- carbonation (1) (remove)
- Mineral sequestration of CO2 by reaction with alkaline residues (2012)
- With the onset of industrialization within the last 150 years, a significant increase in the concentration of the greenhouse gas carbon dioxide (CO2) is recorded in the atmosphere. According to current scientific understanding the rising atmospheric CO2 levels can be linked with high probability to the observed phenomenon of global warming. Consequently, the reduction of anthropogenic greenhouse gas emissions has become a global challenge of environmental research and policy. In this thesis, a novel approach to achieve a long-term mineral sequestration of CO2 was studied, using alkaline residue materials. This study examined for the first time a process that allows for rapid removal of CO2 from flue gas through reaction with lignite fly ashes in aqueous solution. In this process the basicity of the residues is utilized for mineral trapping of CO2 by precipitating stable calcite. Lignite fly ashes are a cheap, inexpensive, highly reactive byproduct of coal combustion. Due to the exposure to heat, these waste streams generally contain high amounts of reactive Ca/Mg (hydr)oxides and thus offer a high alkalinity. The alkaline residues were therefore not considered as an environmental problem, but rather as useful reactants for technical CO2 neutralization in the context of combustion processes. Carbonates are end-products of weathering processes at the earth surface and mineral carbonation is thus assessed to be a permanent and safe storage option of CO2. Compared to alternative forms of carbon storage (e.g. the injection into gas reservoirs) cost-intensive monitoring programs for safety reasons can be omitted. Also, the carbonation generally leads to heavy metal fixation in the residues, allowing for an environmentally less problematic disposal of the products or even their industrial re-use (e.g. road construction, cement industry). Due to the common high reactivity of alkaline fly ashes no pre-treatment (e.g. grinding, using chemical additives) is needed compared to the use of natural silicate minerals as feedstock material. For these reasons mineral carbonation of alkaline residues can be considered as a process with low costs and low energy consumption, thus making it an interesting CO2 reduction pathway from an economical point of view. In Chapter 1, the mechanisms and rates of reactions between alkaline lignite fly ash and CO2 in aqueous suspensions were evaluated. Aqueous laboratory experiments showed that CO2 from flue gas can be bound directly as carbonate. Additionally, solutions with high dissolved inorganic carbon content are formed, which can be injected into aquifers for mineral CO2 sequestration. As the dissolution rates of the alkaline mineral phases are high, gas phase CO2 transfer into the aqueous phase is mostly the limiting factor for the overall carbonation process. CO2 dissolution is controlled by the solution pH, by the available surface area of the gas/water interface and by the gradient at that interface. The maximum conversion of 5.2 moles of CO2 per kg fly ash (≈ 0.23 kg kg-1) obtained at 75 °C demonstrates the high potential of alkaline fly ashes to sequester CO2. This value accounts for a CO2 sequestration capacity of nearly 3.5 million t of CO2 in Germany alone based on the available lignite fly ash, which corresponds to 2 percents of the CO2 emissions from lignite power combustion (168 million t a-1 in 2009). In Chapter 2, laboratory carbonation experiments are described, which were carried out with the individual mineral phases CaO and MgO in aqueous solution. The process showed parallels with the reactions observed during carbonation of lignite fly ashes, suggesting that Ca and Mg (hydr)oxides can be used as proxies to estimate alkaline waste reaction with CO2 in general. The carbonation of CaO happens fast, occurs at high pH values > 12 and is controlled at the mineral surface by the dissolution of Ca(OH)2. As long as Ca(OH)2 is available CO2 uptake by the system is high and leads to the simultaneous precipitation of calcite (CaCO3). Under similar conditions MgO carbonation is a slower and much more complex process. In the presence of MgO an initial pH of ~ 10.8, indicating solubility equilibrium, was reached. Subsequently, TDIC concentrations and EC increased almost linearly. The pool of MgO based alkalinity can be made available for mineral trapping if the kinetic restrictions for precipitation of Mg-carbonate can be overcome, e. g. by running the processes at higher temperature (> 50 °C) and higher s/l-ratio. Corresponding to related work the precipitation of hydromagnesite (Mg5(CO3)4 (OH)2 ∙ 4H2O) is found for temperatures above 50 ° C already at a suspended amount of 4 g L-1. Precipitation of nesquehonite (MgCO3 ∙ 3H2O)) starts upon a suspended amount of MgO of more than 10 g L-1 at 25 ° C. In Chapter 3 the setup and the results of a model are shown, which was used to simulate and evaluate the process of alkaline material carbonation over time. Experimentally derived specific dissolution rates for CaO/MgO and CO2 are used for the development of a kinetic geochemical model based on the freely available PHREEQC algorithm. The software offers the access to databases, which containing thermodynamic constants of all common dissolved species in natural and industrial processes. Experimental assays conducted in an aqueous carbonation reactor (see Chapter 1 and 2) were used as reference to test the model and evaluate its robustness and sensitivity. The reaction course of the experiments based on the use of the pure phases (CaO and MgO) was successfully reproduced by our simulations. The developed model may thus be used as a valuable tool for the optimization of technical scenarios/facilities for CO2 sequestration. In order to study different mineral sequestration scenarios for calcite precipitation, we used the simulation to test the variation of process parameters and the addition of chemical additives (CaCl2, CaSO4). Finally, the simulation of the carbonation of lignite fly ash was tested using our simplified model based on CaO, MgO, calcite, anhydrite as kinetic reactants. It was shown that advanced techniques to determine the exact mineralogy of combustion residues and the extension of the availability of thermodynamic data of specific mineral phases are necessary to improve geochemical modelling in future work. In Chapter 4, the potential contribution of lignite fly ash to mineral CO2 trapping in a high anhydrite (CaSO4) containing aquifer were analyzed. The study examined the possibility of combining underground CO2 storage and geothermal heat/energy production from an anhydrite rich aquifer. In such a scenario Ca2+ for the precipitation of calcite could be provided from the dissolution of the calcium sulfate. The dissolution of anhydrite concurrently releases acid, being counterproductive with respect to the formation of carbonates. The possibility of pH buffering by the addition of alkaline lignite fly ash is therefore appraised to optimize the conditions of carbonate precipitation. The performed laboratory experiments, as basis for thermodynamic simulations with PHREEC, confirmed that the buffering capacity derived from the fly ashes is essential for calcite precipitation in such a system. Already with an addition of 0.1 weight percent of fly ash per volume of the injection solution the amount of precipitated calcite was maximized. The dissolution of anhydrite is associated with a concurrent increase in pore space and can balance the porespace reduction by precipitation of carbonates and secondary silicates in the geothermal reservoir.