scispace - formally typeset
Open AccessJournal ArticleDOI

Kinetics of carbochlorination of chromium (III) oxide

Reads0
Chats0
TLDR
In this article, the shrinking sphere model is used to describe the carbochlorination mechanism of chromium oxide and that is controlled by the chemical reaction, and the reaction order is about 1.34 and is independent of temperature.
Abstract
Kinetics of the carbochlorination of Cr2O3 has been studied with Cl2+CO gas mixtures between 500 °C to 900 °C using thermogravimetric analysis. The apparent activation energy is about 100 kJ/mol. Mathematical fitting of the experimental data suggests that the shrinking sphere model is the most adequate to describe the carbochlorination mechanism of chromium oxide and that is controlled by the chemical reaction. In the temperature range of 550 °C to 800 °C, the reaction order is about 1.34 and is independent of temperature. Changing the Cl2+CO content from 15 to 100 pct increases the reaction rate and does not affect the reaction mechanism. Similarly, changing the ratio of Cl2/(Cl2+CO) from 0.125 to 0.857 does not modify the carbochlorination mechanism of Cr2O3. In these conditions, the reaction rate passes through a maximum when using a chlorinating gas mixture having a Cl2/(Cl2+CO) ratio of about 0.5.

read more

Content maybe subject to copyright    Report

Citations
More filters
Journal ArticleDOI

An overview study of chlorination reactions applied to the primary extraction and recycling of metals and to the synthesis of new reagents

TL;DR: In this article, the authors summarized laboratory experimentation of chlorination processes developed for the extraction of tantalum and niobium from their bearing materials, the upgrading of chromite, the treatment of sulfide concentrates, and the decontamination of jarosite, as well as for the synthesis of potassium ferrate.
Journal ArticleDOI

Hot Corrosion Behavior of Some Superalloys in a Simulated Incinerator Environment at 900 °C

TL;DR: In this article, the oxide scales formed on the surface of the corroded superalloys have been characterized by FESEM, EDS, XRD, cross-sectional analysis, and x-ray mapping.
Patent

A method for increasing the chrome to iron ratio of chromites products

TL;DR: In this article, a method for increasing the chrome to iron ratio of a chromite product selected from the group consisting of ore and ore concentrate comprising the steps of mixing the chromite products with at least one salt so as to produce a mixture, whereby the concentration of salt in the mixture is selected to induce the selective chlorination of iron; and chlorinating the mixture in the presence of CO at a temperature sufficient to induce a thin film of a melt around the chromitic product and at a time able to promote the selectivechlorination of the iron, whereby an iron impoverished chromite
Journal ArticleDOI

Novel extraction route of lithium from α-spodumene by dry chlorination

TL;DR: In this article , a direct chlorination of α-spodumene using calcium chloride followed by water leaching of the residue to recover lithium was investigated, which reduced the energy requirement and number of unit operations.
Journal ArticleDOI

Kinetics of Magnesium and Calcium Extraction from Fly Ash by Carbochlorination

TL;DR: The kinetic regime of carbochlorination of Mg-and Ca-bearing compounds in fly ash was identified by chemical analysis and scanning electron microscopy in this paper, and the results showed that chemical reaction control was dominant in carbo-chlorination for Mg in the temperature range of 800°C to 1050°C.
References
More filters
Book

Gas-solid reactions

TL;DR: In this article, the authors present an integrated view of gas-solid reaction systems, where full account is taken of these new developments and where structural models of single particle systems, experimental techniques, interpretation of measurements, the design of gas solids contacting systems, and practical applications are treated in a unified manner.
Journal ArticleDOI

Recovery of Co, Ni, Mo, and V from unroasted spent hydrorefining catalysts by selective chlorination

TL;DR: In this article, the fastest chlorination kinetics were obtained using the Cl2 + CO + N2 gas mixture, followed by Cl2+ N2. And the best selective chlorination of spent hydrorefining catalysts was obtained using a Cl 2 + air gas mixture.
Journal ArticleDOI

Kinetics of chlorination and carbochlorination of pure tantalum and niobium pentoxides

TL;DR: In this article, thermogravimetric analysis of pure Nb2O-Cl and Ta2O5 systems was carried out with a shrinking sphere model between 700 °C and 1000 °C.
Journal ArticleDOI

Kinetics of Chlorination and Carbochlorination of Molybdenum Trioxide

TL;DR: In this article, the authors studied the chlorination reaction of MoO3 with Cl2-N2 gas mixture with an apparent activation energy of about 165 kJ/mole, reflecting that a chemical reaction is the rate-controlling step.
Journal ArticleDOI

Kinetics of chlorination and carbochlorination of vanadium pentoxide

TL;DR: In this paper, the authors studied the chlorination of V2O5 with Cl2-air, C12-N2, and C12 CO-N 2 gas mixtures.
Related Papers (5)
Frequently Asked Questions (14)
Q1. What are the contributions in "Kinetics of carbochlorination of chromium (iii) oxide" ?

In this paper, Ndue Kanari, B.R. Reddy, and I. Gaballah have shown that the reaction products of the carbochlorination of Cr2O3 will be CrCl2 and CrCl3 at temperatures lower and higher than 650 °C. 

They emphasized that for a reaction time of one hour, temperatures higher than 800 °C, a chlorine flow rate of about 3 L/g/h and three times the stoiciometric amount of carbon are necessary for the chlorination of the above mentioned oxides. 

To determine the effect of diluting the carbochlorinating gas mixture with nitrogen on the reaction rate, a series of experiments was performed at 550 °C, 650 °C and 800 °C with gas mixture having a Cl2+CO content that varied from 15 pct to 100 pct. 

The thermodynamic study suggests that the reaction products of the carbochlorination of Cr2O3 will be CrCl2 and CrCl3 at temperatures lower and higher than 650 °C. 

The chlorine content in the Cl2+CO gas mixture was varied from 0 to 100 pct that corresponds to a Cl2/(Cl2+CO) ratio of 0 to 1, while the total gas flow rate was kept constant at 80 L/h. 

Increasing the Cl2+CO content in the chlorinating gas mixture from 15 pct to 100 pct does not affect the carbochlorination mechanism of Cr2O3. 

Carbochlorination at low temperatures of the chromite concentrate allowsthe selective removal of iron leading to higher chromium content and Cr/Fe ratio. 

Sano and Belton [5] investigated the chlorination of Cr2O3 with Cl2-O2-Ar atmosphere using transpiration technique in the temperature range of 627 °C to 977 °C. 

The effect of Cl2+CO gas velocity on the chlorination reaction rate was studied to determine the conditions where gas starvation and mass transfer limitations could be minimized. 

It seems that the carbochlorination mechanism is again independent of the partial pressure of reactive gases in the chlorinating gas mixture. 

The reaction rate of Cr2O3 with 100 pct CO is almost equal to zero and rises with increasing the chlorine content in the gas mixture. 

Saeki et al. [2] investigated chlorination of Cr2O3 by Cl2 using samples obtained by heating a hydrated chromium oxide either at 440 °C or 1000 °C. 

During the carbochlorination of Cr2O3, the rate of formation of chromium trichloride was systematically lower than its rate of volatilization between 500 °C and 900 °C. 

Spectra of EPMA - SEM (electron probe microanalysis of the scanning electron microscope) and that of XRD (X-rays diffraction) of the sample indicate only the presence of Cr2O3 phase (Fig. 1).