*Article* **Anti-Fouling Ceramic Coating for Improving the Energy Efficiency of Steel Boiler Systems**

**Minh Dat Nguyen 1,2, Jung Won Bang 1, Young Hee Kim 1, An Su Bin 1, Kyu Hong Hwang 2, Vuong-Hung Pham <sup>3</sup> and Woo-Teck Kwon 1,\***


Received: 26 July 2018; Accepted: 28 September 2018; Published: 2 October 2018

**Abstract:** Boilers are systems used mainly to generate steam in industries and waste-to-energy facilities. During operation, heat transfer loss occurs because a fouling layer with low thermal conductivity is deposited on the external surfaces of the boiler tube system, which contributes to the overall poor energy efficiency of waste-to-energy power plants. To overcome the fouling problem, a ceramic coating was developed and applied to carbon steel with a simple and inexpensive coating method. Anti-fouling testing, thermal conductivity measurement, and microstructure observation were performed to evaluate the performance of the coating. All evaluated properties of the coating were found to be excellent. The developed ceramic coating can be applied to boiler tubes in a real facility to protect them from the fouling problem and improve their energy efficiency.

**Keywords:** ceramic coating; fly ash; anti-fouling; slagging; boiler; energy efficiency

#### **1. Introduction**

Energy conservation and environmental protection are currently very important issues worldwide. Municipal solid waste (MSW), which is an inevitable product of modern society, is one of the most serious urban pollution sources and one of the greatest challenges for future generations. Deep concerns over global warming have led to numerous studies on energy efficiency and renewable energy [1]. MSW can be converted to an eco-friendly renewable resource that not only produces energy but also significantly reduces the greenhouse gas emissions from landfills. A waste-to-energy (WTE) incineration plant recovers energy from MSW and produces electricity and/or steam for heating [2]. For a WTE plant, the energy efficiency can be improved and CO2 emissions be reduced by improving the heat efficiency of the boiler system because this is the main method for heat transfer. However, one of the most serious problems in WTE facilities is that unwanted mineral matter such as slagging and fouling is always deposited on the heating surfaces of the boiler. As a general definition, fouling is the deposition and accumulation of unwanted materials such as scale, algae, suspended solids, and insoluble salts on the internal or external surfaces of processing equipment, including boilers and heat exchangers [3]. In WTE plants, ash fouling is the result of several physical and chemical processes. Ash fouling, which causes serious corrosion and erosion problems, builds up on the heat transfer surfaces of boilers to act as an insulator; this greatly reduces the global heat transfer of the boiler and minimizes the yield of the plant [4]. In one study, a typical 1–1.5 mm fouling build-up

on the boiler surface can increase fuel consumption by about 3%–8% [4,5]. In another study, a 0.03 in (0.8 mm) thick fouling layer caused a 9.5% reduction in the heat transfer, and a fouling layer thickness of 0.18 in (4.5 mm) caused a 69% reduction in an extreme case [6]. When this occurs, the boiler heat transfer surface should be cleaned. However, the operating costs from working to clean fouling is extremely high. Therefore, it is necessary to prevent the deposition and accumulation of unwanted matter on the boiler.

A small improvement in the boiler efficiency will clearly help save a large amount of fuel and to reduce CO2 emissions. In a literature review, many researchers were found to have focused on improving boiler efficiency. For example, Gopal et al. [7] studied losses in boilers. Nussbaumer et al. [8] reported a measure to save boiler energy by improving the combustion efficiency. Gao et al. [9] and Karell et al. [10] investigated the role of maintenance on boiler energy conservation. Most of these researchers did not study methods to control or prevent the formation of a fouling layer on the heating surface of a boiler. To address this shortcoming of previous approaches, an anti-fouling coating to prevent ash from attaching was developed in this study to protect boilers from fouling agents and increase their thermal conductivity efficiency.

Among the various coating systems used for boiler systems, polymer-derived ceramic coatings (PDCs), glass, and glass–ceramic coatings have the advantages of chemical inertness, high temperature stability, and superior mechanical properties compared to other materials suitable for spraying [11]. Moreover, advanced thermal spraying processes such as plasma spray and high-velocity oxy-fuel (HVOF) are also typically used to deposit coatings on the surface of boilers to enhance their high-temperature oxidation resistance but they are quite expensive because of high energy consumption [12]. Until now, however, most coating techniques just focused on improving the wear, oxidation, and corrosion resistance of the boiler surface [13–17]. Few have been used to mitigate and prevent fouling problems. In this study, an anti-fouling ceramic coating was developed for application to the external surfaces of a boiler by using a low-cost slurry spray coating method.

#### **2. Material and Methods**

The experimental procedure was performed as follows: (i) prepare the starting materials and ceramic coating materials, (ii) apply the ceramic coating materials to the steel substrates, (iii) cure and heat-treat the coated substrates, and (iv) characterize and evaluate the coatings.

#### *2.1. Starting Materials and Ceramic Coating Preparation*

JIS S45C steel is the most common material used in boiler tubes and was used in this experiment. Table 1 presents the chemical composition. Steel plates with dimensions of 10 mm × 10 mm × 2 mm were cut and then cleaned in ethanol to remove all dust and oil from their surfaces prior to coating deposition.


**Table 1.** Chemical composition of the steel substrate (wt %).

Potassium silicate (water glass with concentration of 37 wt %–a product of Young Il Chemical Co., Ltd., City, Country) was used as a binder because of its strong bond with the steel substrate. To enhance the properties of the coating slurry, several kinds of active and passive fillers with particle sizes of 2–25 μm were added to the binder. Table 2 lists some of their properties. Günthner et al. [18] selected some passive fillers (BN; Si3O4; ZrO2) to enable the processing of thick, dense, and crack-free composite coating systems. In our present study, passive fillers (Al2O3; SiO2) were used due to their good compatibility with the alkali silicate glass and low oxygen permeability to enhance high-temperature oxidation resistance of steel. By adding these fillers, it is possible not only to generate coating with high thermal conductivity than glass coating but also to reduce the volume change of glass binder

during crystallization at high temperature [18]. The dissolution of the Al2O3 and SiO2 inclusions turned the binary glass (K2O–SiO2) into a ternary glass (K2O–Al2O3–SiO2) which may improve the chemical stability of the glass [19]. Active filler (flake Al) was added to achieve crack-free coating. In the meantime, CoO and NiO was doped to improve the adhesion between the coating and substrate and reduce the porous structure of the coating [11,20]. Various parameters such as the mass fraction of the fillers, the viscosity, the dispersing methods were varied to optimize the coating system. As a result, a mixture of binder and fillers with the chemical composition listed in Table 3 was then mixed with a mixer. The mixture was ground at 400 rpm for 240 min using a ball mill such that the fillers were dispersed homogeneously in the binder. Finally, a coating slurry with solid concentration of 43 wt % was filtered and stored.


**Table 2.** Some properties of chosen binders and fillers (manufacturer's data).


**Table 3.** Chemical composition (wt %) of the slurry mixture.

The ceramic coating was sprayed on the steel plates by an air gun (W-71, Anest Iwata, Taiwan). The steel specimens were placed about 15–20 cm in front of the gun nozzle. All surfaces of the steel substrates were sequentially covered with the glass ceramic slurry by changing the surface facing the gun nozzle. To obtain a thicker glass ceramic coating, the spraying process was performed twice. Next, the specimens were cured for 2 h at 95 ◦C and finally sintered in a box furnace at 800 ◦C for 24 h. The sintered temperature was selected based on the real operating temperature of a boiler in a WTE plant.

#### *2.2. Fly Ash and Coating Characterization*

Four fly ashes from four different Korean incinerators were considered because they were very rich in alkali, chlorine, and calcium. The fly ash samples were analyzed at the Test & Standard Center of Korea Institute of Ceramic and Engineering (KICET) by scanning electron microscopy (SEM) equipped with backscattered and secondary electron detectors coupled with energy-dispersive X-ray spectroscopy (EDS) (SEM; JSM-6700F, JEOL, Tokyo, Japan), X-ray diffraction (XRD), a laser diffraction particle size analyzer (PSA) (Mastersizer S Ver. 2.15, Malvern Instruments, Malvern, UK), and inductively coupled plasma optical emission spectrometry (ICP-OES) (Perkin Elmer OPTIMA 8300, PerkinElmer, Inc., Waltham, MA, USA).

The coatings were observed with a camera (EOS 600D, Canon, Tokyo, Japan) to determine the macroscopic morphology and then further investigated by an optical microscopy. SEM-EDS and XRD were used for the microstructure characterization. To prepare cross-sectional surfaces for SEM observation, standard metallographic polishing techniques were performed; the coated specimens were cold-mounted in epoxy resin and then sequentially polished with 200, 800, 1200, and 2000 grit SiC abrasive paper.

#### *2.3. Adhesion and Thermal Shock Testings*

In the present work we used cross-cut tape test (ASTM D3359) [21] and pull-off test (ASTM D4541) [22] to obtain the adhesion between the coating and the substrate. For thermal shock testing, the coated specimen was subjected to 800 ◦C in a furnace for 5 min and subsequently removed using a pair of pliers and placed in a water tank (20 ◦C) for 5 min. The process was repeated and the total number of thermal cycles was determined up to the time when macroscopic cracks or failure appeared.

#### *2.4. Anti-Fouling Testing*

The anti-fouling performance of the developed coating against fly ash was studied. To study the anti-fouling ability of the coating, the slurry containing ash was used to observe the ash attachment on the coating surface. To do this, coated and non-coated steel plates were immersed in the fly ash solution and then dried at 50 ◦C for 1 h. After 24 h of sintering in the box furnace at 800 ◦C for 24 h, the specimens were cooled to room temperature (20–25 ◦C). A compressed air gun (0.5 MPa) was then used to blow the fly ash powder-deposited surface of each specimen for 1 min. The air gun nozzle was placed 20 cm away from the specimens. Subsequently, the air-blown specimens were examined with SEM-EDS. Figure 1 shows the entire experimental process. In addition, the prepared composite coatings were applied to a real-life boiler system to assess their effectiveness.

**Figure 1.** Anti-fouling resistance testing procedure.

#### *2.5. Thermal Conductivity Measurement*

To evaluate the energy efficiency, four different specimens were prepared comprising: (i) steel with ceramic coating; (ii) steel without ceramic coating; (iii) ceramic coating materials and (iv) corrosion specimen. Here, specimens (i) and (ii) were then subjected to anti-fouling testing. Specimen (iii) was a bulk material made from the mixture of slurry coating. Specimen (iv) was separated from the ash deposits attached to the boiler systems at JINJU INDUSTRY power plant. All the specimens were made in size of 10 mm × 10 mm × 1.2 mm and their thermal conductivity were measured with the laser-flash method (Netzsch LFA 427, Netzsch, Wittelsbacherstraβe, Germany). To assess the thermal conductivity <sup>λ</sup> (W/m·K) of a specimen, the thermal diffusivity *<sup>a</sup>* (mm2/s), density <sup>ρ</sup> (g/cm3), and specific heat *C*<sup>p</sup> (J/g·K) of the specimen must be known. The thermal diffusivity was measured with the heating rate 5 K/min. The data was recorded after each 100 ◦C from 25 to 800 ◦C. The specific heat *C*<sup>p</sup> of the specimen was estimated by simple rule of mixture of the fillers and the coating matrix. The density of the specimen was determined using Archimedes principle.

$$
\lambda(T) = \mathbb{C}\_{\mathbb{P}}(T) \times a(T) \times \mathbb{p}(T) \tag{1}
$$

#### **3. Results and Discussion**

#### *3.1. Properties of Fly Ashes*

To date, various studies have investigated the ash deposition characteristics from different perspectives to clarify the influences of individual factors, including the chemical/mineral compositions of the ashes. Wibberley et al. [23] concluded that fine particles (<10 μm) with a high content of alkali vapors, including sodium and potassium, are the main reason for the inner layer formed in the initial stage of ash deposition. Lee et al. [24] stated that high concentrations of chlorine and sulfur in MSW affect the rate of corrosion in WTE boilers. Furthermore, accumulated ash with a high chlorine concentration on tube surfaces may lead to corrosion underneath the deposit [25,26].

The composition of MSW varies because of differences in lifestyle, so the ash content also varies. Generally, the chemical compositions of the fly ashes showed that SiO2, Al2O3, Fe2O3, CaO, and Na2O were the main oxides (Table 4). Lead and copper were the most common heavy metals in the ashes (Table 5). Based on previous studies, fly ash 1 (Tables 4 and 5), which has high sodium and chlorine contents, was selected as the fouling matter. The physical and chemical properties of fly ash 1 were examined in more detail. The mean size of fly ash 1 was 25 μm (Figure 2). The elemental concentrations of fly ash 1 as determined by SEM-EDS (Figure 3) were consistent with the results from ICP-OES (Tables 4 and 5).

**Table 4.** Oxide compositions in fly ashes 1–4 (wt %).


**Table 5.** Heavy metals in fly ashes 1–4 (mg/kg).

**Figure 2.** Particle size distribution of fly ash 1.

**Figure 3.** EDS mapping of fly ash 1.

#### *3.2. Microstructure and Morphology of Ceramic Coating*

The XRD patterns of the composite coating on steel substrate are shown in Figure 4. SiO2, Al2O3, and abite Na(Si3Al)O8 peaks were detected. Abite may be the new phases formed during thermal treatment. Because the softening point of glass (640–680 ◦C) is lower than its heat treatment temperature (800 ◦C), the glass would soften, flow, and spread well on the steel surface. The fillers may be partially dissolved into the glass matrix and it is not surprising that the reactions between glass and fillers may be occurred during thermal treatment.

**Figure 4.** XRD patterns of the composite coating after thermal treatment at 800 ◦C.

Generally, the coating should have a relatively low surface energy and a dense structure to significantly reduce the sticking of molten ash particles to the surfaces. Moreover, it should have an appropriate thickness and have no chemical affinity with the fouling matter. Finally, it must have good adhesion with the boiler. Figure 5 shows the cross-section morphology of the heat-treated ceramic coating with a thickness of 150–160 μm. A layer enriched with silicon and aluminum in the cross-section was observed. Additionally, the coating was intact and only a few closed pores with spherical shape were seen. These certain pores can help alleviate thermal stress and thermal expansion mismatch between the coating and substrate. No cracks in the coating or interlayer at the coating–steel interface were observed, which suggests that the coating has a thermal expansion coefficient (CTE) similar to that of the steel and had a strong chemical bond with the steel [26,27]. The adhesion between the coating and steel was measured in detail as follows.

**Figure 5.** Morphology and EDS maps for the cross-section of the ceramic coating.
