3.1. Flow Field and Aerodynamic Analysis
The aerodynamic performance and cooling characteristics of endwalls are affected by the secondary flow structures and the interactions between the purge flow and mainstream flow.
Figure 7 clearly elucidates the static pressure coefficient at the root of the vane. The results point out that the NEC can significantly alter the static pressure at the root of the vane near the suction side but has almost no impact near the pressure side and that the half-cycle circumferential function can greatly reduce the circumferential pressure gradient.
When 0.1 < Z/Cax < 0.7, both Case 1 and Case 2 decelerate and boost the secondary flows due to the valley near the suction side, and the circumferential pressure difference decreases. During the range of 0 < Z/Cax < 0.65, for Case 3, because of the valley on the side of the suction side, the secondary flows slow down and increase the static pressure. As for Case 4, during the range of 0 < Z/Cax < 0.1, the lateral differential pressure is reduced, and at the position of 0.1 < Z/Cax < 1.0, the overall transverse pressure difference is increased on account of the hump.
On the other hand, it is vital to clarify the impact of different NECs on the passage vortex.
Figure 8 depicts the axial vortex distribution of various NECs at the four position sections: the leading edge, 0.1 C
ax, 0.4 C
ax, and 0.7 C
ax.
The consequences portray how the NECs could hinder the development of the horseshoe vortex. In the section of the leading edge, there is no noticeable difference in the horseshoe vortex. At the 0.4 Cax and 0.7 Cax cross-sections, Cases 1, 2, and 4 show the attenuation of the passage vortex loss core. Among them, Cases 1 and 2 inhibit the development of the passage vortex because of half-cycle contouring, which extremely reduces the circumferential pressure gradient, and Case 4 forms a hump between the suction-side and the pressure-side legs of the horseshoe vortex, destroying the evolution of the pressure-side leg of the horseshoe vortex, limiting it in the valley, and then weakening the strength of the passage vortex. Case 3 creates a hump between the pressure-side leg of the horseshoe vortex and the pressure side, forcing the pressure-side leg of the horseshoe vortex to approach the suction side. It is worth mentioning that compared to Case 1, Case 2 dilutes the suction-side leg of the horseshoe vortex.
Figure 9 plots the limit streamlines of the coolant and the mainstream flow under different NECs, clearly revealing the intermixing and transport of flows. The incoming flow is separated into two legs: the pressure-side leg and the suction-side leg of the horseshoe vortex. At the flat endwall, the suction-side leg of the horseshoe vortex flows to the suction side under the action of the transverse pressure gradient. The pressure-side leg of the horseshoe vortex continually absorbs the low-energy fluid in the region near endwall to institute the passage vortex. The blue arrow indicates the position where the pressure-side leg of the horseshoe vortex reaches the suction side. On the whole, Cases 1 and 2 significantly reduce the circumferential pressure gradient and inhibit the development of the pressure-side leg of the horseshoe vortex. In addition, due to the lack of a small value valley buffer, Case 2 creates a low-pressure region at 10% C
ax, where the secondary flows briefly converge (as shown in
Figure 9c). As for Case 3, because of hump contouring between the pressure-side leg of the horseshoe vortex and the pressure side, the pressure-side leg of the horseshoe vortex reaches the suction side in advance. In Case 4, due to the formation of a hump between the suction-side leg and pressure-side leg of the horseshoe vortex, the pressure-side leg of the horseshoe vortex is confined in the valley to impede development. Meanwhile, a part of the pressure-side leg of the horseshoe vortex climbs along the hump and then converges with the suction-side leg of the horseshoe vortex to form a stagnation region (as shown in
Figure 9e), which increases aerodynamic losses.
The total pressure loss coefficient tells the flow loss via the examination of the reduction of the total pressure in the cascade.
Table 4 records the reduction percentage of the average total pressure loss coefficient at the outlet and is based on a flat endwall. It can be seen that Cases 1, 2, and 3 can lessen the total pressure loss by a maximum of 0.305%, indicating that the reduction of the circumferential pressure difference can inhibit the growth of secondary flows. Moreover, although Case 4 weakens the strength of the pressure-side leg of the horseshoe vortex, the increase in the circumferential pressure difference is not conducive to reducing aerodynamic losses.
To sum up, for the high-load turbine vane selected in this paper, under the condition of purge flow cooling, an NEC based on the differential pressure method can reduce the aerodynamic losses of the cascade by lowering the transverse pressure difference, and Case 3 has the best aerodynamic characteristics. On the contrary, Case 4 achieves the worst aerodynamic performance.
3.2. Film Cooling Performance Analysis
Figure 10 points out that with the limit of the suction-side leg and pressure-side leg of the horseshoe vortex, the purge flow is not evenly distributed on the endwall and has an insufficient coverage effect on the leading edge of the vane and the endwall near the pressure side, constantly moving toward the suction side. Due to the constrained transverse pressure gradient in Case 1 and Case 2, the enrolling ability of the passage vortex to purge flow is inhibited, and the coolant is restricted to the area closer to the endwall near the suction side. In Case 3, owing to the hump around the pressure side, the pressure-side leg of the horseshoe vortex is closer to the suction surface, the purge flow is also sucked by it, and the cooling effect decreases immensely. In Case 4, due to the hump near the suction side, the purge flow is slightly affected by the pressure-side leg of the horseshoe vortex and achieves great coverage. It should be noted that in a location in Case 4, where the hump contouring amplitude is the largest, the film cooling effectiveness is lower than it is in the surrounding area.
Obviously, NECs will increase the surface area of endwalls. Hence, a dimensionless effective coolant coverage area
is introduced to quantify the effects of the NEC on purge flow. An area of
> 0.05 is chosen as the effective coverage area of coolant, and the area from the outlet of the slot to the endwall of the trailing edge is
.
Table 5 shows the increase in Δ
by taking the effective coverage area of the flat endwall as the basis for different NECs. The results indicate that in Case 1, Case 2, and Case 4, the coverage area of the coolant can still be significantly increased by increasing the endwall surface area, and the maximum increase is observed in Case 4. Compared with Case 1, due to the weakening of the suction-side leg of the horseshoe vortex, Case 2’s coverage area of coolant increased by 3.33%.
To explain the influence of different NECs on the film cooling performance in more depth, the axial distribution of the laterally average film effectiveness of the flat endwall and the NECs are shown in
Figure 11. Overall, Case 4 can improve the laterally averaged film effectiveness of the entire endwall compared to the flat endwall. Case 2 enhances the laterally averaged film effectiveness of region Z/C
ax > 0.2; for Case 1, although the area covered by coolant is increased, the global laterally averaged film effectiveness is decreased. Case 3 has the worst cooling performance, similar to what is observed in
Figure 10. In addition, various NECs can improve the film cooling effectiveness in the range of Z/C
ax > 0.75.
3.3. Effect of Slotting Angle on Gas Film Cooling Characteristics of Molded Endwall
At a certain mass flow rate, the slotting angle will impact the mixing of purge flow and the mainstream flow, thus, affecting the endwall’s cooling performance. Combining the conclusions in
Section 3.2 with the aerodynamic and cooling characteristics, this section investigates the influence of 30°, 45°, and 60° angles (as shown in
Figure 12) on the cooling characteristics in Case 1 and Case 2. In this section, the other parameters remain unchanged, with the exception of changing the incident angle of the slot, W = 10 mm.
Table 6 shows the increase based on the effective coverage area of the initial endwall at different incident angles—Δ
.
Figure 13 states the purge flow cooling effectiveness distribution at different angles, and the results indicate that the angle has a great influence on the coverage of the coolant; under the 30° inclination angle, the momentum of the radial component of the coolant is the smallest. The coolant can better cover the endwall, and the film-cooling effectiveness on the pressure side is significantly increased. On the contrary, due to the large radial component’s momentum at the 60° inclination angle, a small amount of coolant covers the endwall. In this context, Case 1 and Case 2 weaken the passage vortex, with a small amount of coolant on the endwall being fully diffused and protecting the downstream area of the suction surface.
To further illustrate the influence of different incident angles on the cooling performance in different areas of the endwall,
Figure 14 shows the axial distribution of the laterally average film effectiveness of the endwall. The results show that the angle of 30° is favorable for coolant covering the endwall, and Cases 1 and 2 reduce the laterally averaged film effectiveness. When the inclination angle is 60°, Case 2 can improve the laterally averaged film effectiveness throughout the whole passage.