Hydrocarbon cool flames and the influence of hydrogen bromide

Small amounts of hydrogen bromide added to n -pentane + 1.33 O 2 mixtures lower both the limiting pressure for the onset of two-stage ignition and also, to a smaller extent, that for the appearance of cool flames. The induction period preceding the first cool flame, ז 1 , is shown to be related to the initial pressure, P 0 , by a relation of the form ז 1 = kP -n 0 + c , where k , n and c are constants for a given set of initial conditions. The results show that c ≠ 0 and that the addition of hydrogen bromide reduces both ז 1 and c . However, since ז 1 ≽ c and c is always finite, it is clear that, even at temperatures above the ignition profiles, ignition continues to take place as a two-stage process. Plots of lg ז 1 against reciprocal temper­ature are invariably characterized by a well-defined change in slope and the temperature at which this occurs decreases with increasing concentration of hydrogen bromide, eventually reaching a limiting value of ca . 270 °C. Above this temperature the slopes of the plots are more or less independent of hydrogen bromide and correspond to an overall activation energy of 82 kJ mol -1 . Below this temperature the apparent energy of activation decreases from 206 to 113 kJ mol -1 as the concentration of hydrogen bromide is increased. Similarly there is a limiting concentration of the additive above which the pressure change accompanying the first cool flame is not appreciably increased except at low temperatures. In systems which exhibit multiple cool flames, the second and fourth cool flames are generally too indistinct for their characteristics to be measured with any accuracy. However, the third cool flame appears as a well-defined but relatively weak pressure pulse. In striking contrast to the behaviour of the first cool flame, neither the third cool flame nor the induction period preceding it is appreciably affected by the presence of hydrogen bromide. It thus appears that, although the halogen compound is pre­sumably involved in the chemical reactions leading to the first cool flame, the third cool flame is propagated by intermediates whose mode of forma­tion is independent of the additive.

The progressive formation of products in the combustion of benzene and its monoalkyl derivatives has been studied by analytical methods, and the characteristic features of the isothermal reactions at various temperatures have been established. A cool-flame reaction of n -propylbenzene has also been investigated, and by comparison with corresponding isothermal combustions, it is concluded that the propagation of cool-flames is conditioned by the accumulation of a phenylalkyl hydroperoxide. The results are interpreted in the light of the theory of the two-stage process, and a schematic mechanism for the main combustion reaction is outlined. This comprises degradation of the side-chain (if present) and rupture of the benzene nucleus, followed by rapid degradation of the higher aliphatic aldehyde thus formed, yielding finally formaldehyde and the ultimate combustion products CO 2 , CO and H 2 O.


A numerical study has been undertaken to predict quantitatively each of the non-isothermal reaction modes (stationary-state reaction, oscillatory cool flames and oscillatory two-stage and multiple-stage ignitions) associated with the oxidation of ethanal in a non-adiabatic well-stirred flow system (0.5 dm 3 ) at a mean residence time of 3 s. The kinetic scheme comprises 28 species involved in 60 reactions and it is coupled to the thermal characteristics through enthalpy change in each step, heat capacities of the major components and a heat transfer coefficient appropriate to heat loss through the reaction vessel wall. Spatial uniformity of temperature and concentrations is assumed, matching the experimental conditions. Very satisfactory accord is obtained between the experimentally measured and predicted location of the different reaction modes in the ( p - T a ) ignition diagram (where p is pressure and T a is temperature at ambient conditions), and the time-dependent patterns for oscillatory reaction agree with experimental measurements. The competition between degenerate branching and non-branching reaction modes is governed ultimately by the equilibrium CH 3 +O 2 ⇌CH 3 O 2 . The predicted behaviour is found also to be especially sensitive to the rate of decomposition of the acetyl radical CH 3 CO + M → CH 3 + CO + M. Corrections for its pressure dependence are essential if the predicted form of the oscillatory cool flame region in the ( p - T a ) diagram is to match the experimental results. Variations of the rate of this reaction also give new kinetic insight into the origins of complex oscillatory wave-forms for cool flames that have been observed experimentally. Relationships between the results of the detailed kinetic computations and the predictions from a three-variable, thermokinetic model are examined. This model is the simplest of all reduced schemes that makes successful predictions of two-stage ignition phenomena.


Detailed studies have been made of the products of the cool-flame combustion of n -pentane in the absence and presence of small concentrations (2-6 vol. %) of added hydrogen bromide. In the uncatalysed reaction, acetone and acetaldehyde are the principal products formed at low temperatures during the induction period preceding the first cool flame but increasing amounts of C 5 alkenes and O-heterocycles start to be formed as the initial temperature is increased. The main effect of hydrogen bromide is to increase dramatically the yields of C 5 ketones at the expense of almost all the other products. The results indicate that in the absence of the halogen compound the principal fate of the initially formed pentylperoxy radicals is isomerisation to hydroperoxypentyl radicals. At 250 °C, the latter radicals mainly add on further oxygen and are eventually converted to pentanedihydroperoxides; at higher temperatures, the hydroperoxypentyl radicals tend increasingly to decompose directly to give principally pentenes and C 5 O-heterocycles. Hydrogen bromide alters the mechanism operating with binary mixtures primarily by providing a source of readily abstractable hydrogen and thus enhancing the formation of pentenemonohydroperoxides. Control experiments on the homogeneous breakdown of pentane-2-monohydroperoxide show that the principal decomposition product is pentan-2-one and thus confirm the probable importance of pentanemonohydroperoxides as intermediates in the HBr-promoted reaction. Studies of the chemical changes accompanying the passage of cool flames show that these vary considerably with the prevailing conditions as well as with the number of previous cool flames which have propagated through the mixture. Hydrogen bromide causes well-defined differences in the nature and distribution of the products of the combustion of n -pentane, although these changes are not as great as those brought about by the passage of cool flames which generally lead to considerable transient temperature rises in the system.


1970 ◽  
Vol 23 (6) ◽  
pp. 1149
Author(s):  
DA Kairaitis ◽  
VR Stimson

Hydrogen bromide catalyses the decomposition of propionic acid at 405-468�. The initial products are ethyl bromide, carbon monoxide, and water; however, ethyl bromide decomposes into ethylene and hydrogen bromide at rates comparable with those of the initial reaction. The kinetic form of an individual run is therefore not simple, and initial pressure change has been used to measure the rate. The reaction,is first order in each reactant, and the variation of rate with temperature is given by K2 = 1.36 x 1012exp(-30850/RT) s-1 ml mol-1 Comparison with the hydrogen bromide catalysed decarbonylations of other acids and esters has been made. Isobutene added to the reaction affects the kinetic form of individual runs slightly and mainly through its effect on the decomposition of ethyl bromide.


Previous work has demonstrated that knock in the spark-ignition engine is a phenomenon confined to the last part of the charge to burn, and that it is the chemical reactions in this ‘ end-gas ’ which determine whether or not knock will occur. The purpose of this paper is to try to elucidate the nature of these reactions and to discover some of the critical chemical factors controlling the occur­- rence of knock. This has been done in three main ways: ( a ) the sequence of chemical reactions occurring in the ‘end-gas’ prior to knock has been followed by means of a specially designed electromagnetic gas-sampling valve which can abstract samples of this gas at various stages in the combustion cycle, ( b ) the effect of the addition of various substances to the cylinder charge on the knock-limited compression ratio of the engine has been determined and ( c ) a study has been made in a motored engine of the limits of cool and hot flame formation. Ricardo E. 6 variable-compression engines were used for all these investigations. Preliminary tests with small quantities of additives, such as azomethane, alkyl nitrites and nitrates, carbon tetrachloride and chloropicrin, demonstrated that substances which would be expected to give rise to free radicals in the engine cylinder are strong pro-knocks. This and the anti-knock action of minute quantities of additives such as lead tetraethyl show the chain nature of the reactions leading to knock. Experiments are described to demonstrate that these reactions are substantially independent of the nature of the cylinder walls. Qualitative sampling tests indicated that knock depends not so much on the formation of some new substance which was not present under non-knocking conditions but rather on the attainment of a critical rate of formation of products present under both conditions. Further experiments with additives in which various intermediate products of reaction, such as aldehydes, nitrogen peroxide and organic peroxides, were tested, showed that with normal fuels the organic peroxides were the only products which were strongly pro-knock and formaldehyde the only product which had an anti-knock effect. This led to the subsequent sampling investigation being concentrated largely on the estimation of these two products in the ‘end-gases’. A method for analyzing for organic peroxides in small concentration and in the presence of other reaction products, such as nitrogen peroxide, was developed. Use of this method with a higher paraffinic fuel showed that peroxide formation was two-stage in nature. The first stage culminated in the formation of a point of inflexion or small peak in the curve of peroxide concentration about 1 ° after top dead centre. In the second stage the curve normally rose again to a higher peak at about 7° 1. Lead tetraethyl had a much greater depressing effect on the peak at 7° L compared with that at 1° 1. The mixture strength giving maximum knock was the same as that giving maximum peroxide concentration. Analyses were also made for aldehydes, shown to be mainly formaldehyde. The main growth of the formaldehyde formation took place in the second of the two stages of peroxide formation. A much smaller quantity of peroxide appeared to be formed when methane was the fuel, and this was eliminated when lead tetraethyl was added to suppress the knock. Benzene formed no peroxides, and none was detected with the alkyl benzenes up to cumene. This difference between benzene and methane on the one hand and the higher paraffinic fuels on the other in regard to peroxide formation was paralleled by the different effect of additives on the two classes of fuel. Formaldehyde was an anti-knock in the latter class and a pro-knock in the former class; acetaldehyde and benzaldehyde were ineffective in the latter but strongly pro-knock in the former; nitrogen peroxide has only a slight pro-knock effect in the latter but was strongly pro­ knock in the former. Experiments with the higher paraffinic fuels on a motored engine showed that if conditions of temperature and pressure were such as to simulate those obtaining in the ‘end-gas’ prior to knock, cool flames were formed at a time in the cycle approximately corresponding to the point of inflexion of the peroxide sampling curves. No cool flames were detected with benzene or methane. Bright blue flames were observed near the ignition point over certain ranges of mixture strength with benzene and methane as well as with the higher paraffins. Non-engine work has shown the existence of two main types of combustion, namely, so-called ‘low’- and ‘ high ’-temperature types. Of these the first is associated with peroxide and cool-flame formation, ignition taking place by a two-stage process, whereas ignition of the second type is a single-stage process and not usually associated with cool flames or peroxide formation. From the evidence of (1) the peroxide analyses, (2) the experiments with additives and (3) the experiments with a motored engine, it is clear that normal fuels knock by the ‘low’-temperature process but that benzene and methane knock by the ‘ high’-temperature process. Experiments in which formaldehyde was used as a fuel and the effect of various additives on its knock limit determined, showed that its oxidation is best classified as of the ‘ high ’-temperature type and yielded further understanding of the nature of the reactions leading to knock. The effect of hydrogen as an additive with other fuels and the effect of various additives on its own highest useful compression ratio was determined. No peroxides were detected in engine samples when hydrogen was used as the fuel.


2015 ◽  
Vol 6 (1) ◽  
pp. 143-156
Author(s):  
Arnon Atzmon

The question of the Sitz im Leben of Pesikta de-Rav Kahana and how it affected its redaction and formulation is one of the most fascinating issues in the study of the aggadic midrashim. In this article, I conduct a detailed analysis of the piska referred to as “In the Third Month,” elucidating its character and nature primarily by comparing it to passages found in parallel midrashim. This analysis reveals that the extant piska was created in a two-stage process. First, the original darshan or redactor created midrashic material pertaining to the Shavuot Torah reading from Exod 19–20, the revelation of the Torah at Sinai which had recently replaced the older Shavuot reading connected to the agricultural aspect of the festival. Subsequently a later redactor of the Pesikta augmented the original piska by adding two midrashic passages drawn from the Tanhuma literature. Analysis of the dynamics involved in the creation and redaction of this particular piska sheds light not only on this text but on the connection between the liturgical and literary processes at work in this period as a whole. Most importantly, it affords us a glimpse into the link between the midrashim and actual synagogue life in the amoraic period.


The oxidation of butane ([C 4 H 10 ] : [ O 2 ] = 1.13:1.00) has been studied over the temperature and pressure ranges 371 ⩽ T/ K ⩽ 675, 226 ⩽ P /Torr ⩽ 489 in a jet stirred reactor with a residence time of 9.4 s (1 Torr ≈ 133.3 Pa), The gas temperature and pressure were probed and phase diagrams constructed delineating regions of oscillatory ignitions and cool flames, and high- and low -temperature stationary states. On heating at an initial pressure of 400 Torr from 570 K sharp transitions were observed, first to an oscillatory ignition and then to an oscillatory cool flame region, followed by a smooth transition to a high-temperature stationary state via a supercritical Hopf bifurcation. On cooling from this high - temperature stationary state, oscillatory cool flames were observed with a sharp extinction at 542 K, without any entry to the oscillatory ignition region. The latter could be entered, however, by suddenly cooling the system from the oscillatory cool flame region by temporarily substituting nitrogen for oxygen in the gas streams. Complex waveforms, consisting of bursts of oscillatory cool flames interspersed with periods of monotonic cooling, were also observed at lower pressures. A Nd : YAG pumped dye laser was used to probe laser induced fluorescence from form aldehyde in the oscillatory ignition region. Variations in the internal surface of the reactor demonstrated the significance of surface reactions. An outline mechanism, based on detailed numerical simulations, is presented to account for the shape of the ignition profiles and the transition from multiple ignitions to oscillatory cool flames.


Energies ◽  
2021 ◽  
Vol 14 (12) ◽  
pp. 3703
Author(s):  
Ming-Chien Hsiao ◽  
Wei-Ting Lin ◽  
Wei-Cheng Chiu ◽  
Shuhn-Shyurng Hou

In this study, ultrasound was used to accelerate two-stage (esterification–transesterification) catalytic synthesis of biodiesel from used cooking oil, which originally had a high acid value (4.35 mg KOH/g). In the first stage, acid-catalyzed esterification reaction conditions were developed with a 9:1 methanol/oil molar ratio, sulfuric acid dosage at 2 wt %, and a reaction temperature of 60 °C. Under ultrasound irradiation for 40 min, the acid value was effectively decreased from 4.35 to 1.67 mg KOH/g, which was decreased to a sufficient level (<2 mg KOH/g) to avoid the saponification problem for the subsequent transesterification reaction. In the following stage, base-catalyzed transesterification reactions were carried out with a 12:1 methanol/oil molar ratio, a sodium hydroxide dosage of 1 wt %, and a reaction temperature of 65 °C. Under ultrasound-assisted transesterification for 40 min, the conversion rate of biodiesel reached 97.05%, which met the requirement of EN 14214 standard, i.e., 96.5% minimum. In order to evaluate and explore the improvement of the ultrasound-assisted two-stage (esterification–transesterification) process in shortening the reaction time, additional two-stage biodiesel synthesis experiments using the traditional mechanical stirring method under the optimal conditions were further carried out in this study. It was found that, under the same optimal conditions, using the ultrasound-assisted two-stage process, the total reaction time was significantly reduced to only 80 min, which was much shorter than the total time required by the conventional method of 140 min. It is worth noting that compared with the traditional method without ultrasound, the intensification of the ultrasound-assisted two-stage process significantly shortened the total time from 140 min to 80 min, which is a reduction of 42.9%. It was concluded that the ultrasound-assisted two-stage (esterification–transesterification) catalytic process is an effective and time-saving method for synthesizing biodiesel from used cooking oil with a high acid value.


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