scholarly journals Contributions of Experimental Data Obtained in Concentrated Mixtures to Kinetic Studies: Application to Monomethylhydrazine Pyrolysis

2020 ◽  
Vol 124 (30) ◽  
pp. 6214-6236
Author(s):  
Pascal Diévart ◽  
Laurent Catoire
2018 ◽  
Vol 3 (1) ◽  
pp. 4 ◽  
Author(s):  
Liudmyla Soldatkina ◽  
Marianna Zavrichko

Corn stalks (CS) were modified by a cationic surfactant, cetylpyridinium bromide (CPB), and used as an adsorbent (CS-CP) to remove anionic dyes [Acid Red (AR) and Acid Orange (AO)] from aqueous solutions. The FTIR analysis and the obtained calculations based on the determination of the adsorption capacity of CS towards CPB confirmed that the cationic surfactant had been adsorbed on the surface of corn stalks. Adsorption of the anionic dyes on modified corn stalks was investigated in a series of batch adsorption experiments at 303–328 K. The adsorption data were analyzed using Langmuir, Freundlich, and Temkin models. The Langmuir model was found to be more suitable for the experimental data of the anionic dyes on CS-CP than other adsorption models. Kinetic studies revealed that the pseudo-second order model showed the best fit to the experimental data. The thermodynamic parameters indicated that the adsorption process was spontaneous and exothermic. Mechanisms involving ion exchange and chemisorption might be responsible for the uptake of the anionic dyes on CS-CP. Obtained results imply that CS-CP could be applied as an effective adsorbent to remove anionic dyes from aqueous solutions.


1989 ◽  
Vol 11 (3) ◽  
pp. 113-118
Author(s):  
Yu-zhen Zhu ◽  
Xin Zhou ◽  
Xiang-sheng Zang

The computer-interfaced system for second-order chemical kinetic studies was applied to the determination of the rate constant of the saponification of ethyl acetate at 35°C. For this specific problem, an averaging treatment was used which can be called an interval method. The use of this method avoids the diffcully of measuring the starting time of the reaction. Two groups of experimental data and results were used to evaluate the systems performance. All of the results obtained are in agreement with the reference value.


2019 ◽  
pp. 42-51
Author(s):  
Mianovska Yana ◽  
Proidak Yuriy ◽  
Kamkina L

Purpose: to determine the effect of temperature and duration of firing on the dissociation-reduction reaction of mineral components of manganese ores. Recovery of manganese ore is carried out in four stages, which are determined by temperatures: <150°C, 150°C - 300°C, 300°C - 480°C, above 480°C. Topicality. Ores and concentrates undergo a number of complex transformations during heat treatment (agglomeration, firing of pellets and briquettes, preheating). The nature of such transformations is largely determined by chemical, mineralogical and particle size distribution, as well as other properties of the source ore. In addition to external conditions (temperature, pressure, nature of recovery, gas flow rate), the reaction rate is influenced by the physicochemical properties of the renewable substance, its mineralogical composition, structure, surface condition. The kinetic features of the reduction of pure manganese oxides are difficult to apply to manganese ores and concentrates with a rather complex structure and chemical composition. Understanding the basic chemical processes occurring in the smelting of manganese alloys is important for finding and justifying technological solutions to increase the efficiency of smelting of alloys. Method. Kinetic studies at different temperatures and fractional composition of the components under study. Results. The available literature data clearly indicate the dependence of the kinetic parameters of the processes occurring when heating manganese oxides in reducing conditions, from their physicochemical nature. To a lesser extent, process performance differs for natural minerals, although the composition of minerals may vary depending on the place of extraction. In this paper, it seems more appropriate to study the transformations that occur with manganese ores when heated, to use as an object of study the natural minerals that are part of these ores. Experimental data obtained in the study of physicochemical characteristics of the reducing processes of natural minerals can be used in the analysis of ore reduction and improvement of ferroalloy production processes. Scientific novelty. Kinetic studies of the process of interaction of minerals with reducing gas were performed at a constant heating rate of 14 degrees in the temperature range of 25-1000°C. Oxide concentrate and natural minerals lose moisture in the first 5-6 minutes. Their recovery proceeded at high speeds at temperatures of 300-4000C. A significant increase in speed was observed during the transition from a temperature of 4000C to a temperature of 6000C. Subsequent heating at 2000C led to a small increase in the total process speed. The total weight loss of the samples during heat treatment consisted of weight loss due to dissociation of manganese dioxide, weight loss due to dehydration and dissociation of carbonates that are part of the concentrate, as well as oxygen loss due to reduction. Calculations showed that the temperature of the beginning of the dissociation of MnO2 in a helium atmosphere is 460K. Dissociation of pure MnO2 is thermodynamically possible in the studied temperature range. The final decomposition product can only be manganese oxide. Practical significance. The obtained experimental data allowed to draw a conclusion about the inefficiency of grinding of oxidative manganese materials smaller than to the fraction -2.0 +1.5 mm before their heat or reduction-heat treatment in the processes of preparation of the charge for melting manganese ferroalloys. Key words: manganese ore, minerals, dissociation, kinetics, ore fractions


2021 ◽  
Vol 2063 (1) ◽  
pp. 012011
Author(s):  
Huda S Al-Niaeem ◽  
Ali A Abdulwahid ◽  
Whidad S Hanoosh

Abstract Hydrogels of acrylamide (AM), acrylamide\ 2-acrylamido-2-methyl-1-propane sulphonic acid (AMS), and acrylamide\ 2-acrylamido-2-methyl-1-propane sulphonic acid\graphene oxide (AMSGO) were prepared as adsorbents to remove carcinogenic dyes Congo red (CR) and Bismarck brown Y (BBY) from aqueous solutions. Hydrogels were characterized using FSEM and XRD analyses. For both dyes, the synthesized hydrogels demonstrated high adsorption capability at near-neutral pH. Experimental adsorption data were analyzed using the Langmuir and Freundlich isotherm models. It was found that the Langmuir model was more suitable for the experimental data. Kinetic studies found that the pseudo-second-order model demonstrated the best fitting to the experimental data. In addition, thermodynamic studies suggest that the adsorption process was spontaneous and endothermic. The prepared hydrogels were regenerated and reused in four consecutive cycles and it could be applied to remove anionic dyes from aqueous solutions as an effective adsorbent.


2014 ◽  
Vol 625 ◽  
pp. 901-906
Author(s):  
Anisa Ur Rahmah ◽  
Sabtanti Harimurti ◽  
Abdul Aziz Omar ◽  
Thanabalan Murugesan

–Oxytetracycline (OTC), a widely used of veterinary antibiotic, was degraded inside a UV/H2O2system. Kinetic study was conducted at 30°C of temperature and pH 6.37, as suggested by the previous optimization experiment. About 250, 375 and 500 ppm initial OTC concentration were used for the kinetic studies, at H2O2concentration of 0.116 M. The experimental data were plotted against the pseudo zero-th, first and second order of kinetic. Based on regression coefficient value, the data was well fitted with the pseudo first order of kinetic. The calculated value ofkobswas 0.181 min-1.


Energies ◽  
2018 ◽  
Vol 11 (9) ◽  
pp. 2481 ◽  
Author(s):  
Longwei Pan ◽  
Yong Jiang ◽  
Lei Wang ◽  
Wu Xu

The reaction models employed in the kinetic studies of biomass pyrolysis generally do not include the secondary charring reactions. The aim of this work is to propose an applicable kinetic model to characterize the pyrolysis mechanism of medium density fiberboard (MDF) and to evaluate the effects of secondary charring reactions on estimated products yields. The kinetic study for pyrolysis of MDF was performed by a thermogravimetric analyzer over a heating rate range from 10 to 40 °C/min in a nitrogen atmosphere. Four stages related to the degradation of resin, hemicellulose, cellulose, and lignin could be distinguished from the thermogravimetric analyses (TGA). Based on the four components and multi-component parallel reaction scheme, a kinetic model considering secondary charring reactions was proposed. A comparison model was also provided. An efficient optimization algorithm, differential evolution (DE), was coupled with the two models to determine the kinetic parameters. Comparisons of the results of the two models to experiment showed that the mass fraction (TG) and mass loss rate (DTG) calculated by the model considering secondary charring reactions were in better agreement with the experimental data. Furthermore, higher product yields than the experimental values will be obtained if secondary charring reactions were not considered in the kinetic study of MDF pyrolysis. On the contrary, with the consideration of secondary charring reactions, the estimated product yield had little error with the experimental data.


2016 ◽  
Vol 5 (2) ◽  
Author(s):  
Ali Hashem ◽  
Alaauddin Al-Anwar ◽  
Negma M. Nagy ◽  
Doaa M. Hussein ◽  
Sara Eisa

AbstractL. (ZscL) is a plant residue that has been used as adsorbent for the removal of Hg(II) ions from an aqueous solution. The ability of ZscL to adsorb Hg(II) ions was investigated by using the batch adsorption procedure. It was characterized by Fourier transform infrared spectroscopy (FTIR) and scanning electron microscopy (SEM) to support the adsorption of Hg(II) ions. The effects of various parameters on the adsorption process, such as contact time, adsorbent concentration, solution pH and initial concentrations of metal ions were studied to optimize the conditions for maximum adsorption. Experimental equilibrium data were fitted to the Freundlich, Langmuir, Dubinin-Radushkevich, Halsey and Temkin (two parameter models), Redlich-Peterson, Sips, Khan, Hill, Radke-Prausnitz, Langmuir-Freundlich and Toth (three parameter models), Fritz-Schlunder and Baudu (four parameter models) and Fritz-Schlunder (five parameter model) at 30°C by using nonlinear regression analysis. The examination of error analysis methods showed that the Halsey model provides the best fit for experimental data compared with the other isotherms. Various kinetic models have been applied to the experimental data to predict the adsorption kinetics. It was found that pseudo-second-order rate was better obeyed than pseudo-first-order reaction, supporting that the chemisorption process was involved. The obtained results show that ZscL can be used as an effective and natural low-cost adsorbent for the removal of Hg(II) ions from aqueous solutions.


Author(s):  
Navid Mostoufi ◽  
Ali Ghoorchian ◽  
Rahmat Sotudeh-Gharebagh

The kinetics of acetylene hydrogenation has been studied in a fixed bed reactor of a commercial Pd/Al2O3 catalyst. The experiments were carried out at 30, 50 and 70 ºC with various feed compositions at atmospheric pressure. The experiments were repeated at 70 ºC in the presence of the used catalyst to determine the effect of the catalyst deactivation where the corresponding deactivation rate constant was determined in order to predict the activity of the catalyst during each run. Two well known kinetic models were used for a nearly similar catalyst to predict the experimental data of this work and none of them were found satisfactory. A new model was then proposed to fit the experimental data. The hydrogenation reactor was also simulated at industrial operating conditions with the proposed kinetics for both plug and dispersion flows. The results of these simulations were almost close to each other in most cases.


2019 ◽  
Vol 57 (3A) ◽  
pp. 94
Author(s):  
Tam Hoang Luu ◽  
Hung Van Nguyen ◽  
Nhan Thuc Chi Ha ◽  
Khoa Nguyen Dang Vo

The adsorbent is prepared by the montmorillonite co-modification with starch for the removal of Pb (II) ions from aqueous solution. The Fourier-transformed infrared (FTIR), X-ray diffraction (XRD) spectroscopies were used to determine the structure and characteristics of the adsorbent. The main factors affecting the removal of Pb (II) ions were investigated, including the effect of pH, contact time, adsorbent dosage and the initial concentration of Pb (II). Batch process can be used for adsorption and equilibrium studies. The experimental data were fitted using Freundlich and Langmuir adsorption models. The Langmuir isotherm best fitted the experimental data with R2> 0.99 and maximum Pb (II) adsorption capacity of 21.5 mg/g indicated monolayer adsorption. Kinetic studies using pseudo-first-order and pseudo-second-order rate models showed that the process complied well with the pseudo second-order rate model.


Author(s):  
Yong Liu ◽  
Zheng Zhou ◽  
Gaodong Yang ◽  
Zhibing Zhang

The direct hydration of camphene to isoborneol has been studied in the presence of strong acidic cation exchange resins as catalyst. The effect of various parameters such as temperature, catalyst loading, mass ratio of the reactants, and reaction time on the conversion of camphene was investigated to optimize the reaction conditions. Based on the optimized reaction conditions, a novel pilot-scale jet reactor was used to study the direct hydration of camphene. The kinetic studies of direct hydration reaction have been discussed in detail. A pseudo-homogeneous (PH) model was used to correlate the experimental data in the temperature range from 353.15 K to 383.15 K. The kinetic parameters were evaluated, which made the calculated results in excellent agreement with the experimental results.


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