpaced the growth of BD demand, an oversupply of BD has been created. This situation provides the incen- tive for developing technologies with BD as the starting material. The objective of this report is to evaluate the economics of BD-based routes and to compare the economics with those of cur- rently commercial technologies. In addition, this report addresses commercial aspects of the butadiene industry such as supply/demand, BD surplus, price projections, pricing history, and BD value in nonchemical applications. We present process economics for two technologies: • Cyclodimerization of BD leading to ethylbenzene (DSM-Chiyoda) • Hydrocyanation of BD leading to caprolactam (BASF). Furthermore, we present updated economics for technologies evaluated earlier by PEP: • Cyclodimerization of BD leading to styrene (Dow) • Carboalkoxylation of BD leading to caprolactam and to adipic acid • Hydrocyanation of BD leading to hexamethylenediamine. We also present a comparison of the DSM-Chiyoda and Dow technologies for producing sty- rene. The Dow technology produces styrene directly and is limited in terms of capacity by the BD available from a world-scale naphtha cracker. The 250 million lb/yr (113,000 t/yr) capacity se- lected for the Dow technology requires the BD output of two world-scale naphtha crackers. The DSM-Chiyoda technology produces ethylbenzene. In our evaluations, we assumed a scheme whereby ethylbenzene from a 266 million lb/yr (121,000 t/yr) DSM-Chiyoda unit is combined with 798 million lb/yr (362,000 t/yr) of ethylbenzene produced by conventional alkylation of benzene with ethylene. -
Thermochemistry of Heteroatomic Compounds:Calculation of the Heat
Open Journal of Physical Chemistry, 2011, 1, 1-5 doi:10.4236/ojpc.2011.11001 Published Online May 2011 (http://www.SciRP.org/journal/ojpc) Thermochemistry of Heteroatomic Compounds: Calculation of the heat of Combustion and the heat of Formation of some Bioorganic Molecules with Different Hydrophenanthrene Rows Vitaly V. Ovchinnikov Tupolev Kazan State Technical University, St- K. Marks 10, 420111 Kazan, Russian Federation E-mail: [email protected] Received March 23rd, 2011; revised April 10th, 2011; accepted May 10th, 2011. Abstract On the basis of the known experimental heats of combustions of the seventeen alkanes in condensed state, the general equation comb HifNg has been deduced, in which i and f are correlation coefficients, N and g are a numbers of valence electrons and lone electron pairs of heteroatoms in molecule. The pre- sented dependence has been used for the calculation of the heats of combustion of thirteen organic molecules with biochemical properties: holestan, cholesterol, methyl-cholesterol, ergosterol, vitamin-D2, estradiol, an- drostenone, testosterone, androstanedione, morphine, morphinanone, codeine and pentasozine. It is noted that good convergence was obtained within the limits of errors of thermochemical experiments known in the literature and calculations of the heats of combustion for some of them were conducted. With the application of Hess law and the heats of vaporization vap H , which has been calculated with the use of a topological 1 s solvation index of the first order x , the heats of formation f H for condensed and gaseous phases were calculated for the listed bioorganic molecules. Keywords: Alkanes, Biochemical Molecules, the Heat of Combustion, Heat of Formation, Heat of Vaporiza- tion, Topological Solvation Index 1. -
Butadiene Bdi
BUTADIENE BDI CAUTIONARY RESPONSE INFORMATION 4. FIRE HAZARDS 7. SHIPPING INFORMATION 4.1 Flash Point: 7.1 Grades of Purity: Research grade: 99.86 Common Synonyms Liquefied compressed Colorless Gasoline-like odor 105°F (est.) mole% Special purity: 99.5 mole% Rubber Biethylene gas 4.2 Flammable Limits in Air: 2.0%-11.5% grade: 99.0mole% Commercial: 98% Bivinyl 4.3 Fire Extinguishing Agents: Stop flow of 7.2 Storage Temperature: Ambient 1,3-Butadiene Divinyl Floats and boils on water. Flammable visible vapor cloud is produced. gas 7.3 Inert Atmosphere: No requirement Vinyl ethylene 4.4 Fire Extinguishing Agents Not to Be 7.4 Venting: Safety relief Used: Not pertinent 7.5 IMO Pollution Category: Currently not available 4.5 Special Hazards of Combustion Restrict access. 7.6 Ship Type: 2 Avoid contact with liquid and gas. Products: Not pertinent Wear goggles, self-contained breathing apparatus, and rubber overclothing (including gloves). 4.6 Behavior in Fire: Vapors heavier than air 7.7 Barge Hull Type: 2 Shut off ignition sources and call fire department. and may travel a considerable distance Evacuate area in case of large discharge. to a source of ignition and flashback. 8. HAZARD CLASSIFICATIONS Stay upwind and use water spray to ``knock down'' vapor. Containers may explode in a fire due to Notify local health and pollution control agencies. polymerization. 8.1 49 CFR Category: Flammable gas Protect water intakes. 4.7 Auto Ignition Temperature: 788°F 8.2 49 CFR Class: 2.1 4.8 Electrical Hazards: Class 1, Group B 8.3 49 CFR Package Group: Not listed. -
Thermal Properties of Petroleum Products
UNITED STATES DEPARTMENT OF COMMERCE BUREAU OF STANDARDS THERMAL PROPERTIES OF PETROLEUM PRODUCTS MISCELLANEOUS PUBLICATION OF THE BUREAU OF STANDARDS, No. 97 UNITED STATES DEPARTMENT OF COMMERCE R. P. LAMONT, Secretary BUREAU OF STANDARDS GEORGE K. BURGESS, Director MISCELLANEOUS PUBLICATION No. 97 THERMAL PROPERTIES OF PETROLEUM PRODUCTS NOVEMBER 9, 1929 UNITED STATES GOVERNMENT PRINTING OFFICE WASHINGTON : 1929 F<ir isale by tfttf^uperintendent of Dotmrtients, Washington, D. C. - - - Price IS cants THERMAL PROPERTIES OF PETROLEUM PRODUCTS By C. S. Cragoe ABSTRACT Various thermal properties of petroleum products are given in numerous tables which embody the results of a critical study of the data in the literature, together with unpublished data obtained at the Bureau of Standards. The tables contain what appear to be the most reliable values at present available. The experimental basis for each table, and the agreement of the tabulated values with experimental results, are given. Accompanying each table is a statement regarding the esti- mated accuracy of the data and a practical example of the use of the data. The tables have been prepared in forms convenient for use in engineering. CONTENTS Page I. Introduction 1 II. Fundamental units and constants 2 III. Thermal expansion t 4 1. Thermal expansion of petroleum asphalts and fluxes 6 2. Thermal expansion of volatile petroleum liquids 8 3. Thermal expansion of gasoline-benzol mixtures 10 IV. Heats of combustion : 14 1. Heats of combustion of crude oils, fuel oils, and kerosenes 16 2. Heats of combustion of volatile petroleum products 18 3. Heats of combustion of gasoline-benzol mixtures 20 V. -
Chapter Two Properties of Ammonia
Chapter Two Properties of Ammonia Physical Properties General Anhydrous ammonia exists as either a colorless gas, colorless liquid, or white solid, depending on its pressure and temperature. In nearly all commonly encountered situations, it exists as either a liquid or a gas. The gas is less dense than air and the liquid is less dense than water at standard conditions. Ammonia gas (vapor) diffuses readily in air and the liquid is highly soluble in water with an accompanying release of heat. Ammonia exhibits classical saturation relationships whereby pressure and temperature are directly related so long as both the vapor and liquid phase are present. It does have a critical pressure and temperature. At atmospheric pressure, a closed container of ammonia vapor and liquid will be in equilibrium at a temperature of –28°F [–33°C]. It should be noted however that if liquid ammonia is spilled or released to the atmosphere at normal temperatures, the resultant pool of boiling liquid will be significantly colder than –28°F due to the law of partial pressures (the partial pressure of the ammonia vapor in the air near the liquid surface will be less than atmospheric pressure). The following table provides some of the important physical properties of ammonia. TABLE 2-1 Physical Properties of Ammonia Property Condition Value (IP) Value (SI) Molecular Weight 17.03 17.03 Color None None Physical State Room Temp Gas Gas Freezing Point P=1 atm –108°F –78°C Boiling Point P=1 atm –28.1°F –33.3°C Critical Pressure 1657 psia 11,410 kPa Critical Temp 271°F -
Fullerene Derivatives and Fullerene Superconductors H
Digital Commons @ George Fox University Faculty Publications - Department of Biology and Department of Biology and Chemistry Chemistry 1993 Fullerene Derivatives and Fullerene Superconductors H. H. Wang J. A. Schlueter A. C. Cooper J. L. Smart [email protected] M. E. Whitten See next page for additional authors Follow this and additional works at: http://digitalcommons.georgefox.edu/bio_fac Part of the Chemistry Commons, and the Physics Commons Recommended Citation Previously published in Journal of Physics and Chemistry of Solids, 1993, 54(12), 1655-1666. This Article is brought to you for free and open access by the Department of Biology and Chemistry at Digital Commons @ George Fox University. It has been accepted for inclusion in Faculty Publications - Department of Biology and Chemistry by an authorized administrator of Digital Commons @ George Fox University. For more information, please contact [email protected]. Authors H. H. Wang, J. A. Schlueter, A. C. Cooper, J. L. Smart, M. E. Whitten, U. Geiser, K. D. Carlson, J. M. Williams, U. Welp, J. D. Dudek, and M. A. Caleca This article is available at Digital Commons @ George Fox University: http://digitalcommons.georgefox.edu/bio_fac/91 Fullerene Derivatives and Fullerene Superconductors H. H. Wang, J. A. Schlueter, A. C. Cooper, J. L. Smart, M. E. Whitten, U. Geiser, K. D. Carlson, J. M. Williams, U. Welp, J. D. Dudek and M. A. Caleca Chemistry and Materials Science Divisions Argonne National Laboratory 9700 South Cass Avenue Argonne, IL 60439 DISCLAIMER This report was prepared as an account of work sponsored by an agency of the United States Government. -
Community-Scale Air Toxics Ambient Monitoring Projects (CSATAM) Summary Report
Community-Scale Air Toxics Ambient Monitoring Projects (CSATAM) Summary Report U.S. Environmental Protection Agency Office of Air Quality, Planning and Standards Air Quality Analysis Division 109 TW Alexander Drive Research Triangle Park, NC 27711 July 2009 DISCLAIMER The information presented in this document is intended as a technical resource to those conducting community-scale monitoring projects. The mention of commercial products, their source, or their use in connection with material reported herein is not to be construed as actual or implied endorsement of such products. This is document and will be updated periodically as additional final reports are delivered. The Environmental Protection Agency welcomes public input on this document at any time. Comments should be sent to Barbara Driscoll ([email protected]). FORWARD In June 2009, Eastern Research Group (ERG) under subcontract to RTI International prepared a final technical report under Contract No. EP-D-08-047, Work Assignment 1-03. The report was prepared for Barbara Driscoll of the Air Quality Assessment Division (AQAD) within the Office of Air Quality Planning and Standards (OAQPS) in Research Triangle Park, North Carolina. The report was written by Regi Ooman and was incorporated into this final report. ii TABLE OF CONTENTS Page List of Figures ................................................................................................................................... v List of Tables.................................................................................................................................... -
1 Volumetric Energy Density of Compressed Air and Compressed
Volumetric Energy Density of Compressed Air and Compressed Methane. Volumetric energy density is a combination of the potential for mechanical work, w, done by the change in pressure (P), and volume (V), and the chemical heat, q, released from burning the gas. For example, compressed air at 2,900 psi (~197 atm) has an energy density of 0.1 MJ/L calculated from PV and compressed methane (at 2,900 psi) has an energy density of 8.0 MJ/L calculated from the combination of PV and heat of combustion (Eq. 1). Estimate of Pressure Immediately After Ignition. Using the unpressurized channel volume of 1.0 mL, and our theoretically estimated temperature immediately after ignition of 2,800 oC, we calculated the maximum pressure, using the ideal gas law, to be ~1 MPa (~140 psi). Though this value is an overestimate (it does not take into account the channel volume expansion and the gas cooling, a complex calculation that is beyond the scope of this paper), we use it to illustrate the quick impulse of high pressure to use a passive valving system to control the flow of gas out of the channel after combustion and cooling. Fabrication of the Robot. The elastomer we used for the actuation layer was a stiff silicone rubber (Dragon Skin 10, DS-10; Smooth-on, Inc.). This elastomer has a greater Young’s modulus than our previous choice for pneumatic actuation (Ecoflex 00-30; Smooth-on, Inc.); pneu-nets composed of DS-10 could withstand the large forces generated within the channels during the explosion better than Ecoflex; in addition, DS-10 has a high resilience, which allowed the pneu-nets to release stored elastic energy rapidly for propulsion (Fig.