Kinetics of H₂S Reaction with Calcined Calcium-Based Sorbents

Abstract

Sulfidation experiments at atmospheric pressure in a thermogravimetric analyzer were performed with two calcined limestones and a fully calcined dolomite at temperatures between 450 and 700 °C and with sorbent particle sizes between 0.4 and 1.6 mm. The effects of reaction temperature, sorbent particle size, and H2S concentration were analyzed. The sulfidation rate of the dolomite and a limestone increased with temperature in all of the ranges tested. However, the sulfidation rate of the other limestone increased with temperature until 600 °C and was nearly constant from this temperature. The temperature effect on the conversion versus time curves diminished with increasing particle size. At low temperatures (<500−550 °C) the sulfidation rate did not depend on sorbent particle size. On the other hand, at temperatures above 500−550 °C the sulfidation rate increased with decreasing sorbent particle size due to the effect of the intraparticle diffusion. This finding was in agreement with the SEM-EDX sulfur distribution profiles measured in partially sulfided sorbent particles. The sulfidation rate increased when the H2S pressure was raised, and a reaction order in H2S of 1 could adequately describe the sulfidation reaction of the sorbents. The changing grain size model proposed by Georgakis et al. together with the molecular scale hypotheses of Attar and Dupuis was used to determine the kinetic parameters of the reaction and to test its ability to predict the data for the sulfidation reaction over a broad range of particle sizes and temperatures. Good agreement between measured and predicted conversion time curves and sulfur distributions inside the particles was observed. The values of the activation energies varied from 29.1 to 56.5 kJ mol-1 to calculate the chemical reaction rate constant, k s, and from 154.6 to 217.5 kJ mol-1 to calculate the product layer diffusion coefficient, D s. Analysis of the kinetic parameters showed that the resistance due to the chemical reaction on the overall reaction rate increased in relation to the resistance of the H2S diffusion through the product layer with increasing the reaction temperature. This effect was very similar for the two limestones and higher than for the dolomite.

In situ gasification Chemical-Looping Combustion of coal using limestone as oxygen carrier precursor and sulphur sorbent

“…As a result, an increase in the mass of the sample was registered [59]. In addition, an effective oxygen transport capacity, R OC,eff , is defined considering that some sulphur is released to gas phase as SO 2 , which decrease transferable oxygen.…”

Echogenicity of liver metastases from colorectal carcinoma is an independent prognostic factor in patients treated with regional chemotherapy

“…They found that all particle size of 125–180 μm was limited by diffusion through CaSO 4 layer in the temperature range of 750–900°C and the activation energies of effective diffusivity through the CaSO 4 layer were 110–280 kJ/mol, whereas 1–5‐μm particles the sulphation was limited by chemical reaction kinetics above 850°C. Adαnez and co‐workers [49, 50] used the changing grain size model (CGSM) proposed by Georgakis et al [43] combined with the molecular scale hypotheses of Attar et al [51] to determine the kinetic parameter data for the sulfidation reaction over a broad range of particle sizes and temperatures. Good agreement between measured and predicted conversion time curves and sulfur distributions inside the particles was observed.…”

Experiment of Sulfur Removal in 1MW Poly-Generation System with Air Gasification and Combustion Combined

“…Sulfur release and removal by Ca-based sorbent in fluidized bed during coal gasification and combustion has been reported by many researches [1][2][3][4] . In recent years, more investigations emphasized sulfur transfer and distribution during coal pyrolysis or gasification.…”