Use of a continuously-fed batch reactor for gas-phase mixture with many first-order reactions

1979 ◽  
Vol 34 (1) ◽  
pp. 1-4 ◽  
Author(s):  
Hong H. Lee
2020 ◽  
Vol 53 (2) ◽  
pp. 16820-16825
Author(s):  
Carlos Martínez ◽  
Jean-Luc Gouzé

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.


2013 ◽  
Vol 21 (2) ◽  
pp. 360-371 ◽  
Author(s):  
S. Bahroun ◽  
F. Couenne ◽  
C. Jallut ◽  
C. Valentin

1968 ◽  
Vol 21 (10) ◽  
pp. 2385 ◽  
Author(s):  
RL Johnson ◽  
VR Stimson

The gas-phase decomposition of 2,3-dimethylbutan-2-ol into 2,3-dimethylbut-1-ene, 2,3-dimethylbut-2-ene, and water, catalysed by hydrogen bromide at 303-400�, is described. The rate is first-order in each reactant and the Arrhenius equation k2 = 1011.88 exp(-26490/RT) sec-l ml mole-1 is followed. The olefins appear to be in their equilibrium proportions. The effects of substitutions in the alcohol at Cα and Cβ on the rate are discussed.


2019 ◽  
Vol 326 ◽  
pp. 75-81 ◽  
Author(s):  
M.A.L.R.M. Cortes ◽  
J.W.J. Hamilton ◽  
P.K. Sharma ◽  
A. Brown ◽  
M. Nolan ◽  
...  

2003 ◽  
Vol 95 (5) ◽  
pp. 1896-1900
Author(s):  
Wenfei Yan ◽  
Stephen B. Hall

Captive bubbles are commonly used to determine how interfacial films of pulmonary surfactant respond to changes in surface area, achieved by varying hydrostatic pressure. Although assumed to be isothermal, the gas phase temperature (Tg) would increase by >100°C during compression from 1 to 3 atm if the process were adiabatic. To determine the actual change in temperature, we monitored pressure (P) and volume (V) during compressions lasting <1 s for bubbles with and without interfacial films and used P · V to evaluate Tg. P · V fell during and after the rapid compressions, consistent with reductions in n, the moles of gas phase molecules, because of increasing solubility in the subphase at higher P. As expected for a process with first-order kinetics, during 1 h after the rapid compression P · V decreased along a simple exponential curve. The temporal variation of n moles of gas was determined from P · V >10 min after the compression when the two phases should be isothermal. Back extrapolation of n then allowed calculation of Tg from P · V immediately after the compression. Our results indicate that for bubbles with or without interfacial films compressed to >3 atm within 1 s, the change in Tg is <2°C.


1963 ◽  
Vol 41 (5) ◽  
pp. 1265-1275 ◽  
Author(s):  
F. H. C. Edgecombe

The polymerization of ethylene has been studied in the gas phase on a solid catalyst formed by the reaction of an organotitanium vapor with a solid crystalline titanium compound deposited on the walls of a reaction vessel.The rate of polymerization of ethylene was found to be, initially, of first order but as the reaction proceeded departure from the first-order case was observed.Experiments conducted under the condition of constant pressure as well as the usual constant-volume state enabled us, with the aid of an analogue computer, to devise a mathematical model which explained the experimental results in an unique fashion.A measure of the rate constant for catalyst decay was also obtained as well as the activation energy for the overall propagation step in the polymerization of ethylene.


1971 ◽  
Vol 24 (12) ◽  
pp. 2541 ◽  
Author(s):  
NJ Daly ◽  
F Ziolkowski

Ethyl N-methyl-N-phenylcarbamate decomposes in the gas phase over the range 329-380� to give N-methylaniline, carbon dioxide, and ethylene. The reaction is quantitative, and is first order in the carbamate. First-order rate constants are described by the equation ������������������� k1 = 1012.44 exp(-45,380/RT) (s-1) and are unaffected by the addition of cyclohexene or by increase in the surface to volume ratio of the reaction vessel. The reaction is considered to be unimolecular and likely to proceed by means of a mechanism of the type represented by the pyrolyses of acetates, xanthates, and carbonates.


Sign in / Sign up

Export Citation Format

Share Document