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Liquid-Phase Oxidation Kinetics: Paraffin Blends
Kinetics of O2 depletion in an air-saturated (74.7 ppm O2) paraffin blend (Exxsol D-80) were conducted with a near-isothermal flowing test rig using passivated heat-exchanger tubing over the range 408−438 K. Hydroperoxide formation was monitored by cyclic voltammetry. Autoxidation data are consisten...
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Published in: | Energy & fuels 1998-11, Vol.12 (6), p.1241-1244 |
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container_title | Energy & fuels |
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creator | Pickard, James M Jones, E. Grant |
description | Kinetics of O2 depletion in an air-saturated (74.7 ppm O2) paraffin blend (Exxsol D-80) were conducted with a near-isothermal flowing test rig using passivated heat-exchanger tubing over the range 408−438 K. Hydroperoxide formation was monitored by cyclic voltammetry. Autoxidation data are consistent with an initiation mechanism involving hydroperoxide dissociation; the kinetic data are independent of the initial O2 concentration. Data analysis yielded the following rate parameters: log(k i/s-1) = (15.2 ± 1.6) − (33.1 ± 3.1)/θ, log[k iv(k i/2k v)1/2/M-1/2s-1] = (9.5 ± 0.2) − (26.3 ± 0.4)/θ, and log[(k iv/2k v)1/2/M-1/2s-1/2] = (3.3 ± 1.3) − (12.5 ± 2.6)/θ (where k i, k iv, and k v are rate constants for initiation, propagation, and termination, respectively, θ = 2.303RT kcal mol-1, R is the ideal-gas-law constant, and T is absolute temperature). Results are discussed with reference to kinetic parameters reported for conventional aviation fuels and normal paraffins. |
doi_str_mv | 10.1021/ef980063r |
format | article |
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Grant</creator><creatorcontrib>Pickard, James M ; Jones, E. Grant</creatorcontrib><description>Kinetics of O2 depletion in an air-saturated (74.7 ppm O2) paraffin blend (Exxsol D-80) were conducted with a near-isothermal flowing test rig using passivated heat-exchanger tubing over the range 408−438 K. Hydroperoxide formation was monitored by cyclic voltammetry. Autoxidation data are consistent with an initiation mechanism involving hydroperoxide dissociation; the kinetic data are independent of the initial O2 concentration. Data analysis yielded the following rate parameters: log(k i/s-1) = (15.2 ± 1.6) − (33.1 ± 3.1)/θ, log[k iv(k i/2k v)1/2/M-1/2s-1] = (9.5 ± 0.2) − (26.3 ± 0.4)/θ, and log[(k iv/2k v)1/2/M-1/2s-1/2] = (3.3 ± 1.3) − (12.5 ± 2.6)/θ (where k i, k iv, and k v are rate constants for initiation, propagation, and termination, respectively, θ = 2.303RT kcal mol-1, R is the ideal-gas-law constant, and T is absolute temperature). Results are discussed with reference to kinetic parameters reported for conventional aviation fuels and normal paraffins.</description><identifier>ISSN: 0887-0624</identifier><identifier>EISSN: 1520-5029</identifier><identifier>DOI: 10.1021/ef980063r</identifier><identifier>CODEN: ENFUEM</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Applied sciences ; Crude oil, natural gas and petroleum products ; Energy ; Exact sciences and technology ; Fuels ; Petroleum products, gas and fuels. 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Grant</creatorcontrib><title>Liquid-Phase Oxidation Kinetics: Paraffin Blends</title><title>Energy & fuels</title><addtitle>Energy Fuels</addtitle><description>Kinetics of O2 depletion in an air-saturated (74.7 ppm O2) paraffin blend (Exxsol D-80) were conducted with a near-isothermal flowing test rig using passivated heat-exchanger tubing over the range 408−438 K. Hydroperoxide formation was monitored by cyclic voltammetry. Autoxidation data are consistent with an initiation mechanism involving hydroperoxide dissociation; the kinetic data are independent of the initial O2 concentration. Data analysis yielded the following rate parameters: log(k i/s-1) = (15.2 ± 1.6) − (33.1 ± 3.1)/θ, log[k iv(k i/2k v)1/2/M-1/2s-1] = (9.5 ± 0.2) − (26.3 ± 0.4)/θ, and log[(k iv/2k v)1/2/M-1/2s-1/2] = (3.3 ± 1.3) − (12.5 ± 2.6)/θ (where k i, k iv, and k v are rate constants for initiation, propagation, and termination, respectively, θ = 2.303RT kcal mol-1, R is the ideal-gas-law constant, and T is absolute temperature). Results are discussed with reference to kinetic parameters reported for conventional aviation fuels and normal paraffins.</description><subject>Applied sciences</subject><subject>Crude oil, natural gas and petroleum products</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>Petroleum products, gas and fuels. 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Grant</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Energy & fuels</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Pickard, James M</au><au>Jones, E. Grant</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Liquid-Phase Oxidation Kinetics: Paraffin Blends</atitle><jtitle>Energy & fuels</jtitle><addtitle>Energy Fuels</addtitle><date>1998-11-16</date><risdate>1998</risdate><volume>12</volume><issue>6</issue><spage>1241</spage><epage>1244</epage><pages>1241-1244</pages><issn>0887-0624</issn><eissn>1520-5029</eissn><coden>ENFUEM</coden><abstract>Kinetics of O2 depletion in an air-saturated (74.7 ppm O2) paraffin blend (Exxsol D-80) were conducted with a near-isothermal flowing test rig using passivated heat-exchanger tubing over the range 408−438 K. Hydroperoxide formation was monitored by cyclic voltammetry. Autoxidation data are consistent with an initiation mechanism involving hydroperoxide dissociation; the kinetic data are independent of the initial O2 concentration. Data analysis yielded the following rate parameters: log(k i/s-1) = (15.2 ± 1.6) − (33.1 ± 3.1)/θ, log[k iv(k i/2k v)1/2/M-1/2s-1] = (9.5 ± 0.2) − (26.3 ± 0.4)/θ, and log[(k iv/2k v)1/2/M-1/2s-1/2] = (3.3 ± 1.3) − (12.5 ± 2.6)/θ (where k i, k iv, and k v are rate constants for initiation, propagation, and termination, respectively, θ = 2.303RT kcal mol-1, R is the ideal-gas-law constant, and T is absolute temperature). Results are discussed with reference to kinetic parameters reported for conventional aviation fuels and normal paraffins.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ef980063r</doi><tpages>4</tpages></addata></record> |
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source | American Chemical Society:Jisc Collections:American Chemical Society Read & Publish Agreement 2022-2024 (Reading list) |
subjects | Applied sciences Crude oil, natural gas and petroleum products Energy Exact sciences and technology Fuels Petroleum products, gas and fuels. Motor fuels, lubricants and asphalts |
title | Liquid-Phase Oxidation Kinetics: Paraffin Blends |
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