scholarly journals Analysis on Thermal Decomposition Behavior of Fluorescein using First-order Reaction Rate Equation

2006 ◽  
Vol 122 (3) ◽  
pp. 101-106 ◽  
Author(s):  
Hajime SUGITA ◽  
Isao MATSUNAGA ◽  
Norio YANAGISAWA ◽  
Takeshi KOMAI
2014 ◽  
Vol 28 (2) ◽  
pp. 231-237 ◽  
Author(s):  
Lech W. Szajdak ◽  
Jerzy Lipiec ◽  
Anna Siczek ◽  
Artur Nosalewicz ◽  
Urszula Majewska

Abstract The aim of this study was to verify first-order kinetic reaction rate model performance in predicting of leaching of atrazine and inorganic compounds (K+1, Fe+3, Mg+2, Mn+2, NH4 +, NO3 - and PO4 -3) from tilled and orchard silty loam soils. This model provided an excellent fit to the experimental concentration changes of the compounds vs. time data during leaching. Calculated values of the first-order reaction rate constants for the changes of all chemicals were from 3.8 to 19.0 times higher in orchard than in tilled soil. Higher first-order reaction constants for orchard than tilled soil correspond with both higher total porosity and contribution of biological pores in the former. The first order reaction constants for the leaching of chemical compounds enables prediction of the actual compound concentration and the interactions between compound and soil as affected by management system. The study demonstrates the effectiveness of simultaneous chemical and physical analyses as a tool for the understanding of leaching in variously managed soils.


2019 ◽  
Vol 292 ◽  
pp. 01063
Author(s):  
Lubomír Macků

An alternative method of determining exothermic reactor model parameters which include first order reaction rate constant is described in this paper. The method is based on known in reactor temperature development and is suitable for processes with changing quality of input substances. This method allows us to evaluate the reaction substances composition change and is also capable of the reaction rate constant (parameters of the Arrhenius equation) determination. Method can be used in exothermic batch or semi- batch reactors running processes based on the first order reaction. An example of such process is given here and the problem is shown on its mathematical model with the help of simulations.


1976 ◽  
Vol 29 (2) ◽  
pp. 443 ◽  
Author(s):  
MA Haleem ◽  
MA Hakeem

Kinetic data are reported for the decarboxylation of β-resorcylic acid in resorcinol and catechol for the first time. The reaction is first order. The observation supports the view that the decomposition proceeds through an intermediate complex mechanism. The parameters of the absolute reaction rate equation are calculated.


1982 ◽  
Vol 203 (1) ◽  
pp. 117-123 ◽  
Author(s):  
E A Boeker

Excellent estimations of initial rates can be obtained from plots of delta P/t versus product formed (where P is the instantaneous concentration of the product). delta P/t is the chord from P0,t0 to P,t on an ordinary P-versus-t plot. When the chord is plotted as a function of product, the intercept at P0 of the resulting curve is necessarily dP/dt0. This curve approximates to a straight line extremely closely in all cases tested thus far. If delta P/t versus product is calculated from the integrated rate equation for a first-order reaction, and if a straight line is fitted through points representing the first 50% of the reaction, the discrepancy between the true initial rate and dP/dt0 estimated from the plot is 0.68%. For the most common form of the integrated rate equation for catalysed reactions the discrepancy varies between 0 and 0.90%. Because of the complexities of the integrated rate equations, catalysed second-order reactions have not been evaluated directly; uncatalysed reactions have been done instead. For a reaction with one reactant and two products, the discrepancy varies from 0.68 to 2.02%. For two reactants and one product, it varies from 0 to 0.68%; for two and two, 0 to 2.02%. The larger discrepancies occur only when unfavourable equilibrium constants are being overcome by the initial conditions.


2014 ◽  
Vol 625 ◽  
pp. 306-310 ◽  
Author(s):  
Nunung Prabaningrum ◽  
Lukman B. Ismail ◽  
Duvvuri Subbarao

In-situ methanolysis of Jatropha curcas had been investigated at various reaction temperatures along with reaction time. Increasing reaction temperature enhanced the yield of biodiesel and shortened the reaction completion. According to shrinking core model, the mechanism of in-situ methanolysis of Jatropha curcas was chemical reaction control with the first-order reaction. The constant of the first-order reaction rate in the range of 5.15×10-9 to 8.78×10-9 m·s-1 and Arrhenius activation energy of 22.66 kJ⋅mol-1 were obtained.


1984 ◽  
Vol 56 (2) ◽  
pp. 268-270 ◽  
Author(s):  
Joseph T. Vanderslice ◽  
Gary R. Beecher ◽  
A. Gregory. Rosenfeld

1943 ◽  
Vol 21b (5) ◽  
pp. 97-110 ◽  
Author(s):  
Sheng-Nien Wang ◽  
C. A. Winkler

Over the temperature range 377° to 448 °C, vinyl ethyl ether has been found to decompose by a first order reaction to give ethylene and acetaldehyde, at a rate given by[Formula: see text]The reaction is capable of sensitizing the decomposition of acetaldehyde and the polymerization of ethylene; this indicates that free radicals are produced during the decomposition of the ether.Nitric oxide exerts virtually no effect upon the rate of ether decomposition, although it does reduce the rates of pressure change of ether-acetaldehyde mixtures to those corresponding to ether decomposition alone.It is suggested that the decomposition of vinyl ethyl ether occurs essentially through a rearrangement mechanism, and that free radicals do not play an important part, owing possibly to the inhibiting character of this unsaturated ether.


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