Ignition Studies of N-Heptane/Iso-Octane/Toluene Blends
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Review of Market for Octane Enhancers
May 2000 • NREL/SR-580-28193 Review of Market for Octane Enhancers Final Report J.E. Sinor Consultants, Inc. Niwot, Colorado National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401-3393 NREL is a U.S. Department of Energy Laboratory Operated by Midwest Research Institute • Battelle • Bechtel Contract No. DE-AC36-99-GO10337 May 2000 • NREL/SR-580-28193 Review of Market for Octane Enhancers Final Report J.E. Sinor Consultants, Inc. Niwot, Colorado NREL Technical Monitor: K. Ibsen Prepared under Subcontract No. TXE-0-29113-01 National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401-3393 NREL is a U.S. Department of Energy Laboratory Operated by Midwest Research Institute • Battelle • Bechtel Contract No. DE-AC36-99-GO10337 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or any agency thereof. Available electronically at http://www.doe.gov/bridge Available for a processing fee to U.S. -
APPENDIX M SUMMARY of MAJOR TYPES of Carfg2 REFINERY
APPENDIX M SUMMARY OF MAJOR TYPES OF CaRFG2 REFINERY MODIFICATIONS Appendix M: Summan/ of Major Types of CaRFG2 Refinery Modifications: Alkylation Units A process unit that combines small-molecule hydrocarbon gases produced in the FCCU with a branched chain hydrocarbon called isobutane, producing a material called alkylate, which is blended into gasoline to raise the octane rating. Alkylate is a high octane, low vapor pressure gasoline blending component that essentially contains no olefins, aromatics, or sulfur. This plant improves the ultimate gasoline-making ability of the FCC plant. Therefore, many California refineries built new or modified existing units to increase alkylate production to blend and to produce greater amounts of CaRFG2. Alkylate is produced by combining C3, C4, and C5 components with isobutane (nC4). The process of alkylation is the reverse of cracking. Olefins (such as butenes and propenes) and isobutane are used as feedstocks and combined to produce alkylate. This process enables refiners to utilize lighter components that otherwise could not be blended into gasoline due to their high vapor pressures. Feed to alkylation unit can include pentanes from light cracked gasoline treaters, isobutanes from butane isomerization unit, and C3/C4 streams from delayed coking units. Isomerization Units - C4/C5/C6 A refinery that has an alkylation plant is not likely to have exactly enough is-butane to match the proplylene and butylene (olefin) feeds. The refiner usually has two choices - buy iso-butane or make it in a butane isomerization (Bl) plant. Isomerization is the rearrangement of straight chain hydrocarbon molecules to form branched chain products or to convert normal paraffins to their isomer. -
Chemical Kinetic Research on HCCI & Diesel Fuels
Lawrence Livermore National Laboratory Chemical Kinetic Research on HCCI & Diesel Fuels William J. Pitz (PI), Charles K. Westbrook, Marco Mehl, M. Lee Davisson Lawrence Livermore National Laboratory May 12, 2009 Project ID # ace_13_pitz DOE National Laboratory Advanced Combustion Engine R&D Merit Review and Peer Evaluation Washington, DC This presentation does not contain any proprietary or confidential information This work performed under the auspices of the U.S. Department of Energy by LLNL-PRES-411416 Lawrence Livermore National Laboratory under Contract DE-AC52-07NA27344 Overview Timeline Barriers • Ongoing project with yearly • Increases in engine efficiency and direction from DOE decreases in engine emissions are being inhibited by an inadequate ability to simulate in-cylinder combustion and emission formation processes • Chemical kinetic models are critical for Budget improved engine modeling and ultimately for engine design • Funding received in FY08 and expected in FY09: Partners • 800K (DOE) • Interactions/ collaborations: DOE Working Group, National Labs, many universities, FACE Working group. Lawrence Livermore National Laboratory 2 LLNL-PRES-411416LLNL-PRES- 411416 2009 DOE Merit Review Relevance to DOE objectives Support DOE objectives of petroleum-fuel displacement by • Improving engine models so that further improvements in engine efficiency can be made • Developing models for alternative fuels (biodiesel, ethanol, other biofuels, oil-sand derived fuels, Fischer-Tropsch derived fuels) so that they can be better used -
Exposure Investigation Protocol: the Identification of Air Contaminants Around the Continental Aluminum Plant in New Hudson, Michigan Conducted by ATSDR and MDCH
Exposure Investigation Protocol - Continental Aluminum New Hudson, Lyon Township, Oakland County, Michigan Exposure Investigation Protocol: The Identification of Air Contaminants Around the Continental Aluminum Plant in New Hudson, Michigan Conducted by ATSDR and MDCH MDCH/ATSDR - 2004 Exposure Investigation Protocol - Continental Aluminum New Hudson, Lyon Township, Oakland County, Michigan TABLE OF CONTENTS OBJECTIVE/PURPOSE..................................................................................................... 3 RATIONALE...................................................................................................................... 4 BACKGROUND ................................................................................................................ 5 AGENCY ROLES .............................................................................................................. 6 ESTABLISHING CRITERIA ............................................................................................ 7 “Odor Events”................................................................................................................. 7 Comparison Values......................................................................................................... 7 METHODS ....................................................................................................................... 12 Instantaneous (“Grab”) Air Sampling........................................................................... 12 Continuous Air Monitoring.......................................................................................... -
Transition Metal Hydrides That Mediate Catalytic Hydrogen Atom Transfers
Transition Metal Hydrides that Mediate Catalytic Hydrogen Atom Transfers Deven P. Estes Submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy in the Graduate School of Arts and Sciences COLUMBIA UNIVERSITY 2014 © 2014 Deven P. Estes All Rights Reserved ABSTRACT Transition Metal Hydrides that Mediate Catalytic Hydrogen Atom Transfers Deven P. Estes Radical cyclizations are important reactions in organic chemistry. However, they are seldom used industrially due to their reliance on neurotoxic trialkyltin hydride. Many substitutes for tin hydrides have been developed but none have provided a general solution to the problem. Transition metal hydrides with weak M–H bonds can generate carbon centered radicals by hydrogen atom transfer (HAT) to olefins. This metal to olefin hydrogen atom transfer (MOHAT) reaction has been postulated as the initial step in many hydrogenation and hydroformylation reactions. The Norton group has shown MOHAT can mediate radical cyclizations of α,ω dienes to form five and six membered rings. The reaction can be done catalytically if 1) the product metalloradical reacts with hydrogen gas to reform the hydride and 2) the hydride can perform MOHAT reactions. The Norton group has shown that both CpCr(CO)3H and Co(dmgBF2)2(H2O)2 can catalyze radical cyclizations. However, both have significant draw backs. In an effort to improve the catalytic efficiency of these reactions we have studied several potential catalyst candidates to test their viability as radical cyclization catalysts. I investigate the hydride CpFe(CO)2H (FpH). FpH has been shown to transfer hydrogen atoms to dienes and styrenes. I measured the Fe–H bond dissociation free energy (BDFE) to be 63 kcal/mol (much higher than previously thought) and showed that this hydride is not a good candidate for catalytic radical cyclizations. -
Energy and the Hydrogen Economy
Energy and the Hydrogen Economy Ulf Bossel Fuel Cell Consultant Morgenacherstrasse 2F CH-5452 Oberrohrdorf / Switzerland +41-56-496-7292 and Baldur Eliasson ABB Switzerland Ltd. Corporate Research CH-5405 Baden-Dättwil / Switzerland Abstract Between production and use any commercial product is subject to the following processes: packaging, transportation, storage and transfer. The same is true for hydrogen in a “Hydrogen Economy”. Hydrogen has to be packaged by compression or liquefaction, it has to be transported by surface vehicles or pipelines, it has to be stored and transferred. Generated by electrolysis or chemistry, the fuel gas has to go through theses market procedures before it can be used by the customer, even if it is produced locally at filling stations. As there are no environmental or energetic advantages in producing hydrogen from natural gas or other hydrocarbons, we do not consider this option, although hydrogen can be chemically synthesized at relative low cost. In the past, hydrogen production and hydrogen use have been addressed by many, assuming that hydrogen gas is just another gaseous energy carrier and that it can be handled much like natural gas in today’s energy economy. With this study we present an analysis of the energy required to operate a pure hydrogen economy. High-grade electricity from renewable or nuclear sources is needed not only to generate hydrogen, but also for all other essential steps of a hydrogen economy. But because of the molecular structure of hydrogen, a hydrogen infrastructure is much more energy-intensive than a natural gas economy. In this study, the energy consumed by each stage is related to the energy content (higher heating value HHV) of the delivered hydrogen itself. -
Thermal Conductivity Correlations for Minor Constituent Fluids in Natural
Fluid Phase Equilibria 227 (2005) 47–55 Thermal conductivity correlations for minor constituent fluids in natural gas: n-octane, n-nonane and n-decaneଝ M.L. Huber∗, R.A. Perkins Physical and Chemical Properties Division, National Institute of Standards and Technology, Boulder, CO 80305, USA Received 21 July 2004; received in revised form 29 October 2004; accepted 29 October 2004 Abstract Natural gas, although predominantly comprised of methane, often contains small amounts of heavier hydrocarbons that contribute to its thermodynamic and transport properties. In this manuscript, we review the current literature and present new correlations for the thermal conductivity of the pure fluids n-octane, n-nonane, and n-decane that are valid over a wide range of fluid states, from the dilute-gas to the dense liquid, and include an enhancement in the critical region. The new correlations represent the thermal conductivity to within the uncertainty of the best experimental data and will be useful for researchers working on thermal conductivity models for natural gas and other hydrocarbon mixtures. © 2004 Elsevier B.V. All rights reserved. Keywords: Alkanes; Decane; Natural gas constituents; Nonane; Octane; Thermal conductivity 1. Introduction 2. Thermal conductivity correlation Natural gas is a mixture of many components. Wide- We represent the thermal conductivity λ of a pure fluid as ranging correlations for the thermal conductivity of the lower a sum of three contributions: alkanes, such as methane, ethane, propane, butane and isobu- λ ρ, T = λ T + λ ρ, T + λ ρ, T tane, have already been developed and are available in the lit- ( ) 0( ) r( ) c( ) (1) erature [1–6]. -
Ignition Characteristics of Heptane-Hydrogen and Heptane
international journal of hydrogen energy 36 (2011) 15392e15402 Available online at www.sciencedirect.com journal homepage: www.elsevier.com/locate/he Ignition characteristics of heptaneehydrogen and heptaneemethane fuel blends at elevated pressures S.K. Aggarwal*, O. Awomolo, K. Akber Department of Mechanical and Industrial Engineering, University of Illinois at Chicago, 842 W, Taylor St, Chicago, IL 60607, USA article info abstract Article history: There is significant interest in using hydrogen and natural gas for enhancing the perfor- Received 20 May 2011 mance of diesel engines. We report herein a numerical investigation on the ignition of Received in revised form n-C7H16/H2 and n-C7H16/CH4 fuel blends. The CHEMKIN 4.1 software is used to model 17 August 2011 ignition in a closed homogenous reactor under conditions relevant to diesel/HCCI engines. Accepted 19 August 2011 Three reaction mechanisms used are (i) NIST mechanism involving 203 species and 1463 Available online 14 September 2011 reactions, (ii) Dryer mechanism with 116 species and 754 reactions, and (iii) a reduced mechanism (Chalmers) with 42 species and 168 reactions. The parameters include pres- Keywords: sures of 30 atm and 55 atm, equivalence ratios of ɸ ¼ 0.5, 1.0 and 2.0, temperature range of e Hydrogeneheptane blends 800 1400 K, and mole fractions of H2 or CH4 in the blend between 0 and 100%. For Methaneeheptane blends n-C7H16/air mixtures, the Chalmers mechanism not only provides closer agreement with Ignition measurements compared to the other two mechanisms, but also reproduces the negative Engine conditions temperature coefficient regime. Consequently, this mechanism is used to characterize the effects of H2 or CH4 on the ignition of n-C7H16. -
Organic Chemistry Name Formula Isomers Methane CH 1 Ethane C H
Organic Chemistry Organic chemistry is the chemistry of carbon. The simplest carbon molecules are compounds of just carbon and hydrogen, hydrocarbons. We name the compounds based on the length of the longest carbon chain. We then add prefixes and suffixes to describe the types of bonds and any add-ons the molecule has. When the molecule has just single bonds we use the -ane suffix. Name Formula Isomers Methane CH4 1 Ethane C2H6 1 Propane C3H8 1 Butane C4H10 2 Pentane C5H12 3 Hexane C6H14 5 Heptane C7H16 9 Octane C8H18 18 Nonane C9H20 35 Decane C10H22 75 Isomers are compounds that have the same formula but different bonding. isobutane n-butane 1 Naming Alkanes Hydrocarbons are always named based on the longest carbon chain. When an alkane is a substituent group they are named using the -yl ending instead of the -ane ending. So, -CH3 would be a methyl group. The substituent groups are named by numbering the carbons on the longest chain so that the first branching gets the lowest number possible. The substituents are listed alphabetically with out regard to the number prefixes that might be used. 3-methylhexane 1 2 3 4 5 6 6 5 4 3 2 1 Alkenes and Alkynes When a hydrocarbon has a double bond we replace the -ane ending with -ene. When the hydrocarbon has more than three carbon the position of the double bond must be specified with a number. 1-butene 2-butene Hydrocarbons with triple bonds are named basically the same, we replace the -ane ending with -yne. -
N-Heptane (Pure Grade) Version 1.9 Revision Date 2020-05-20
SAFETY DATA SHEET n-Heptane (Pure Grade) Version 1.9 Revision Date 2020-05-20 SECTION 1: Identification of the substance/mixture and of the company/undertaking Product information Product Name : n-Heptane (Pure Grade) Material : 1119723, 1099971, 1016082, 1099970, 1084145, 1061726, 1021845, 1028621, 1021842, 1021844, 1028384, 1028355, 1021843, 10455211 Company : Chevron Phillips Chemical Company LP Specialty Chemicals 10001 Six Pines Drive The Woodlands, TX 77380 Local : See Company Address Emergency telephone: Health: 866.442.9628 (North America) 1.832.813.4984 (International) Transport: CHEMTREC 800.424.9300 or 703.527.3887(int'l) Asia: CHEMWATCH (+612 9186 1132) China: 0532 8388 9090 EUROPE: BIG +32.14.584545 (phone) or +32.14583516 (telefax) Mexico CHEMTREC 01-800-681-9531 (24 hours) South America SOS-Cotec Inside Brazil: 0800.111.767 Outside Brazil: +55.19.3467.1600 Argentina: +(54)-1159839431 Responsible Department : Product Safety and Toxicology Group E-mail address : [email protected] Website : www.CPChem.com SECTION 2: Hazards identification Classification of the substance or mixture GHS Classification and labelling according to JIS Z 7252-2019 and JIS Z 7253-2019 (GHS 2015) Classification : Flammable liquids, Category 2 Skin corrosion/irritation, Category 2 Serious eye damage/eye irritation, Category 2 Specific target organ toxicity - single exposure, Category 3, SDS Number:100000067062 1/14 SAFETY DATA SHEET n-Heptane (Pure Grade) Version 1.9 Revision Date 2020-05-20 Respiratory tract irritation, Narcotic effects Specific target organ toxicity - repeated exposure, Category 1, Nervous system Aspiration hazard, Category 1 Short-term (acute) aquatic hazard, Category 1 Long-term (chronic) aquatic hazard, Category 1 Labeling Symbol(s) : Signal Word : Danger Hazard Statements : H225: Highly flammable liquid and vapor. -
Effect of Varying the Initial Diameter of N-Octane and N-Decane Droplets
Paper # 070HE-0310 Topic: Heterogeneous combustion, sprays & droplets 8th U. S. National Combustion Meeting Organized by the Western States Section of the Combustion Institute and hosted by the University of Utah May 19-22, 2013 Effect of Varying the Initial Diameter of n-Octane and n-Decane Droplets over a Wide Range on the Spherically Symmetric Combustion Process: International Space Station and Ground-based Experiments Yu Cheng Liu 1, Koffi N. Trenou 1, Jeff Rah 1, Michael C. Hicks 2, C. Thomas Avedisian 1 1Sibley School of Mechanical and Aerospace Engineering, Cornell University, Ithaca, NY 14853. 2NASA Glenn Research Center, Cleveland, OH 44135. This study reports on an investigation of varying the initial droplet diameter (D o) over a very wide range (from 0.5 mm to 5 mm) on droplet combustion. The droplet burning history is examined in an environment of reduced convection as promoted by low gravity to achieve spherical droplet flames. The fuels examined are n-octane and n-decane. The long burning times for D o > 1.2 mm were accommodated in the Multi-user Droplet Combustion Apparatus (MDCA) onboard the orbiting International Space Station (ISS), while experiments for D o < 1 mm were carried out in a ground-based drop tower. The results reported encompass the widest range of D o examined in the history of droplet combustion experimentation for a given fuel. Both free floating (unsupported) and fiber-supported droplets are deployed and ignited. Quantitative data are obtained from digital analysis of the individual video images of the burning process for the droplet, flame and soot shell diameters. -
United States Patent [191 [11] Patent Number: 4,639,533 Finnan [45] Date of Patent: Jan
United States Patent [191 [11] Patent Number: 4,639,533 Finnan [45] Date of Patent: Jan. 27, 1987 [54] ALPHA TOCOPHEROL PROCESS [56] References Cited U.S. PATENT DOCUMENTS [75] Inventon Jeffrey L- Finn?n, Southgate, Mich- 4,191,692 3/1980 Grafen et a1. ..................... .. 549/411 4,208,334 6/1980 Fitton et a1. 549/411 [73] Assignee: BASF Corporation, Wyandotte, 4,217,2 8 5 8 / 1980 Y 05 h’mo et a 1. ................... .. 549 / 411 Mich. Primary Examiner-Nicky Chan Attorney, Agent, or Firm-Rupert B. Hurley, Jr.; Joseph [21] Appl. No.: 403,085 D. Michaels [57] ABSTRACT . _ D,1-a1pha-toc0phero1 can be prepared by reacting [22] Flled' Jul’ 29’ 1982 trimethylhydroquinone and a phytyl derivative such as phytol or isophytol in the presence of a Lewis acid, a [51] Int. Cl.4 .......................................... .. C07D 311/72 strong acid and an amine. [52] US. Cl. ............................. .. [58] Field of Search .............................. .. 549/411, 410 19 Claims, No Drawings 4,639,533 1 2 halogen-leaving groups are preferably chlorine and ALPHA TOCOPHEROL PROCESS bromine. The preferred lower alkylsulfonyloxy leaving group is mesyloxy. The preferred arylsulfonyloxy leav BACKGROUND OF THE INVENTION ing group is tosyloxy. The preferred lower alkanoyloxy 1. Field of the Invention group is acetoxy. The preferred lower alkoxy leaving This invention relates to an improved process for groups are n-butoxy, methoxy, isobutoxy, and ethoxy. manufacturing d,l-alpha-tocopherol. As used throughout the speci?cation, the term “halo 2. Description of the Prior Art gen” includes all four halogens such as bromine, chlo The preparation of d,l-alpha-tocopherol by the con rine, ?uorine and iodine.