The experimental setup for this study was shown in Figure 1. It consisted of a detection system, test duct section, DC power supply system, and an ESP equipped with fabrics collectors. An aerosol feeding device (SAG-410) aerosolized the test particles from storage tank at a predetermined rate. The air entering the device at a negative pressure was deduced by an induced draft. The distance between two collectors was 400 mm, the ESP cross- sectional area was 0.32 m², and the length of the collectors was 4 m. A patented integrated system with water distribution and tension functions for polypropylene fibrous collectors (Patent No.: CN200910019222.7) was installed in the ESP. Gases flowed from right to left via deflectors which was guided by numerical simulation results, respectively. The gas residence time was 1.1 ~ 3.33 s. A DC voltage controller was used, and the applied voltage was in the range of 25 ~ 70 kV, thus the electric field strength was 0.275 ~ 0.35 kV/cm. The temperature was in the range of 325 ~ 330 K (measured by type K thermocouples), respectively. The high-voltage electrodes were barbed wires which could produce more gaseous ions at high negative potential.

The industrial smoke dust was screened to obtain test particles by electromagnetic high frequency vibrating screen. A real-time detection system (ELPI) was used to measure the variety of the number concentration under several conditions. Figure 2 shows the size distribution of fine particles, the predetermined mass concentrations were controlled by frequency modulator of SAG which was earlier calibrated by dust meter (3012 H). They are charged particles from 0.05 to <2.5 µm in size. Electrical effects can predominate as transport and deposition mechanism for particles < 1 µm in size. The greater the charge they possess the higher deposition.

The overall current density curve of polypropylene fibrous collector was carried out to obtain electric behavior using negative high-voltage DC power as shown in Figure 3. The current density increased sharply when the applied voltage increased from 10 kV to 60 kV until the blue filaments or spark-over were visible. These measurements were carried out with various secondary voltages. A nameplate indicating primary voltage, primary current, secondary voltage, secondary current, power consumption, etc. were located on the front of the low vol-

tage panel. The maximum working voltage was ensured under above-mentioned conditions. Figure 3 shows a similar tendency of discharge current density for flexible collector and rigid steel collector. The current density by flexible collector was 20 ~ 100 percent higher than that by rigid collector as illustrated in Table 1. Higher stronger electric field resulted in higher discharge current. Even though the initial collectors are insulated before water penetrating them via capillary flow, it could be demonstrated that flexible collector wetted was consistent with the behavior of conventional rigid steel collector in electric field. The current density by flexible collectors were increased which would help to precipitate PM2.5 more easily than conventional steel materials.

The concentration of particles entering the ESP, C_in, and the concentration of particles leaving the ESP, C_out, were monitored by Electrical Low Pressure Impactor (ELPI). Thus, the collection efficiency could be derived as:

where η is the collection efficiency, C_in is the initial number concentration of fine particles, and C_out is the final number concentration at the outlet of the improved wet ESP.

As illustrated in Figure 2, the number concentration at the outlet was strongly influenced by both gas velocity and applied voltage. The higher applied voltage or lower gas velocity, the lower concentration at the outlet would be. Figure 2 shows initial number concentration with zero voltage at setting feeding frequency via experimental duration. Its final number concentration depends on the secondary voltage and its initial values. After particles injected into the device by SAG, the number concentration decreased rapidly after about 1 s. As illustrated in Figure 4, the number distribution of submicron particles decreased rapidly. The results show that the

overall efficiency curves had similar curvilinear trend under various working conditions. As illustrated in Figure 5, there was not obvious link between initial concentration and collection efficiencies, the efficiencies at higher inlet concentration or lower concentration by flexible collectors were almost the same. The average number collection efficiencies by flexible collector amounted to 88.3% for PM2.5 when the gas residence time was 4 s at 60 kV as shown in Figure 6. It could be conclude that flexible collectors allowed the current to be higher, and the collection efficiencies, especially for fine particles, were also higher. An increase in applied voltage was presumably caused higher charge for PM2.5 particles, thus would be beneficial to offer better collection efficiency. It can be concluded that the number efficiency was higher with higher applied voltage than that with lower applied voltage for particles in the same gas treatment time. The higher performance of flexible collectors indicated that they could be popularized to applications, thus would be propitious to solve cool-end corrosion and extra water consumptions problems.

The effects of water film on particle agglomeration in gas were investigated. Agglomeration is a process in which smaller particles adhere to a larger one, or in which smaller particles come together to form a larger one. As shown in Figure 7, the effect of water film evaporation on decreasing the number concentration was of great

significance to particles agglomeration. Meanwhile, the number concentration of fine particles (<0.5 µm) declined substantially, and all repeated test indicated that there was significant effect on the particle agglomeration for wet collectors in gas. Furthermore, the maximum water evaporation addition rate was 25 L/(h∙m²) when the gas velocity was 3 m/s, respectively. It could be calculated that the decrease of the number concentration was not less than 40% for ultrafine particles (<0.5 µm) depend on the water film adsorption. In other words, the effect of water film adsorption on the temperature drop was more sensible. Meanwhile, it could be observed that as long as there was any water on the surface, any particle would exhibit similar agglomeration, whether at higher or smaller water addition rate. It could be concluded that the flexible collectors could maintain uniform wetting property and excellent adsorption via capillary penetration consuming smaller water, thus would allow lower water consumption in the applications.