Abstract
Fly ash generation in fluidized bed combustion (FBC) is a critical issue in many countries due to its disposal is becoming increasingly restricted and expensive. Because of this, there is a demand for applications in which these types of fly ashes could be utilized efficiently. One promising use for FBC fly ashes is as a cement replacement material in mortar and concrete. The current concrete regulations do not allow the use FBC fly ash as a supplementary cementitious material, but it can be expected to be included in the standards in the future. The properties of FBC fly ashes typically do not fulfill the values set in the standards as such. This study aimed to establish whether the properties of fly ashes from FBC of peat, wood, and wastes can be modified by mechanical classification and grinding so that they meet the requirements of the standards. The sulfate and chloride content, the sum of the main components (Si, Al, Fe), and the fineness of material were analyzed before and after the classification and grinding processes. In addition, the mortar specimens were prepared by using the processed fly ash as a cement replacement material. It was found that air jet classification is an effective fractionating method for fly ashes that effectively removes sulfate and chloride into fine fraction. Classified and ground fly ashes are potential alternative cement replacement materials. It is possible to achieve 80% of the control sample’s compressive strength and 90% of the control sample’s flexural strength for mortars containing 20% of classified and ground FBC fly ashes.
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Statement of Novelty
This study aimed to establish whether the utilization potential of fly ashes from FBC of peat, wood, and wastes can be improved in concrete by mechanical classification and grinding, which is not done earlier. We found that it is possible to modify these fly ashes to fulfill concrete standards. Usually it is thought that fly ashes from fluidized bed combustion are not suitable for standardized concrete, but this study shows that with treatments it is possible.
Introduction
Biomass is a sustainable energy source used to produce electricity and heat, and its use will continue to increase. The use of renewable energy is encouraged by the political goals of the European Union (EU), such as the “2030 climate and energy framework” that has set a target to increase the share of renewable energy sources to cover at least 27% of EU energy consumption by 2030 [1]. Biomass can be co-fired with peat and different wastes, such as recycling waste, which contains different packing materials, or side-streams from the food and paper industries. Among the available combustion methods, fluidized bed combustion (FBC) is efficient and common due to its ability to utilize low-grade fuels with fluctuating quality, composition, and moisture content, or mixtures of fuels, in situ capture of SOx, and low NOx emission [2]. However, the fly ash originating from FBC has thus far had limited utilization potential even though millions of tons of this type of fly ash are generated annually in Europe alone and this amount is expected to increase. Fly ash generation is a critical issue in many countries, especially when considering that disposal is becoming increasingly restricted and expensive, contributing to a demand for applications in which fly ashes could be utilized efficiently.
One interesting category of use for FBC fly ashes is as a cement replacement material or an aggregate in concrete. In addition to prevent disposal, using fly ash as a cement replacement material means a significant reduction in CO2 emissions related to industrial cement production from traditional raw materials (limestone and clay), and the preservation of natural resources can also be achieved. There are many promising studies that have investigated the use of FBC fly ash as a cement replacement material [3,4,5,6,7,8,9,10,11,12,13]. However, the use of FBC or biomass fly ashes as a partial cement replacement material is not allowed by the American standard ASTM 618 [14] or the European standard EN 450-1 [15], which are the standards governing the use of fly ashes as mineral admixtures in concrete. EN 450-1 applies to ashes originating from pulverized combustion where the coal content must be over 60%, or over 50% when coal combustion takes place with pure wood. However, it is reasonable to expect that in the future, extension of the current regulations surrounding the use of fly ash in concrete should be limited to those fly ashes meeting the physical and chemical requirements (see Table 1) as specified in the ASTM C 618 or EN 450-1 standards. Therefore, these limit values can be used now to provide a guideline for fly ash utilization in concrete.
The European standard EN 450-1 sets several required chemical and physical properties for fly ash to be used in concrete. When concerning biomass fly ash, the most critical properties are sulfate and chloride content and the sum of the main components, namely SiO2, Al2O3, and Fe2O3. According to that standard, chloride content must be < 0.1%, sulfate < 3%, and the sum of the main components over 70%. Peat fly ash fulfilled the requirements of these standards without any treatment [16], but in contrast, biomass and waste fly ash often require some sort of treatment to ensure that they adhere to the limits set by the governing standards [17,18,19,20,21,22]. To comply with the limit values set by the standards, water-washing treatment for biomass fly ashes has been carried out [17, 18]. However, this procedure requires water and energy for drying. Therefore, mechanical classification is one interesting option to improve fly ash chemical composition without the use of water, as there is a relationship between fly ash particle size and heavy metal, Cl− and SO42 content [23,24,25,26,27,28,29,30,31]. It has been found that the utilization potential of fly ash from biomass and waste combustion can be significantly improved with mechanical classification [30]. However, the particle size distribution of classified coarse fraction and its behavior as a cement replacement material is not studied. Therefore, this study aimed to establish whether the properties of fly ashes from FBC of peat, wood, and wastes can be modified by mechanical classification and grinding so that they meet the requirements of the standards. Fly ash composition after classification and grinding was compared to limit values set by the European EN 450-1 standard. The effect of sulfate and chloride content, the sum of the main components, and fly ash fineness for mortar properties were investigated.
Materials and Methods
Fly Ashes
Fly ashes from three different Finnish power plants utilizing bubbling fluidized bed boilers were studied. The power plants used different mixtures of fuels; therefore, the fly ash samples differed in their properties. Fuel composition of the first fly ash sample (FA1) was 70% forest residues and 30% peat; the second fly ash sample (FA2) was 60% forest residues, 30% recycling waste, and 10% sludge from the papermaking industry; the third fly ash sample (FA3) was 40% peat, 50% forest residues, and 10% recycled wood waste. Forest industry residues contains felling waste, like branch, bark and leaf. Recycling waste contains packing material waste, such as plastic (not PVC), carton, paper, and wood collected from industrial and retail outlets. Recycled wood waste is collected from industrial and retail outlets. Sludge from the papermaking industry contains cellulose fibers, pigments and fillers from papermaking process. Fly ash samples were collected from the first electrostatic precipitator unit in 10 L buckets.
Materials for Mortars
The cement used in this study was Portland cement type CEM I 52.5 R-SR5 from Finnsementti (Finland). Sand used as an aggregate material was sieved natural silicon sand from Fescon (Finland). A particle size distribution of the sand is the following: d10 = 440 µm, d25 = 630 µm, d50 = 880 µm, d75 = 1200 µm and d90 = 1940 µm measured by laser diffraction technique. A polycarboxylate-based superplasticizer agent (Sem®Flow ELE 20, Semtu) was used to adjust the consistency of mortar mixtures.
Methods
Analysis of Fly Ashes
The particle size distribution of the fly ash samples reported as a volumetric median size (d50) was measured with the laser diffraction technique (Beckman Coulter LS 13320) using the Fraunhofer model and the wet procedure using water. A specific surface area measurement was based on the physical adsorption of gas molecules on a solid surface using Micrometrics ASAP 2020, and the results were reported as a BET isotherm. The main chemical components of fly ash were determined using an Omnian Pananalytics Axiosmax 4 kV X-ray fluorescence (XRF) from a melt-fused tablet. The melt-fused tablet was produced from 1.5 g of fly ash melted at 1150 °C with 7.5 g of X-ray Flux Type 66:34 (66% LiB4O7 and 34% LiBO2). Field-emission scanning electron microscopy (FESEM, Zeiss Ultra Plus) was used to visualize the fly ash samples. The FESEM sample was prepared by adding a thin layer of fly ash on the coal sticker. The samples were sputter-coated with platinum, and a 10 kV voltage was used when imaging the samples.
Classification
The air jet classification method (Multiprocessing System, Hosokawa Alpine, Augsburg, Germany) was used to fractionate fly ash samples into fine and coarse fractions, as presented in [30]. Classification rotor speed of 2000 rpm and air flow of 75 m3/h was used, and fine material shares from 15 to 30% were achieved depending on the fly ash. The achieved coarse and fine fractions were collected for weighing and elemental analysis. The classified coarse fly ash fractions are further abbreviated as FA1_C, FA2_C, and FA3_C.
Grinding
Half of the classified coarse fly ash fractions (FA1_C, FA2_C, and FA3_C) were ground by an impact mill with one rotating and one stationary pin disc (Laboratory Fine Impact Mill 100 UPZ-II, Hosokawa Alpine, Augsburg, Germany). The pin mill was operated with the rotational speed of 22,000 rpm, corresponding to a tip speed of 160 m/s. After grinding, three new samples for mortar tests were achieved: FA1_CG, FA2_CG, and FA3_CG.
Mortar Preparation
The control sample was prepared using cement, tap water, and sand. Original fly ashes, coarse fractions of fly ashes from classification before (FA1_C, FA2_C, and FA3_C) and after grinding (FA1_CG, FA2_CG, and FA3_CG) were used to replace 20% of the cement in the mortar samples. Preparation of mortar samples was done according to cement standard EN 196-1 [32] with slight modifications. Modifications included the flow table test done before molding the samples. Additionally, adjustments were made to mortar consistency using a superplasticizer in the samples. Consistencies of fresh mortar mixtures were evaluated using a flow table test described in a mortar testing standard [33]. The consistency was evaluated to ensure the proper rheology of the mortar mixtures (i.e., spread values 17 mm ± 2 mm), and to determine whether a superplasticizer is necessary to use. The designs of the mortar mixtures are presented in Table 2. All mortar specimens fabricated were cured in water at room temperature (20 °C) for 28 days prior to being tested.
Mortar Strength Measurements
Flexural strength was measured from 40 × 40 × 160-mm mortar prisms, and broken halves were used for unconfined compressive strength measurements. The strengths of the samples were measured after 28 days of curing using a Zwick testing machine with a maximum load of 100 kN employing a loading force of 2.4 kN/s. The reported strength of mortar is the average of the replica specimens tested: three replicas for flexural strength and six replicas for compressive strength were measured.
Results and Discussion
Fly ash Properties
The chemical compositions of the original fly ashes were mainly CaO and SiO2, but the fly ashes also contained high percentages of Al2O3 and Fe2O3 (Table 3). All fly ashes contained small percentages of Na2O, K2O, and P2O5, except for FA3, which contained as much as 6.5% of K2O. FA2 and FA3 had a high sulfate content of over 6%. FA1 and FA2 had similar particle size: the median particle size was 45.0 µm for FA1 and 46.5 µm for FA2. FA3 was much smaller, having a median particle size of 22.1 µm. The BET surface area varied substantially between fly ashes, from 1.0 to 4.5 m2/g. When comparing the chemical composition of fly ashes to SFS-EN 450-1 limit values (see Table 1), it can be noted that the sulfate and chloride content of FA1 are at an acceptable level, but levels are remarkably high for FA2 and FA3. P2O5 and MgO contents are below the limits for all fly ashes. The sum of SiO2, Al2O3, and Fe2O3 is below the limit (70%) for all studied fly ashes: 68% for FA1, 56.4% for FA2, and 53.8% for FA3. A FESEM images of original fly ash samples are presented in Fig. 1. Fly ash particles have mainly an irregular shape, but the particle shape changes from spherical to fibrous. Differences between ash samples can not be seen reliably from FESEM images.
Classification of the Fly Ashes
Through air jet classification, the FBC fly ash utilization potential for concrete use can be increased significantly. Air jet classification is an efficient separation process that separates components into fine and coarse fractions so that hazardous components tend to concentrate to a fine fraction [30]. According to mass balance, when some elements concentrate to a fine fraction, other elements must concentrate to a coarse fraction. The work of [30] showed that when FBC fly ashes are classified with air jet classification, CaO is concentrated to a fine fraction, whereas SiO2 and Al2O3 are concentrated to a coarse fraction. Both sulfate and chloride have been found to concentrate to a fine fraction with high selectivity, which means that if mass share for fine fraction is 20%, up to 70% of the total sulfate and chloride content can concentrate to a fine fraction [30]. The removed fine material share depended on the original fly ash properties, i.e., particle size and shape: with the used classification parameters (rotor speed of 2000 rpm and air flow of 75 m3/h), fine fraction removal was 15% from FA1, 31% from FA2, and 22% from FA3.
According to SFS-EN 450-1, for fly ash to be used in concrete, the sum of the contents of SiO2, Al2O3, and Fe2O3 shall not be < 70% by mass. Therefore, the concentration of SiO2, Al2O3, and Fe2O3 to coarse fraction and CaO to fine fraction is an advantage when considering concrete applications for fly ash. For the fly ash samples studied here, the sum of SiO2, Al2O3, and Fe2O3 increased with air jet classification (Fig. 2). The sum increased from 68 to 71% for FA1, from 56 to 69% for FA2, and from 54 to 68% for FA3.
The sulfate content of fly ashes (Fig. 3a) can be decreased significantly and clearly to an acceptable level by removing 30% as fine fraction from FA2 and 22% from FA3. However, for FA1, it can be noted that air jet classification was not necessary according to the sulfate content. As with SO3, chloride content (Fig. 3b) for FA1 was also at an acceptable level originally, making classification unnecessary. Instead, for FA2 and FA3, chloride content could be decreased significantly to a nearly acceptable level by removing 30% as fine fraction from FA2 and 22% from FA3.
Grinding of the Fly Ashes
Typically, fly ashes are quite fine-grained and easy to grind [34]. However, when fly ash is classified and coarse fraction is taken for further processing, grinding becomes more important. FA1 and FA2 had median particle sizes of approximately 45 µm and FA3’s median particle size was approximately 22 µm. After air jet classification, the particle sizes of coarse fly ash fractions were around 200 µm, but this could be further reduced by grinding to around 30 µm for all fly ashes.
After grinding, all classified fly ashes (FA1_CG, FA2_CG, and FA3_CG) fulfilled the Class N fineness requirement (Fig. 4). Particle sizes of fly ashes are presented in Fig. 4 as a cumulative > 45 µm because standard EN 450-1 uses this value as a fineness measurement. According to EN 450-1, Category N means that the fineness shall not exceed 40% by mass, and category S means that the fineness shall not exceed 12% by mass. Original and classified FA1 and FA2 did not meet Class N or S requirements. However, FA3 originally fulfilled the standard. The particle size distributions of all fly ash samples was measured using laser diffraction method (see Fig. 5a–c). As can be seen classification increased the particle size distribution for all ashes, but grinding reduced the distribution to finer size compared to original. Exception to this is FA3 which classified fraction is coarser and it most probably explains the need for superplasticizer (Table 2).
Mortar Experiments
Mortars containing 20 mass-% of fly ashes did not achieve the same flexural strength as the control, but it can be seen that grinding improved the strength to close to the control’s level for all studied fly ashes (Fig. 6). Flexural strength for the control sample (100% OPC) after 28 days was 6.7 MPa. When only classified coarse fraction was used as a cement replacement material, around a 20% loss in flexural strength was incurred. This means that coarse fly ash particles are not reactive and are only working as a filler material. Instead, when using classified and ground FA1 and FA3 as cement replacement materials, only a 10% decrease in strength was observed. Mortar containing FA2 did not attain strength as high as FA1 or FA3 in any case.
Mortars containing 20 mass-% of fly ashes did not achieve the same compressive strength as the control, but it can be seen that grinding improved the strength to close to the required 75% of the control strength for FA1 and FA3 (Fig. 7). Standard EN 450-1 sets the limit for the activity index to be 75% of the control sample for mortars containing cement replacement material. Therefore, the dashed line in Fig. 7 indicates 75% strength compared to the control sample. The control sample (100% of OPC) had a compressive strength of 50 MPa. Mortar containing the FA2 sample did not attain strength as high as FA1 or FA3. When only classified coarse fraction of FA1 and FA2 was used as a cement replacement material, around a 40% loss in compressive strength was incurred. Mortar containing 20% of FA3 had higher strength of around 75% of the control, and that value did not increase significantly when ground FA3 was used. It can be seen that grinding of coarse fraction is valuable for FA1: an over 20% increase in mortar compressive strength was possible to achieve.
When comparing these results to earlier published work [9, 16, 29, 35], it can be seen that the achieved activity indexes are lower for classified fly ashes (Fig. 7) than for original fly ashes. The reason for this is probably the lower reactivity of classified ashes: calcium and sulfur are important components for FBC fly ash reactivity [16, 35], and in this present work, many of those components were removed from the fraction used to replace cement. Because of this, aiming to fulfill concrete standards is questionable for FBC fly ash if significant strength loss is not wanted. Therefore, long-term durability tests for mortar and concrete containing un-fractioned FBC fly ashes are needed in the future.
Conclusions
The utilization potential of fly ashes from FBC of peat, wood, and wastes in concrete can be increased significantly through air jet classification and grinding. Air jet classification effectively removes sulfate and chloride into fine fraction. The coarse fraction contains mostly the desired chemical components (SiO2, Al2O3 and Fe2O3), but it is too coarse to be utilized as it is. Desired particle size distribution is achieved by tumbling ball milling. Classified and ground fly ashes are potential alternative cement replacement materials because they fulfill the requirements of the EN 450-1 concrete standard for chemical composition, particle fineness and activity index of mortar. It is possible to achieve 80% of the control sample’s compressive strength and 90% of the control sample’s flexural strength for mortars containing 20% of classified and ground FBC fly ashes. Therefore, these type of fly ashes can be utilized in construction industry instead of landfilling and at the same time, CO2 emissions of cement industry can be reduced.
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Acknowledgements
Open access funding provided by University of Oulu including Oulu University Hospital. This study was supported by the Finnish Funding Agency for Technology and Innovation and the following Finnish companies: Boliden Harjavalta Oy, Ekokem Palvelu Oy, Fortum Power and Heat Oy, Helen Oy, Jyväskylän Energia Oy, Kemira Chemicals Oy, Metsä Board Oyj, Napapiirin Energia ja Vesi Oy, Nordkalk Oy Ab, Paroc Group Oy, SSAB Europe Oy, Stora Enso Oyj, UPM-Kymmene Oyj, and Valmet Technologies Oy. We would like to thank Mr. Jarno Karvonen, Mr. Jani Österlund, and Ms. Maria Tomperi for their contributions to the laboratory work.
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Ohenoja, K., Wigren, V., Österbacka, J. et al. Mechanically Treated Fly Ash from Fluidized Bed Combustion of Peat, Wood, and Wastes in Concrete. Waste Biomass Valor 11, 3071–3079 (2020). https://doi.org/10.1007/s12649-019-00615-y
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DOI: https://doi.org/10.1007/s12649-019-00615-y