Shaft-inflow pumping stations have frequently been constrained to the urban and rural planning, as well as the land use. For instance, the mainstream deviation and backflow are prone to occur, leading to poor inflow conditions in the design-constrained shaft-inflow pumping station, particularly harmful to the safe, stable, and efficient operation. The shaft-inflow pumping station can distribute the water into the forebay through the bottom pipe culvert and the inlet shaft, thus resulting in the complex flow in the forebay. The water flow in the forebay and inlet sump is often characterized by the concentrated mainstream and uneven velocity distribution in the vertical direction. This study aims to improve the flow pattern of the shaft-inflow pumping stations. Numerical simulation and physical model tests were also adopted to determine the low flow pattern in the forebay of a shaft-inflow pumping station under the rated operating flow rate of 28.92 m³/s. Among them, the inlet boundary was set as the pressure inlet, while the outlet boundary was set as the mass flow outlet, and the walls were set as the non-slip wall. On the water surface, the numerical simulation of the volume of fluid (VOF) and the rigid-lid hypothesis were compared to consider the calculation cost and efficiency. The rigid lid hypothesis was ultimately adopted to simulate the water surface. Qualitative and quantitative analysis was conducted using the rotation correction factor, velocity uniformity, and global reflux coefficient. The various types of diversion pier were rectified on the flow pattern in the forebay. The final optimization of the diversion pier was recommended using the response surface method (RSM). The results show that a significant mainstream diversion appeared in the forebay, and then a large-scale reflux zone was formed, due to the bottom inflow and excessive diffusion angle. The hydraulic performance of the pumping station was obtained after optimization. Compared with the vorticity, the rotation correction factor was used to effectively characterize the large-scale reflux zone in the forebay of the pumping station. A comparison was also made on the rectification of the diversion piers configuration in front of the forebay and inside the box culvert. The diversion piers were used to adjust the flow pattern, where the mainstream was guided to uniformly spread in the forebay. Diversion piers were arranged inside the box culvert in order to improve the flow pattern in the forebay. The diversion pier configuration was then optimized in the box culvert using RSM. There was a relatively strong correlation between the distance between the head of diversion pier and the outlet of box culvert X and the angle between the diversion pier and the pumping station θ. The objective function S was solved within the ranges of 1.619 75D ≤ X ≤ 1.835 01D, 0.660 369D ≤ b ≤ 0.665 309D, and 7.475 56β ≤ θ ≤ 8.25 672β. The optimal combination of the diversion pier was obtained: the distance between the head of the diversion pier and the outlet of box culvert X was 1.740D, while the distance between the head of the diversion pier and the inner wall of box culvert b was 0.662 5D, and the angle between the diversion pier and the pumping station θ was 0.333β. The uniform velocity and the global reflux coefficient of the optimal scheme increased by 28.02% and 13.72%, respectively, compared with the scheme without a diversion pier. Finally, the numerical simulation was verified through physical model tests. The surface flow pattern after numerical simulation was similar to the physical test. The relative errors of the hydraulic loss and mean velocity in the forebay were less than 5% and 9%, respectively, indicating the accurate simulation and the reliable optimization scheme. The finding can also provide the theoretical and technical support to the safe and stable operation of the shaft-inflow pumping station.

In order to improve undesirable flow phenomena like spinning and partial flow in forebays of deep tunnel inflow pumping stations, the flow in forebays was numerically simulated based on the RNG k-ε turbulence model, and rectification measures applicable to this kind of urban drainage pumping station were investigated. Numerical simulation results revealed the presence of several adverse hydraulic phenomena within the forebay and inlet pool of the pump station, including local vertical spinning, spiral flow, oblique flow, and uneven velocity distribution with higher velocity at the top and lower velocity at the bottom, resulting in poor hydraulic conditions in the inlet channel of the pump station. A rectification measure combining a double-layer ring plate and two groups of guide piers can suppress the vertical spinning, spiral flow and oblique flow in the forebay and inlet pool. This rectification measure significantly improves the inlet conditions of the flow channel, leading to more uniform flow velocity distribution at the inlet of the inflow channel. Consequently, the pump inflow water conditions become better, and the operation reliability of the pumping station is improved.

To study the flow characteristics of the vortex-type grit chamber and improve the sand removal efficiency, the flow characteristics and sand removal efficiency of the vortex-type grit chamber initially set up in a sewage pumping station were analyzed by RSM model and DPM model based on the numerical simulation method. In view of the shortcomings of the vortex-type grit chamber, the optimization scheme of adding deflector plate were proposed, and the flow characteristics and sand removal efficiency of deflectors in different schemes with different lengths were compared. The results show that the water flow in the vortex-type grit chamber presents a spiral shape due to the horizontal circulation and elevation circulation caused by wall barrier and impeller blade rotation. When the water flow enters the pool along the inlet channel, it has an impact on the rotating water flow in the pool body, and the inlet flow with high velocity shifts to the center of the pool under the action of pressure difference, which easily rolls away the sand particles near the center of the pool, affecting the sand removal effect of the vortex-type grit chamber. Adding a baffle at the end of the inlet channel can effectively reduce the impact of the inlet flow on the rotating water flow in the sand settling basin and make the water flow that hits the baffle turn down to the bottom of the pool, thus improving the sand removal efficiency. Comparing the three baffle schemes, the sand removal effect is better when the length of the baffle is 2000 mm. The sand removal efficiency of 0.10, 0.15, 0.20 mm sand particles increased by 7%, 11% and 2%, respectively.