Elsevier

Fuel

Volume 237, 1 February 2019, Pages 163-169
Fuel

Full Length Article
Viscosity temperature properties from molecular dynamics simulation: The role of calcium oxide, sodium oxide and ferrous oxide

https://doi.org/10.1016/j.fuel.2018.09.127Get rights and content

Abstract

  • For the long-term stable operation of the entrained flow gasifier in the coal chemical industry, the flux agents are generally adopted to adjust the fusibility of coal ash. Therefore, it is necessary to understand the underlying mechanism for the impact of typical oxide flux agents on viscosity temperature properties of coal ash from structures and thermodynamics. In this work, the role of calcium oxide, sodium oxide and ferrous oxide on viscosity temperature properties is investigated by a combination of molecular dynamics simulations and thermodynamic calculations. The variations of viscosity and temperature of critical viscosity are obtained for different ternary coal ash systems by thermodynamic calculation. Ternary phase diagrams are applied to evaluate the effect of different flux agents, which are also found to cause mineral transformation from high-temperature minerals to low-temperature minerals. Oxygen bond species are employed as the indicator of the structural evolution originating from addition of different flux agents. The sodium atoms may more readily weaken the tricluster oxygen bonds than calcium or ferrous atoms according to the results. Higher content of bridging oxygen bonds in the sodium oxide ternary coal ash system can enhance the stability of the structures and induce higher viscosity. Stability coefficients are defined here and a function to describe the relationship between the viscosity and flux agent content is established. The results from the current work are expected to provide new clues to find strategies controlling the fusion behaviour of coal ash systems.

Introduction

The viscosity temperature properties are significant for the long-term stable operation of the entrained flow gasifier [1]. Generally, the expected viscosity range is 2.5 Pa·s–25 Pa·s under the operation temperature of an entrained-flow gasifier. Viscosity higher than that range may cause blockage at the reactor bottom near the slag tapping hole, and consequently, lead to unscheduled emergency shutdown of the process [2]. When the viscosity is lower than 2.5 Pa·s, however, the problem of refractory wear may arise [3], [4]. Therefore, the adjustment of the fusibility, by addition of flux agents to the coal ash system or coal blending, to control viscosity in the appropriate range is one of the most important aspects for running the entrained flow gasifier in both theory and practice. To date, limitations in the coal blending scheme remain such as restrictions in the availability of suitable coal in the neighbouring region. Thus, the method using flux agents is most commonly adopted under the gasification condition. Accordingly, it is essential to understand the impact of flux agents at high temperatures.

Calcium oxides and ferrous oxides are major flux agents widely chosen in the entrained-flow gasifiers. Besides, there is high content of sodium oxide in the Zhundong coal, which is the largest intact coal field in the world [5]. Much research has been conducted to investigate the mechanism by which these flux agents affect viscosity [6], [7], [8]. The effect of calcium oxide on the pattern of viscosity-temperature was investigated macroscopically by varying the amount of solid minerals in the slag [6]. The role of ferrous oxides in the viscosity varies depending on the chemical valences of iron [9]. The analyses of structural characteristics of molten slags reveal sodium oxide plays a role on the viscosity-temperature behavior of coal ash slag [4], [8]. Although the general effect of fluxing agents on viscosity has been reported, the underlying fluxing mechanism for a complicated coal ash system remains unaddressed due to insufficient knowledge of the detail of structural variation in the molecular scale [10]. Moreover, it is meaningful to recognize the difference in the fluxing mechanisms among ferrous oxide, calcium oxide and sodium oxide since these flux agents may coexist in the coal ash. Therefore, it is highly important to understand the fluxing mechanism from the microscopic perspective.

In practice, the influence of flux agents on the chemical and mineral composition can be analyzed by the spectroscopies of X-ray diffraction (XRD), X-ray photoelectron, FTIR and Raman. FactSage is a software package that consists of a thermodynamic database, and various calculation and manipulation modules which enables one to perform thermodynamic calculations using the databases of pure substances and solutions [11]. The ternary phase diagram, predicted by FactSage, is frequently used to investigate the thermodynamics and mineral transformation [11], [12], [13]. Molecular dynamics (MD) simulation has been widely applied to investigate the variations of mineral compositions and structures microscopically, which helps illustrate the nature of physical properties of materials in-depth [14], [15], [16], [17]. The structural features, such as the radial distribution functions, coordination numbers, mean square distances and oxygen bond species, are commonly considered as the key to understand the mechanism of microscopic viscosity variation [16]. Li et al. uncovered the mechanism of the coke reaction at high temperatures by analyses of the structural evolution with the SiO2 content [14]. The role played by alkalis was investigated by the radial distribution function and oxygen bond species. Both Si-O and Al-O networks de-polymerize into simple structures with increasing basicity, causing increased atomic diffusion coefficients and decreased viscosities [17]. The alkalis show different influence on the total diffusivity for various ions in K2O and Na2O bearing systems, leading to distinctive trends in viscosities [15]. Furthermore, mineral transformation in the high-temperature or high-pressure process can also be understood by MD simulation. Molten anorthite was studied from first-principles calculations on the diffusion and viscosity as a function of pressure and temperature [18].

In this study, thermodynamic calculations combined with MD simulations were conducted on the comparison of the roles of calcium oxide, ferrous oxide and sodium oxide on the behavior of the coal ash, especially their influence on viscosity temperature properties. The current work aims to reveal the viscosity variation mechanism for various flux agents and quantify the corresponding dependence of viscosity temperature properties on calcium oxide, ferrous oxide and sodium oxide contents.

Section snippets

Thermodynamic calculation method

The FactSage software package [19], [20] has been used to predict the viscosity and ternary phase diagram for various coal ash systems including silicon oxide, aluminum oxide, ferrous oxide, calcium oxide and sodium oxide using the FactPS and FToxid databases in FactSage 6.4. The silicon and aluminum ratio is 2:1 and the flux agent content covered is 0.00–20.00 wt%. The temperature range is 1000 K-2000 K under 1 atm in the argon atmosphere. The thermodynamic calculations are based on the Gibbs

Effect of flux agent on the coal ash viscosity

Viscosity temperature properties, including viscosity and the temperature of critical viscosity, are important aspects for the steady operation of large-scale entrained-flow gasifiers. The viscosity variation as a function of temperature and flux agent contents calculated by FactSage is shown in Fig. 1(a)-(c). The composition mole ratio of SiO2 and Al2O3 in the model is 2.0 (the typical value for coal ash) which is also adopted in the following sections. The viscosity can be found to decrease

Conclusions

The effect of various flux agents, including ferrous oxide, calcium oxide and sodium oxide, is compared by combining the MD simulations and thermodynamic calculations. The different roles of flux agents on viscosity temperature properties of ternary coal ash systems were investigated from microscopic and macroscopic perspectives, i.e. phase diagrams accompanied with oxygen bond species analyses were constructed. The following three major points are important for further understanding of the

Acknowledgments

The authors acknowledge the financial support of the National Key Research and Development Program of China (No. 2016YFB0700100), Joint Foundation of Natural Science Foundation of China and Shanxi Province (U1510201), National Natural Science Foundation of China (Nos. 21476247 and 21761132032), Joint Foundation of Natural Science Foundation of China and Xinjiang (Grant number U1703252), Shanxi Province Science Foundation (Grant numbers 2015021055, 201601D201003, and 201703D421033), Youth

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