Mechanism of Deoxygenation and Cracking of Fatty Acids by Gas-Phase Cationic Complexes of Ni, Pd, and Pt

Total Page:16

File Type:pdf, Size:1020Kb

Mechanism of Deoxygenation and Cracking of Fatty Acids by Gas-Phase Cationic Complexes of Ni, Pd, and Pt reactions Article Mechanism of Deoxygenation and Cracking of Fatty Acids by Gas-Phase Cationic Complexes of Ni, Pd, and Pt Kevin Parker 1 , Victoria Pho 1, Richard A. J. O’Hair 2 and Victor Ryzhov 1,* 1 Department of Chemistry and Biochemistry, Northern Illinois University, DeKalb, IL 60115, USA; [email protected] (K.P.); [email protected] (V.P.) 2 School of Chemistry, Bio21 Institute of Molecular Science and Biotechnology, The University of Melbourne, Melbourne, VIC 3010, Australia; [email protected] * Correspondence: [email protected]; Tel.: +1-(815)-753-6871 Abstract: Deoxygenation and subsequent cracking of fatty acids are key steps in production of biodiesel fuels from renewable plant sources. Despite the fact that multiple catalysts, including those containing group 10 metals (Ni, Pd, and Pt), are employed for these purposes, little is known about the mechanisms by which they operate. In this work, we utilized tandem mass spectrometry experiments (MSn) to show that multiple types of fatty acids (saturated, mono-, and poly-unsaturated) can be catalytically deoxygenated and converted to smaller hydrocarbons using the ternary metal + complexes [(phen)M(O2CR)] ], where phen = 1,10-phenanthroline and M = Ni, Pd, and Pt. The mechanistic description of deoxygenation/cracking processes builds on our recent works describing simple model systems for deoxygenation and cracking, where the latter comes from the ability of group 10 metal ions to undergo chain-walking with very low activation barriers. This article extends our previous work to a number of fatty acids commonly found in renewable plant sources. We found that in many unsaturated acids cracking can occur prior to deoxygenation and show that mechanisms Citation: Parker, K.; Pho, V.; O’Hair, involving group 10 metals differ from long-known charge-remote fragmentation reactions. R.A.J.; Ryzhov, V. Mechanism of Deoxygenation and Cracking of Fatty Keywords: biomass; gas phase; mass spectrometry; cracking; hydrocarbons Acids by Gas-Phase Cationic Complexes of Ni, Pd, and Pt. Reactions 2021, 2, 102–114. https:// doi.org/10.3390/reactions2020009 1. Introduction Interest in biomass-derived hydrocarbons has grown due to socio-economic and Academic Editor: Dmitry Yu. Murzin environmental pressures to transition from fossil fuel to renewable resources [1–3]. Pro- duction of paraffinic fuel and biodiesel have drawbacks, with poor storage stability of the Received: 20 April 2021 fuels and unfavorable cold-flow properties that can be overcome with the new-generation Accepted: 11 May 2021 Published: 15 May 2021 methods of biomass conversion [1]. One of the main components of biomass suitable for biodiesel production is triglycerides containing fatty acids of varying lengths and degrees Publisher’s Note: MDPI stays neutral of unsaturation [4]. While thermal cracking of fatty acids was shown to produce hydro- with regard to jurisdictional claims in carbons as early as the beginning of the 20th century by Sabatier [2], oxygen-containing published maps and institutional affil- impurities pose a problem of compatibility with modern diesel engines [3]. Through de- iations. oxygenation, access to the pure hydrocarbon chain is granted and, by cracking chemistry, diesel-like hydrocarbons are produced [5]. These “drop-in” fuels can be used with little to no modification to combustion engines on the road today. Characterization of the hydrocarbons released by deoxygenation and cracking of fatty acids has been studied extensively in condensed-phase experiments [5–9]. Metal Copyright: © 2021 by the authors. Licensee MDPI, Basel, Switzerland. catalysts greatly reduce the energy (or temperature) requirements needed to afford the This article is an open access article desired hydrocarbons, with Ni, Pd, and Pt showing the greatest potential [5]. The methods distributed under the terms and of deoxygenation have been studied in multiple experiments with saturated fatty acids conditions of the Creative Commons such as stearic acid [5,6,10]. In these studies, three deoxygenation pathways have been Attribution (CC BY) license (https:// observed: (i) decarbonylation paired with dehydration, (ii) decarboxylation, or (iii) a creativecommons.org/licenses/by/ combination of both. While saturated fatty acids only exhibit cracking of the hydrocarbon 4.0/). chain after deoxygenation [10], it has been shown that, for unsaturated hydrocarbons like Reactions 2021, 2, 102–114. https://doi.org/10.3390/reactions2020009 https://www.mdpi.com/journal/reactions Reactions 2021,, 2,, FORFOR PEERPEER REVIEWREVIEW 2 Reactions 2021, 2 103 chain after deoxygenation [10], it has been shown that, for unsaturated hydrocarbons like oleicoleic acid,acid, deoxygenation deoxygenation is is not not required required for for cracking cracking [11–13]. [11–13 Variou]. Various-lengths-length alkanes, alkanes, ter- terminalminal alkenes, alkenes, and and internal internal alkenes alkenes were were alll observedobserved all observed throughthrough through Gas-chromatographyGas-chromatography Gas-chromatography (GC)(GC) (GC)after aftervarying varying temperature temperature and time and timein a heated in a heated reaction reaction chamber chamber [4]. [4]. Gas-phaseGas-phase studies, studies, often often carried carried out out via via mass mass spectrometry spectrometry (MS) (MS) experiments, experiments, provide pro- avide different a different angle forangle looking for looking at deoxygenation/cracking at deoxygenation/cracking chemistry. chemistry. For example, For example, charge- remotecharge-remote fragmentation fragmentation of unsaturated of unsaturated fatty acids fatty has acids been shownhas been to produceshown to hydrocarbons produce hy- viadrocarbons fatty acid via chain fatty cracking acid chain without cracking deoxygenation without deoxygenation [14,15]. These experiments [14,15]. These have experi- long beenments used have to long determine been used the number to determine and position the number of double and bondsposition in theof double fatty acid bonds chain in [the5]. Thefatty main acid advantage chain [5]. ofThe studying main advantage these reactions of studying in the gas these phase reactions is that, ininconjunction the gas phase with is theoreticalthat,that, inin conjunctionconjunction calculations, withwith they theoreticaltheoretical can be used calculatiocalculatio to determinens, they detailed can be used mechanisms to determine and pathway detailed energetics,mechanisms thus and allowing pathway for energetics, intelligent thus catalyst allowi designng for intelligent [16,17]. Given catalyst the design prevalence [16,17]. of unsaturatedGiven the prevalence fatty acids of found unsaturated in biomass, fatty it isacids important found toin understand biomass, it theis important mechanism to and un- chemistryderstand the involved mechanism in production and chemistry of hydrocarbons involved fromin production their cracking of hydrocarbons reactions. Recent from worktheirtheir fromcrackingcracking our reactions. groupreactions. has RecentRecent shown workwork such details fromfrom our for group the catalytic has shown deoxygenation such details and for cracking the cat- ofalytic stearic deoxygenation acid by Ni and and Pd cracking complexes of stearic studied acid by MS.by Ni The and deoxygenation Pd complexes mechanism studied by was MS. calculatedThe deoxygenation for propionic mechanism acid used was as calculated the simple for gas-phase propionic model acid for used larger as the fatty simple acids, gas- as shownphase model in Scheme for larger1[10]. fatty acids, as shown in Scheme 1 [10]. SchemeScheme 1.1. CatalyticCatalytic deoxygenation deoxygenation and and dehydrogenation dehydrogenation of propionic of propionic acid by acid ternary by ternary 1,10-phe- 1,10- phenanthrolinenanthroline and and metal metal (Ni (Ni and and Pd) Pd) complexes. complexes. OnceOnce deoxygenationdeoxygenation has has occurred, occurred, the the resulting resulting organometallic organometallic ion ion can can undergo undergo facile fac- “chainileile “chain“chain walking” walking”walking” (when (when(when the the metalthe metalmetal is Ni isis or NiNi Pd). oror Pd).Pd). The TheThe isomerization isomerizationisomerization barriers barriersbarriers were werewere shown shownshown to betoto be lowbe lowlow enough enoughenough to toto produce produceproduce a mixtureaa mixturemixture of ofof organometallic organometallicorganometallic isomers isomersisomers prior priorprior to toto fragmentation fragmentationfragmentation (Scheme(Scheme2 )[2) 18[18].]. SchemeScheme 2.2. IsomerizationIsomerization ofof of alkanealkane alkane fromfrom from alphaalpha alpha toto to betabeta beta andand and betabeta beta toto togammagamma gamma isis reversiblereversible is reversible andand and lowlow low enough in energy to be observed in simple gas-phase experiments. enoughenough inin energyenergy toto bebe observedobserved inin simplesimplegas-phase gas-phaseexperiments. experiments. TheThe subsequentsubsequent “cracking”“cracking” allowedallowed forfor anyany lengthlength ofof neutralneutral alkenealkene toto bebe extruded extruded fromfrom thethe hydrocarbonhydrocarbon chain chain [ [19–24].19–24]. ThisThis mechanismmechanism was was modeled modeled with with a a hexyl hexyl chain chain in in ourour recentrecent workwork andand cancan bebe usedused toto describedescribe thethethecracking crackingcrackingchemistry chemistrychemistry observed observedobserved in inin the thethefatty fattyfatty acidacid chemistrychemistry describeddescribed
Recommended publications
  • Cylinder Valve Selection Quick Reference for Valve Abbreviations
    SHERWOOD VALVE COMPRESSED GAS PRODUCTS Appendix Cylinder Valve Selection Quick Reference for Valve Abbreviations Use the Sherwood Cylinder Valve Series Abbreviation Chart on this page with the Sherwood Cylinder Valve Selection Charts found on pages 73–80. The Sherwood Cylinder Valve Selection Chart are for reference only and list: • The most commonly used gases • The Compressed Gas Association primary outlet to be used with each gas • The Sherwood valves designated for use with this gas • The Pressure Relief Device styles that are authorized by the DOT for use with these gases PLEASE NOTE: The Sherwood Cylinder Valve Selection Charts are partial lists extracted from the CGA V-1 and S-1.1 pamphlets. They can change without notice as the CGA V-1 and S-1.1 pamphlets are amended. Sherwood will issue periodic changes to the catalog. If there is any discrepancy or question between these lists and the CGA V-1 and S-1.1 pamphlets, the CGA V-1 and S-1.1 pamphlets take precedence. Sherwood Cylinder Valve Series Abbreviation Chart Abbreviation Sherwood Valve Series AVB Small Cylinder Acetylene Wrench-Operated Valves AVBHW Small Cylinder Acetylene Handwheel-Operated Valves AVMC Small Cylinder Acetylene Wrench-Operated Valves AVMCHW Small Cylinder Acetylene Handwheel-Operated Valves AVWB Small Cylinder Acetylene Wrench-Operated Valves — WB Style BV Hi/Lo Valves with Built-in Regulator DF* Alternative Energy Valves GRPV Residual Pressure Valves GV Large Cylinder Acetylene Valves GVT** Vertical Outlet Acetylene Valves KVAB Post Medical Valves KVMB Post Medical Valves NGV Industrial and Chrome-Plated Valves YVB† Vertical Outlet Oxygen Valves 1 * DF Valves can be used with all gases; however, the outlet will always be ⁄4"–18 NPT female.
    [Show full text]
  • A Comparative Study of the Formation of Aromatics In
    A COMPARATIVE STUDY OF THE FORMATION OF AROMATICS IN RICH METHANE FLAMES DOPED BY UNSATURATED COMPOUNDS H.A. GUENICHE, J. BIET, P.A. GLAUDE, R. FOURNET, F. BATTIN-LECLERC* Département de Chimie-Physique des Réactions, Nancy Université, CNRS, 1 rue Grandville, BP 20451, 54001 NANCY Cedex, France * E-mail : [email protected] ; Tel.: 33 3 83 17 51 25 , Fax : 33 3 83 37 81 20 ABSTRACT For a better modeling of the importance of the different channels leading to the first aromatic ring, we have compared the structures of laminar rich premixed methane flames doped with several unsaturated hydrocarbons: allene and propyne, because they are precursors of propargyl radicals which are well known as having an important role in forming benzene, 1,3-butadiene to put in evidence a possible production of benzene due to reactions of C4 compounds, and, finally, cyclopentene which is a source of cyclopentadienylmethylene radicals which in turn are expected to easily isomerizes to give benzene. These flames have been stabilized on a burner at a pressure of 6.7 kPa (50 Torr) using argon as dilutant, for equivalence ratios (φ) from 1.55 to 1.79. A unique mechanism, including the formation and decomposition of benzene and toluene, has been used to model the oxidation of allene, propyne, 1,3-butadiene and cyclopentene. The main reaction pathways of aromatics formation have been derived from reaction rate and sensitivity analyses and have been compared for the three types of additives. These combined analyses and comparisons can only been performed when a unique mechanism is available for all the studied additives.
    [Show full text]
  • Burton Introduces Thermal Cracking for Refining Petroleum John Alfred Heitmann University of Dayton, [email protected]
    University of Dayton eCommons History Faculty Publications Department of History 1991 Burton Introduces Thermal Cracking for Refining Petroleum John Alfred Heitmann University of Dayton, [email protected] Follow this and additional works at: https://ecommons.udayton.edu/hst_fac_pub Part of the History Commons eCommons Citation Heitmann, John Alfred, "Burton Introduces Thermal Cracking for Refining Petroleum" (1991). History Faculty Publications. 92. https://ecommons.udayton.edu/hst_fac_pub/92 This Encyclopedia Entry is brought to you for free and open access by the Department of History at eCommons. It has been accepted for inclusion in History Faculty Publications by an authorized administrator of eCommons. For more information, please contact [email protected], [email protected]. 573 BURTON INTRODUCES THERMAL CRACKING FOR REFINING PETROLEUM Category of event: Chemistry Time: January, 1913 Locale: Whiting, Indiana Employing high temperatures and pressures, Burton developed a large-scale chem­ ical cracking process, thus pioneering a method that met the need for more fuel Principal personages: WILLIAM MERRIAM BURTON (1865-1954), a chemist who developed a commercial method to convert high boiling petroleum fractions to gas­ oline by "cracking" large organic molecules into more useful and marketable smaller units ROBERT E. HUMPHREYS, a chemist who collaborated with Burton WILLIAM F. RODGERS, a chemist who collaborated with Burton EUGENE HOUDRY, an industrial scientist who developed a procedure us­ ing catalysts to speed the conversion process, which resulted in high­ octane gasoline Summary of Event In January, 1913, William Merriam Burton saw the first battery of twelve stills used in the thermal cracking of petroleum products go into operation at Standard Oil of Indiana's Whiting refinery.
    [Show full text]
  • High Purity/Recovery Separation of Propylene from Propyne Using Anion Pillared Metal-Organic Framework: Application of Vacuum Swing Adsorption (VSA)
    energies Article High Purity/Recovery Separation of Propylene from Propyne Using Anion Pillared Metal-Organic Framework: Application of Vacuum Swing Adsorption (VSA) Majeda Khraisheh 1, Fares AlMomani 1,* and Gavin Walker 2 1 Department of Chemical Engineering, College of Engineering, Qatar University, Doha P.O. Box 2713, Qatar; [email protected] 2 Department of Chemical Sciences, SSPC, Bernal Institute, University of Limerick, V94 T9PX Limerick, Ireland; [email protected] * Correspondence: [email protected]; Tel.: +974-4403-4140 Abstract: Propylene is one of the world’s most important basic olefin raw material used in the produc- tion of a vast array of polymers and other chemicals. The need for high purity grade of propylene is essential and traditionally achieved by the very energy-intensive cryogenic separation. In this study, 2− a pillared inorganic anion SIF6 was used as a highly selective C3H4 due to the square grid pyrazine- based structure. Single gas adsorption revealed a very high C3H4 uptake value (3.32, 3.12, 2.97 and 2.43 mmol·g−1 at 300, 320, 340 and 360 K, respectively). The values for propylene for the same tempera- tures were 2.73, 2.64, 2.31 and 1.84 mmol·g−1, respectively. Experimental results were obtained for the two gases fitted using Langmuir and Toth models. The former had a varied degree of representation of the system with a better presentation of the adsorption of the propylene compared to the propyne system. The Toth model regression offered a better fit of the experimental data over the entire range of pressures.
    [Show full text]
  • (12) United States Patent (10) Patent No.: US 8,198.491 B2 Masatoshi Et Al
    USOO8198491 B2 (12) United States Patent (10) Patent No.: US 8,198.491 B2 Masatoshi et al. (45) Date of Patent: Jun. 12, 2012 (54) PROCESS FOR PREPARING 5,986,151 A 1 1/1999 Van Der Puy 2,3,3,3-TETRAFLUOROPROPENE AND $425, 23.99 Esthet al. 1,3,3,3-TETRAFLUOROPROPENE 7,833.434 B2 11/2010 Rao et al. 2005/0245773 Al 1 1/2005 Mukhopadhyay et al. (75) Inventors: Nose Masatoshi, Settsu (JP): Komatsu 2006/0258891 A1 1 1/2006 Mukhopadhyay et al. Yuzo, Settsu (JP); Sugiyama Akinari, 3.s! .k A. 239. SgO et stal al. Situ (JP); Shibanuma Takashi, Settsu 2009,0264689 A1 10, 2009 Rao et al. (JP) 2010/0200798 A1 8, 2010 Rao et al. (73) Assignee: Daikin Industries, Ltd., Osaka (JP) FOREIGN PATENT DOCUMENTS EP O 974 571 1, 2000 (*) Notice: Subject to any disclaimer, the term of this JP 63-211245 9, 1988 patent is extended or adjusted under 35 JP 11-14.0002 5, 1999 U.S.C. 154(b) by 0 days. JP 2007-320896 12/2007 WO 2008/OO2499 1, 2008 WO 2008/OO2500 1, 2008 (21) Appl. No.: 13/057,525 WO 2008/030440 3, 2008 (22) PCT Filed: Jul. 21, 2009 OTHER PUBLICATIONS International Search Report issued Mar. 3, 2010 in International (86). PCT No.: PCT/UP2O09/063314 (PCT) Application No. PCT/JP2009/063314. S371 (c)(1) PCT Written Opinion of the International Searching Authority issued (2), (4) Date:s Feb. 4, 2011 Mar.sia. 3, 2010 in International ((PCT) ) Application NoNo. PCT/JP2009/ Haszeldine et al., “Addition of FreeRadicals to Unsaturated Systems.
    [Show full text]
  • Optimization of Refining Alkylation Process Unit Using Response
    Optimization of Refining Alkylation Process Unit using Response Surface Methods By Jose Bird, Darryl Seillier, Michael Teders, and Grant Jacobson - Valero Energy Corporation Abstract This paper illustrates a methodology to optimize the operations of an alkylation unit based on response surface methods. Trial based process optimization requires the unit to be operated across a wide range of conditions. This approach tends to be opposed by refinery operations as it can disrupt the normal operations of a process unit. Using the methods presented in this paper, the general direction of process improvement is first identified using a first order profit response surface built from available operating data. The performance of the unit is then evaluated at the refinery by making systematic changes to the key factors in the projected direction of process improvement. The operating results are then used to build a localized second order profit response surface to generate a revised set of optimum targets. Multiple linear regression models are used to predict alkylate yield, alkylate octane and Iso-stripper or De-Isobutanizer reboiler duty as a function of key process variables. These models are then used to generate a profit response surface for selection of an optimum target region for step testing at the refinery prior to implementation of the unit targets. 1. Introduction An alkylation unit takes a feed stream with a high olefin content, typically originating from a fluid catalytic cracking (FCC) unit, and adds isobutane (IC4) which reacts with the olefins to produce a high octane alkylate product. Either hydrofluoric or sulfuric acid is used as a catalyst for the alkylation reaction.
    [Show full text]
  • Invention and Innovation in the Petroleum Refining Industry
    This PDF is a selection from an out-of-print volume from the National Bureau of Economic Research Volume Title: The Rate and Direction of Inventive Activity: Economic and Social Factors Volume Author/Editor: Universities-National Bureau Committee for Economic Research, Committee on Economic Growth of the Social Science Research Council Volume Publisher: Princeton University Press Volume ISBN: 0-87014-304-2 Volume URL: http://www.nber.org/books/univ62-1 Publication Date: 1962 Chapter Title: Invention and Innovation in the Petroleum Refining Industry Chapter Author: John L. Enos Chapter URL: http://www.nber.org/chapters/c2124 Chapter pages in book: (p. 299 - 322) Invention and Innovation in the Petroleum Refining Industry JOHN L. ENOS MASSACHUSETTS INSTITUTE OF TECHNOLOGY AN INNOVATION is the combination of many different activities. Gener- ally an invention is made and recognized, capital is obtained, plant is acquired, managers and workers are hired, markets are developed, and production and distribution take place. As the innovation proceeds the original conception may be altered to make it more amenable to commercial realities. Accomplishing these activities consumes re- sources. At any point in the sequence failure may occur, delaying or even frustrating the innovation. In studying the petroleum refining industry I observed several pro- cessing innovations following one another in time and generating technological progress.' I then sought their origins in terms of the original ideas and the men who conceived them. In this paper I shall discuss the relations between the inventions and the subsequent inno- vations, focusing on the intervals between them, the returns to the inventors and innovators, and the changes in the proportions in which the factors of production in petroleum processing were combined.
    [Show full text]
  • Identification of a Simplest Hypervalent Hydrogen Fluoride
    www.nature.com/scientificreports OPEN Identification of a Simplest Hypervalent Hydrogen Fluoride Anion in Solid Argon Received: 19 December 2016 Meng-Chen Liu1, Hui-Fen Chen2, Chih-Hao Chin1, Tzu-Ping Huang1, Yu-Jung Chen3 & Yu-Jong Accepted: 18 April 2017 Wu1,4 Published: xx xx xxxx Hypervalent molecules are one of the exceptions to the octet rule. Bonding in most hypervalent molecules is well rationalized by the Rundle–Pimentel model (three-center four-electron bond), and high ionic bonding between the ligands and the central atom is essential for stabilizing hypervalent molecules. Here, we produced one of the simplest hypervalent anions, HF−, which is known to deviate from the Rundle–Pimentel model, and identified its ro-vibrational features. High-levelab inito calculations reveal that its bond dissociation energy is comparable to that of dihalides, as supported by secondary photolysis experiments with irradiation at various wavelengths. The charge distribution analysis suggested that the F atom of HF− is negative and hypervalent and the bonding is more covalent than ionic. The octet rule indicates that atoms of the main group elements tend to gain or lose electrons in order to have eight electrons in their valence shells1, 2, similar to the electronic configuration of the noble gases. Therefore, to attain this fully filled electronic configuration, atoms combine to form molecules by sharing their valence electrons to form chemical bonds. This rule is especially applicable to the period 2 and 3 elements. Most molecules are formed by following this rule and the bonding structure of molecules can be easily recognized by using Lewis electron dot diagrams.
    [Show full text]
  • Hydrogen Sulfide Capture: from Absorption in Polar Liquids to Oxide
    Review pubs.acs.org/CR Hydrogen Sulfide Capture: From Absorption in Polar Liquids to Oxide, Zeolite, and Metal−Organic Framework Adsorbents and Membranes Mansi S. Shah,† Michael Tsapatsis,† and J. Ilja Siepmann*,†,‡ † Department of Chemical Engineering and Materials Science, University of Minnesota, 421 Washington Avenue SE, Minneapolis, Minnesota 55455-0132, United States ‡ Department of Chemistry and Chemical Theory Center, University of Minnesota, 207 Pleasant Street SE, Minneapolis, Minnesota 55455-0431, United States ABSTRACT: Hydrogen sulfide removal is a long-standing economic and environ- mental challenge faced by the oil and gas industries. H2S separation processes using reactive and non-reactive absorption and adsorption, membranes, and cryogenic distillation are reviewed. A detailed discussion is presented on new developments in adsorbents, such as ionic liquids, metal oxides, metals, metal−organic frameworks, zeolites, carbon-based materials, and composite materials; and membrane technologies for H2S removal. This Review attempts to exhaustively compile the existing literature on sour gas sweetening and to identify promising areas for future developments in the field. CONTENTS 4.1. Polymeric Membranes 9785 4.2. Membranes for Gas−Liquid Contact 9786 1. Introduction 9755 4.3. Ceramic Membranes 9789 2. Absorption 9758 4.4. Carbon-Based Membranes 9789 2.1. Alkanolamines 9758 4.5. Composite Membranes 9790 2.2. Methanol 9758 N 5. Cryogenic Distillation 9790 2.3. -Methyl-2-pyrrolidone 9758 6. Outlook and Perspectives 9791 2.4. Poly(ethylene glycol) Dimethyl Ether 9759 Author Information 9792 2.5. Sulfolane and Diisopropanolamine 9759 Corresponding Author 9792 2.6. Ionic Liquids 9759 ORCID 9792 3. Adsorption 9762 Notes 9792 3.1.
    [Show full text]
  • Rich Methane Premixed Laminar Flames Doped with Light Unsaturated
    Combustion and Flame 146 (2006) 620–634 www.elsevier.com/locate/combustflame Rich methane premixed laminar flames doped with light unsaturated hydrocarbons I. Allene and propyne H.A. Gueniche, P.A. Glaude, G. Dayma, R. Fournet, F. Battin-Leclerc ∗ Département de Chimie-Physique des Réactions, Nancy University, CNRS, ENSIC, 1 rue Grandville, BP 20451, 54001 Nancy Cedex, France Received 9 February 2006; received in revised form 16 June 2006; accepted 3 July 2006 Available online 4 August 2006 Abstract The structure of three laminar premixed rich flames has been investigated: a pure methane flame and two methane flames doped by allene and propyne, respectively. The gases of the three flames contain 20.9% (mo- lar) of methane and 33.4% of oxygen, corresponding to an equivalence ratio of 1.25 for the pure methane flame. In both doped flames, 2.49% of C3H4 was added, corresponding to a ratio C3H4/CH4 of 12% and an equivalence ra- tio of 1.55. The three flames have been stabilized on a burner at a pressure of 6.7 kPa using argon as dilutant, with a gas velocity at the burner of 36 cm/s at 333 K. The concentration profiles of stable species were measured by gas chromatography after sampling with a quartz microprobe. Quantified species included carbon monoxide and diox- ide, methane, oxygen, hydrogen, ethane, ethylene, acetylene, propyne, allene, propene, propane, 1,2-butadiene, 1,3-butadiene, 1-butene, isobutene, 1-butyne, vinylacetylene, and benzene. The temperature was measured using a PtRh (6%)–PtRh (30%) thermocouple settled inside the enclosure and ranged from 700 K close to the burner up to 1850 K.
    [Show full text]
  • Cracking (Chemistry)
    Cracking (chemistry) In petrochemistry, petroleum geology and organic chemistry, cracking is the process whereby complex organic molecules such as kerogens or long-chain hydrocarbons are broken down into simpler molecules such as light hydrocarbons, by the breaking of carbon-carbon bonds in the precursors. The rate of cracking and the end products are strongly dependent on the temperature and presence of catalysts. Cracking is the breakdown of a large alkane into smaller, more useful alkenes. Simply put, hydrocarbon cracking is the process of breaking a long chain of hydrocarbons into short ones. This process requires high temperatures.[1] More loosely, outside the field of petroleum chemistry, the term "cracking" is used to describe any type of splitting of molecules under the influence of heat, catalysts and solvents, such as in processes of destructive distillation or pyrolysis. Fluid catalytic cracking produces a high yield of petrol and LPG, while hydrocracking is a major source of jet fuel, Diesel fuel, naphtha, and again yields LPG. Contents History and patents Cracking methodologies Thermal cracking Steam cracking Fluid Catalytic cracking Hydrocracking Fundamentals See also Refinery using the Shukhov cracking References process, Baku, Soviet Union, 1934. External links History and patents Among several variants of thermal cracking methods (variously known as the "Shukhov cracking process", "Burton cracking process", "Burton-Humphreys cracking process", and "Dubbs cracking process") Vladimir Shukhov, a Russian engineer, invented and patented the first in 1891 (Russian Empire, patent no. 12926, November 7, 1891).[2] One installation was used to a limited extent in Russia, but development was not followed up. In the first decade of the 20th century the American engineers William Merriam Burton and Robert E.
    [Show full text]
  • Knowledge Check Worksheet
    Knowledge check Subject area: Organic chemistry Level: 14–16 years (Higher) Topic: Cracking hydrocarbons Source: rsc.li/2SCxbLL 1. Ashley and Diane carry out an experiment to crack some liquid paraffin. Liquid paraffin is a mixture of straight chain alkane hydrocarbons containing between 5 and 15 carbon atoms in each molecule. Their equipment is shown below. Answer: Catalyst or broken pot. Answer: Product gas. Answer: Ceramic wool soaked in paraffin. a) Label the diagram by filling in the boxes. See answers above. Organic chemistry in context: © Royal Society of Chemistry Cracking hydrocarbons (H) edu.rsc.org Page 1 of 4 b) Which of the following statements are true or false about this experiment? Write your answers into the box as ‘T’ for true, or ‘F’ for false. i) A molecule of formula C6H12 could be present in the liquid TF paraffin. ii) A catalyst is added to increase the rate or speed of reaction T iii) The paraffin solidifies during the experiment. F iv) The product gas contains smaller molecules than those in T the paraffin oil. v) A Bunsen burner is used to decompose hydrocarbon T molecules. vi) A molecule of formula C2H4 could be present in the product T gas. vii) The process taking place is exothermic. F Organic chemistry in context: © Royal Society of Chemistry Cracking hydrocarbons (H) edu.rsc.org Page 2 of 4 2. The following sentences are about cracking as an industrial process. Which of the following statements are true or false about this process? Write your answers into the box as ‘T’ for true, or ‘F’ for false.
    [Show full text]