3.2.1. Theoretical Modeling of Axial Piston Pump
Axial piston pumps are widely used in industries like manufacturing, aerospace, and mobility due to their ability to provide high power density and easy flow control [
49]. To ensure high reliability and longevity, manufacturers must deeply understand axial piston pump internal structures and operating principles. A typical design contains a rotating group including a splined shaft, cylinder, nine piston-slipper assemblies, and retainer, as depicted in
Figure 6. A compression spring in the central bore pushes the cylinder against a fixed valve plate attached to the pump casing. Concurrently, slippers contact an inclined swash plate pad. The splined shaft rotates the cylinder, reciprocating each piston in its chamber. This reciprocation alternately suctions oil from the low-pressure side and discharges it to the high-pressure side through the valve plate ports. In addition to rotation, the cylinder performs a tilting motion for solid contact with the valve plate [
50]. This tilting motion of the cylinder body is influenced by factors such as periodic eccentric load, multi-degree of freedom, spline transmission clearance, and shaft bending. As a result, the cylinder body and the valve plate maintain a secure contact [
51]. In addition to the previously discussed components, axial piston pumps may incorporate additional features, including a pressure relief valve, a case drain line, and a charge pump. The pressure relief valve regulates the pump’s pressure, preventing system damage and ensuring consistent performance. The case drain line removes any excess fluid that may accumulate in the pump case, while the charge pump supplies oil to the pump during start-up.
- A.
Kinematic model
The motion of the piston in an axial piston pump is influenced by the shaft rotation and the swashplate angle, resulting in a sinusoidal, harmonic, or oscillatory displacement along the cylinder axis. The piston’s velocity and acceleration are determined by the angular velocity and displacement of the shaft, along with the inclination of the swashplate. As the piston moves, it generates a periodic variation in the cylinder volume, leading to fluid flow through the valve plate ports.
As shown in
Figure 7, the displacement along the axial direction can be expressed as follows when the piston moves from point A to point C:
where
R is radius of pitch circle,
β is the swashplate angle,
φ is the rotational angle of cylinder block.
The velocity of the piston is obtained by differentiating the displacement of the piston with respect to time:
The piston’s position affects the volume within its chamber, expressed as:
where
V0 is the fluid volume of the piston chamber in the inner dead center (IDC),
dp is the piston diameter.
- B.
Leakage flow
The major components of leakage in a piston pump encompass internal leakage, external leakage, and flow loss resulting from fluid compression. Among these, external leakage constitutes the largest portion. External leakage comprises piston-slipper leakage, shoe-slipper leakage, and valve plate leakage, all of which are primarily influenced by the oil film thickness between the moving pairs. Additionally, the Reynolds numbers associated with the three leakage gap flows are small, enabling the calculation of friction pair leakage in the piston pump based on laminar flow theory.
- (1)
Piston/cylinder pair
As shown in
Figure 8, throughout the operational cycle of the axial piston pump, the piston experiences a centrifugal force, resulting in the formation of an eccentric annular gap with the center of the cylinder bore. This pressure difference gives rise to Poiseuille flow within the gap. Simultaneously, the axial displacement of the piston within the cylinder bore induces Couette flow in the opposite direction to the Poiseuille flow. As a result of the combined effect of these flows, the leakage of the piston pair can be mathematically expressed as follows:
where
d is the piston diameter;
δ1 is the oil film thickness of the piston/cylinder pair;
μ is the dynamic viscosity of the hydraulic oil;
L is the contact length of the piston and the cylinder;
e is the eccentricity of the piston;
p0 is the tank pressure.
- (2)
Piston/slipper pair
The amount of fluid that escapes from the gap between the slipper and the swash plate, as depicted in
Figure 9, constitutes the leakage of the piston/slipper pairs. This leakage is a significant contributor to power loss in an axial piston pump, which can be represented as follows:
where
h is the thickness of the oil film of the piston/slipper pair;
r1 is the inner radius of the slipper sealing ring;
r0 is the outer radius of the slipper sealing ring;
ld is the length of the piston chamber.
- (3)
Cylinder/Valve Plate Pairs
The leakage of the cylinder/valve plate pairs is caused by the hydrostatic support of the oil during the flowing process. As shown in
Figure 10, based on the laminar flow theory of parallel circular disk gaps, the leakage is calculated as follows:
where
α is the length angle of the kidney port;
δ3 is the thickness of the oil film between cylinder and valve plate;
R1,
R2,
R3 and
R4 are the radius of the valve plate, respectively.
- C.
Valve plate
In a swashplate axial piston pump, the housing holds the swashplate in a fixed position, while the valve plate remains attached to the housing. The pistons, however, are pressed against the swashplate by the retainer. As the shaft rotates the cylinder block, each piston chamber establishes a connection with the suction port and the discharge port through the valve plate. This connection determines how long each piston chamber communicates with the inlet and outlet ports, based on its unique structure. The size of the kidney port on the valve plate is typically kept smaller than the cylinder block port to ensure maximum oil sucked and discharge from the piston chamber. Precise design of the sizes of the inlet and outlet kidney ports, as well as the cylinder block port, is crucial to ensure that the cylinder block port exclusively communicates with either the inlet or the outlet at any given time.
Figure 11 demonstrates the addition of pressure relief grooves at the beginning and end of the kidney-shaped holes, which facilitate smooth flow transitions when entering or leaving the piston chamber through the suction or discharge port. By adjusting the position and size of the pressure relief groove, it is possible to significantly influence the suction and discharge flow, thereby reducing fluid fluctuations and minimizing vibration noise. These optimizations of the valve plate align with our primary objectives.
The dynamics of the pump are indeed influenced by the valve plate, as it plays a crucial role in determining the communication area between the piston chamber and the inlet and outlet ports. The positional relationship between the piston chamber and the kidney port is key in establishing this communication area when the piston chamber connects to the triangular groove. In previous studies, this area can be calculated as follows [
52]:
where
R is the radius of the cylinder port,
θ1 and
θ2 are the width angle and depth angle of the triangle groove, respectively.
- D.
Piston chamber pressure
The piston chamber undergoes periodic changes in its enclosed volume. As the cylinder rotates, the piston reciprocates axially within the cylinder, causing compression or expansion of the oil volume within the piston chamber. Simultaneously, the piston chamber establishes a connection with the valve plate, allowing oil to flow in or out during the distribution process. By analyzing the pressure change characteristics within the piston chamber, the following information can be derived:
where
dp and
dV is the increment of pressure and volume in the piston chamber,
E is the volume modulus of the fluid.
Taking the process of oil suction from the piston chamber, leaving the IDC as an example, two parts can be identified in the volume change, namely dVf and dV2. dVf represents the volume from the discharge port to the piston chamber, dV2 refers to the volume obtained through mechanical compression. By considering these two components, the flow rate into the triangle groove can be calculated as follows:
where
Cq is flow coefficient, Δ
p is the pressure difference between piston chamber and inlet or outlet port,
ρ is the oil density.
In this study, the valve plate, as shown in
Figure 11, is positioned at a cross angle Δ
φ between the axes of the Inlet Dead Center (IDC) and Outlet Dead Center (ODC). The angle formed by the adjacent ends of the inlet and outlet ports and the central angle of the plunger rotor window is defined as the close angle Δ
φ. The magnitude of the cross angle determines the initial placement of the cylinder when it enters the closed dead zone. As the cylinder port rotates, the piston chamber gradually enters the closed dead zone, leading to compression or expansion of the enclosed volume. The behavior of the piston chamber differs significantly when transitioning into the closed dead zone from the IDC and ODC. At the ODC, the piston chamber experiences closed dead compression, while at the IDC, it undergoes closed dead expansion. By employing Δ
φ -
φ0/2, the initial contact position of the piston chamber and the closed dead zone can be expressed when considering the same close angle.
With the assumption that the closed dead zone initially holds a position of zero, the entry of the piston chamber into the closed dead zone occurs when it reaches the inter dead center. As the cylinder port rotates through an angle φ, the volume alteration of the piston chamber can be expressed as follows:
The pressure characteristic relationship of the piston chamber can be derived by incorporating Eqs. (17)-(23) and Eqs. (25)-(27) into Eq. (24), as follows:
The pressure change inside the piston chamber is strongly nonlinearly dependent on several parameters, as indicated by Eq. (28). These parameters include the size of the triangle grooves θ1 and θ2, the swash plate angle γ, the volume of the piston chamber Vf, the close angle φ0 and cross angle Δφ. In order to minimize the amplitude of pressure ripples in the piston chamber, leading to a reduction in both flow ripples and noise at the outlet port of pump, the utilization of an advanced optimization algorithm is imperative for determining the optimal parameter values.
3.2.2. Model Validation and Parametric Study
- A.
Measurement and validation
In order to validate the theoretical model of axial piston pump, the measurement of pump outlet pressure ripples was conducted on a pump-valve integrated test rig. The setup and arrangement of instrumentation can be observed in
Figure 12. A motor with a rated power of 35 kW drove the pump under test, maintaining a stable speed of 2000 r/min. The pump had a displacement of 71 cm3/r and a rated pressure of 27.5 MPa. However, due to power constraints of the driving motor, the outlet pressure during testing was limited to approximately 20 MPa. A relief valve was installed at the end of the outlet pipeline to regulate the discharge pressure. Positioned between the pump outlet and the overflow valve, a flow sensor integrated with a PX-459 pressure transducer was utilized to measure the discharge flow rate and pressure ripples. The transmission medium employed was aviation hydraulic oil, while a cooler and temperature sensor control system maintained a stable temperature in the tank.
Before initiating the testing, the entire test system underwent a stable operation for a minimum duration of half an hour. This was done to eliminate any air from the pipelines and maintain the stability of system variables. The testing process consisted of two steps. In the first step, the driving motor was started, and the supply current was adjusted to stabilize the speed at 2000 r/min by rotating a knob. Multiple tests indicated a slight decrease in the rotational speed of the driving motor as the pump outlet discharge pressure increased. Therefore, the initial rotational speed was set slightly above 2000 r/min when the overflow pressure was at 0 MPa. In the second step, the opening of the overflow valve was adjusted to stabilize the pump outlet pressure at 20 MPa. For data collection, a LANXI-3160 data acquisition system with six channels was utilized, with two channels dedicated to acquiring the pump outlet pressure data during the test. The sampling frequency was set at 1000 Hz to meet specific requirements.
The comparison of simulation and measurement results for the discharge flow rate ripples and variations is depicted in
Figure 13. The outlet discharge pressure was set at either 10 MPa or 20 MPa, while maintaining a rotational speed of 2000 r/min or 2200 r/min and the maximum swash plate angle. The obtained comparative results demonstrate a strong agreement between the simulation and measurement outcomes for both the highest and lowest pressure ripples. As the discharge pressure is directly linked to the piston chamber, it mirrors the variations in pressure occurring within the chamber.
- B.
The effect of close angle
The data in
Figure 14 shows three distinct values of
φ0 that occur as the piston chamber expands its volume while maintaining a near constant angle of approximately 12°. Simultaneously, the pressure inside the piston chamber decreases from 23.5 MPa to 0.75 MPa. At angles closer to 8° or 10°, compression of the piston chamber is initiated as it moves away from the suction port. Discharge from the triangular groove takes place once the maximum pressure is achieved inside the piston chamber, which subsequently leads to a reduction in pressure within the chamber.
- C.
The effect of cross angle
Figure 15 illustrates that the compressing area expands as the cross angle increases, leading to a faster increase in pressure. Conversely, a small cross angle causes an increase in the volume of the piston chamber, resulting in a decrease in pressure during the initial phase.
- D.
The effect of the triangular groove size
Figure 16 presents the pressure variation in the piston chamber, considering different sizes of the triangle groove at φ0 = 12°. It is observed that when θ1 is set at 20° and θ2 at 60°, the pressure continues to rise, but only a minimal amount of fluid passes through the triangle groove. As the open angle of the triangle groove increases, the fluid flow back into the piston chamber intensifies, leading to a faster amplification of the piston chamber pressure. However, it is worth noting that the piston chamber pressure with a larger open angle experiences a rapid decline once it exceeds 22 MPa.
- E.
The effect of wrap angle
The data shown in
Figure 17 indicates that the initial phase exhibits the highest pressure when the angle
φΔ is 12°. This high pressure level is mainly due to fluid flowing back into the piston chamber as the piston moves away from the suction port for the first time. In contrast, the initial phase shows the lowest pressure when
φΔ is 8°. Once the pressure inside the piston chamber surpasses 20 MPa, the pressure declines most rapidly for
φΔ of 12°, primarily because of the larger area available for fluid to exit through the triangular groove. Conversely, when
φΔ is 8°, the pressure remains the highest even after exceeding 20 MPa within the piston chamber.