1. Introduction
The extended use of High-Density Polyethylene (HDPE) 4710 in pressurized systems is due to its advantages over other alternatives, including high corrosion resistance, ease of handling and installation, high-quality butt-fusion welding, flexibility, and resistance to biological microorganisms such as fungi and bacteria.
Its important presence in the industry increases the requirement necessity for a more extensive evaluation of its mechanical behavior under both steady-state pressures and transient pressures caused by water hammer phenomena. These transients arise from wave trains propagating through pipelines as a result of sudden operational changes [
1,
2,
3,
4,
5], suggesting that neglecting the viscoelastic effects of the pipe wall can lead to significant errors in estimating both the velocity and attenuation of pressure waves.
Polyethylene (PE), as a material in continuous technological development, has undergone significant changes in its physicochemical properties over time, resulting in the emergence of different types of resin. Variations in the mechanical properties intrinsic to each resin type, along with residual stresses induced during various stages of pipe fabrication, operating temperatures, and wall thickness, affect the mechanical response of HDPE pipes [
6,
7,
8,
9,
10].
Polyethylene (PE) behaves mostly isotropically under low strain levels but exhibits anisotropic behavior under high strains [
10]. Studies conducted under uniaxial stress states report subtle differences in tensile and compressive properties obtained under relaxation and creep conditions. However, in practical applications, the material exhibits similar behavior across these conditions [
11,
12,
13]. In contrast, under multiaxial stress states—with circumferential stress approximately twice the axial stress—experiments involving internal pressurization of HDPE pipes and monitoring of diameter changes over time have shown that the apparent elastic modulus is about 25% higher than that obtained under uniaxial conditions. This difference is due to the combined stress components that constrain deformation [
11].
To represent the time-dependent behavior of PE in water hammer studies, an increasing number of investigations rely on generalized rheological models, such as the generalized Kelvin-Voigt and Maxwell models or creep compliance functions [
2,
3,
5,
10,
14,
15,
16,
17,
18,
19,
20,
21,
22,
23,
24,
25,
26,
27,
28].
Although these models provide high versatility in fitting numerical simulations to experimental data, the inclusion of numerous parameters can lead to overfitting [
20,
23,
27]. In many cases, multiple parameter combinations can reproduce the experimental results with practically indistinguishable differences [
5]. While several important studies [
3,
5,
14,
28] suggest that using four or five Kelvin–Voigt elements is generally sufficient to achieve good agreement with experimental data, accurately estimating the corresponding parameters remains a significant challenge [
29].
There are two common approaches to determining viscoelastic parameters. The first involves calibration using unsteady flow testing. However, this approach faces a significant limitation due to the difficulty in separating the dispersive and energy dissipation effects present during the water hammer phenomenon, such as viscoelastic deformations, unsteady friction, leaks, and other fluid-structure interactions. This overlap of effects can lead to ambiguous interpretations regarding the origin of energy losses observed in experimental studies [
2,
3,
5,
10,
14,
15,
16,
17,
18,
30]. The second approach relies on standardized tests, such as those proposed by the American Society for Testing and Materials (ASTM) [
31,
32,
33,
34,
35], which characterize material behavior through creep functions, relaxation modulus, apparent elastic modulus, long-term modulus, and flexural modulus. Although results from this testing methodology show a significant correlation with those obtained from water hammer experiments, the viscoelastic material response remains incompletely characterized because ASTM mechanical tests are designed for load or displacement rates slower than those occurring during water hammer events. Therefore, adapting and proposing alternative testing methods may improve the reliability of material characterization under actual working conditions. The work of Autrique-Ruiz et al. [
36] evidences the relationship between instantaneous elastic modulus and wave celerity in HDPE 4710 pipes.
The complexity of estimating viscoelastic parameters for multimodal models encourages the use of models that better preserve the physical interpretability of mechanical behavior, rather than focusing on overly detailed fitting of hydraulic responses for a specific case study [
3,
28]. In this context, the Standard Linear Solid Model (SLSM) is an attractive alternative since it uses only three parameters—long-term modulus, Maxwell branch modulus, and viscous parameter—to reproduce both instantaneous and delayed deformations typical of thermoplastic materials. Its formulation leads to simple mathematical solutions with low computational costs in water hammer analysis, providing advantages when studying more complex systems composed of pipe sections with varying lengths, diameters, thicknesses, and materials, as well as heterogeneous pipeline networks [
15,
25,
26,
28,
30,
37].
Many studies [
15,
25,
26,
28,
30,
37] conclude that, within the range of short characteristic times typical of water hammer, the Standard Linear Solid Model (SLSM) can attenuate and disperse the pressure wave with sufficient accuracy for design and diagnostic applications. Moreover, as a viscoelastic model with a reduced number of parameters, it benefits the establishment of direct relationships between these parameters and the physical characteristics of the pipe system under analysis. Pezzinga et al., Carmona-Paredes et al., and Paniagua-Lovera et al. [
17,
18,
20,
27,
28,
30,
37] suggest that a strong correlation exists between viscoelastic parameters and the characteristic time of pipeline systems, defined as the period of the pressure wave.
This paper addresses these challenges from a perspective focused on material behavior, proposing a practical methodology for viscoelastic characterization and its application to HDPE 4710. The organization of this work is as follows: (i) an experimental testing configuration consisting of a displacement ramp followed by a stress relaxation stage in rings under diametral loads; (ii) an analytical formulation of bending in viscoelastic beams using the Standard Linear Solid Model (SLSM); (iii) calibration of viscoelastic parameters by fitting the numerical solution to experimental data from six pipe ring specimens; (iv) proposal of adjustment equations to obtain the SLSM parameters; and (v) validation of the methodology by comparing the proposed method’s results with observed data from one test not included in the calibration group, demonstrating the method’s capability to correlate with known physical variables during the design stage, where the characteristic time is a dominant factor influencing the viscoelastic parameters.
5. Conclusions
This paper presents a framework for estimating the viscoelastic parameters of PE pipes based on the results of a new setup for experimental testing of rings under diametral loads and its application to HDPE 4710 material represented by the SLSM. The methodology considers factors such as temperature, thickness-to-outer diameter ratio, and characteristic time. The main conclusions of this research are the following:
The experimental methodology and material response representation using the SLSM apply to other PE resins or polymers exhibiting linear viscoelastic behavior. Furthermore, the proposed preparation, installation, instrumentation, and experimental procedure offer economic and spatial advantages over other testing methods used to characterize the mechanical properties of pipes under sustained or transient pressures.
Performing the imposition ramp as briefly as possible is essential for accurately estimating the instantaneous elastic modulus. Longer ramps increase damping in the mechanical response and may lead to an underestimation of this modulus. Complementing its determination with water hammer testing and wave speed analysis further improves the reliability of the instantaneous elastic modulus estimation.
Increasing the sample size and range in key variables, such as temperature and outer diameter, reduces uncertainty in the viscoelastic parameters. Also, it provides information for further improvements in expressions, such as the compensating temperature multiplier, as this work directly accepts the proposal by PPI [
11].
Based on the correlation coefficients obtained during parameter calibration in the imposition and relaxation stages, the mathematical model based on the SLSM accurately reproduces the experimental response of HDPE pipes subjected to displacement imposition through diametral loads for characteristic times of up to 5 s. The SLSM effectively models viscoelastic behavior in rapid pipeline phenomena such as water hammer, as observed for [
14,
30,
36,
37,
49]. To reproduce phenomena at longer characteristic times than those captured by the SLSM, it is necessary to explore generalized Kelvin-Voigt models proposing a methodology that correlates viscoelastic parameters with known physical system characteristics, thereby enabling the correct analysis in design engineering stages and avoiding overfitting problems that can lead to ambiguous conclusions.
The variations in viscoelastic parameters observed for different thickness-to-outer-diameter ratios provide evidence of residual stresses induced during the extrusion and cooling stages of the manufacturing process. These stresses alter the morphology of HDPE polymeric chains, directly affecting mechanical behavior. Generally, residual stress effects are more pronounced in thick-walled pipes (with lower thickness-to-outer-diameter ratios), a phenomenon also reported by [
8].
The long-term elastic modulus depends on characteristic time, temperature, and thickness-to-outer-diameter ratio. The apparent elastic modulus trend, along with its corresponding temperature compensation multiplier reported in [
11], aligns with the long-term elastic modulus obtained through numerical calibrations of the relaxation stage in specimens subjected to a flexural mechanical state for thin-walled pipes (with higher thickness-to-outer-diameter ratios). Thick-walled pipe rings exhibit a higher long-term elastic modulus than thin-walled pipes.
Similar to the long-term elastic modulus, the dynamic elastic modulus, adjusted using temperature compensation factors reported in [
11], shows consistency with the instantaneous elastic modulus calibrated during the displacement imposition ramp for thin-walled pipes. Thick-walled pipes exhibit higher instantaneous modulus values than thin-walled pipes.
This study proposes adjustment equations to estimate the viscoelastic parameters of the SLSM for HDPE 4710. These equations demonstrate a strong correlation with variables such as characteristic modeling time, temperature, and a fabrication factor representing the influence of residual stresses on the pipe’s mechanical properties.