1. Introduction
Turbulent flows in a ribbed channel are present in numerous fields of engineering, such as heat exchange [
1,
2] turbines [
3], maritime engineering [
4], and the mining industry [
5]. The structure of the airflow between two adjacent ribs differs depending on the Reynolds number and the distance between the ribs. Perry et al. [
6] suggested that the flow between ribs should be divided into a d-type and a k-type flow. The former applies to a geometrical configuration, where the distance between two adjacent ribs is small. In this case, stationary vortex is present in the cavity between the two ribs. The mass transfer between the cavity and the airflow over the rib is minor. When the distance between two adjacent ribs is greater than a certain limit value, the stream on the leeward slope of the rib becomes detached. When the w/k ratio (where “w” is the distance between the ribs and “k” is the rib height) reaches a certain limit value, the stream becomes reattached between the ribs and a recirculation zone arises downstream of the leeward slope of the rib.
Coleman et al. [
7] presented studies of turbulent flow in a channel with repeated roughness for the w/k ratio ranging from 1 to 16. The transition from the d-type flow to the k-type flow occurs at w/k = 5. A transitional state is present at that point. Stable vortices occur between the ribs in the case of the d-type flow. In the case of the k-type flow, two vortices characterized by an opposite rotation direction are present between the ribs. Numerical calculations based on the large eddy simulation (LES) method, confirming the presence of both k- and d-type flows, were carried out by Cui et.al [
8]. The boundary between a change in the flow structure occurs for the w/k ratio equal to 4. In the same publication, it was also confirmed that the flow structure also depends on the height of a single rib (k). In [
9] the authors presented the results of studies, conducted using the particle image velocimetry (PIV) method, of water flow in a channel with rough, square-shaped ribs within the 1400–50,000 Re number range. The ratio of the height of a single rough element to the distance between such elements was 1/10 and 1/20. The authors concluded that vortices were forming near the top edge of the rib. They also noticed such phenomena as recirculation, detachment, and reattachment of the stream, the range of which only depended on the Re number to a minor extent. Wang et al. [
10] performed PIV measurements in a ribbed channel for Re = 22,000. The flow structure near the rib was identified. A probability density function (PDF) analysis of velocity fluctuation was carried out, which demonstrated the existence of two modes in the shearing layer. Additionally, the vortex topology was determined. Leonardi et al. [
11] performed numerical calculations using the direct numerical simulation (DNS) method in a channel with a single ribbed wall (with square-shaped ribs). Simulations were conducted for the conditions of a fully developed turbulent flow for the 8800–20,800 Re number range. Analyses were carried out for Re = 8800. The authors analyzed the w/k ratio in several configurations from 0.33 to 19. Two vortices with the opposite rotation direction appeared in the cavity between the ribs for the w/k ratio below 4. When the w/k ratio was equal to or greater than 7, the flow was reattached on the bottom wall.
The problem of turbulent flow near square rough elements was examined by Stoesser et al. in [
12]. The authors performed numerical calculations using the LES method for two flow regimes: of the k-type (w/k = 9) and a transitional one between the d- and the k-type (w/k = 4.5). They observed differences in the flow structure between the two regimes despite the fact that in both regimes water flowed into and out of the cavity between the ribs, and despite the fact that there was a recirculation zone present in the cavity. The calculations performed using the LES method yielded similar results to the measurements carried out by Coleman et al. [
7] as well as the numerical calculations performed using the DNS method by Leonardi et al. [
11].
Square-shaped ribs are the most common rough elements described in the literature. However, the problem of flow in a channel with a trapezoidal rib has only been described in a few studies. Using the PIV and liquid crystal thermography (LCT) methods, Ali et al. [
13] determined the effect the acute angle of the right-angled trapezoid on the flow structure and the distribution of heat downstream the rib for four Reynolds numbers within the 9400–61,480 range. For Re = 9400, the range of the recirculation zone is independent of the angle. For the remaining Re numbers, the recirculation zone increases in size with the increase in the angle of the trapezoid. In their publication, Skotniczny and Ostrogórski [
5] presented the results of measurements and numerical simulations of an airflow near a side wall of a mining longwall working with supports, the elements of which resembled trapezoidal ribs. Velocity measurement results collected in an actual mine were compared with the results of a two-dimensional CFD simulation carried out using a k-ω scale adaptive simulation SAS turbulence model. The velocity value determined experimentally was consistent, to a satisfactory degree, with the velocity obtained through calculations. Large discrepancies between the measurements and the simulation were obtained for turbulence intensity as well as for the kinetic energy of the turbulence.
The results of the measurements presented in this paper provide additional information on the problem of transitional flow occurring between two rough elements and can be used for the purpose of comparison with numerical calculations.
2. Materials and Methods
The experimental setup used for flow testing in a channel with one rough wall consisted of a single radial fan, a section designed to equalize the flow and a measuring channel. Due to its size, the experimental setup is presented in two figures:
Figure 1 and
Figure 2. The radial fan, with inverter-controlled rotational speed, supplied air into the flow equalization section consisting of the following elements: a straightener, a diffuser with two rows of grids, and the first and second confusor connected with the measuring channel (
Figure 1).
The 1.2 m long measuring channel with a 0.20 m × 0.02 m internal cross-section was made of mineral glass. The top wall and the side walls were smooth along their entire length, whereas the bottom wall was smooth only along its initial (0.14 m) and its final (0.1 m) sections. Along its remaining length, the bottom wall featured periodic roughness in the form of evenly spaced, isosceles trapezoid shaped ribs positioned crosswise in relation to the direction of the flow. The ribs represented a simplified laboratory model of ribbed, arched supports used in mining longwall workings. The dimensions of the ribs (in millimeters) are presented in
Figure 3.
Velocity field measurements were carried out using the PIV method. The PIVTEC GmbH Goettingen, Germany aerosol generator with Laskin atomizer nozzles supplied Di-Ethyl-Hexyl-Sebacat (DEHS) marker particles into the channel through the suction opening of the fan. Based on the air dynamic viscosity 18.13 Pa·s, DEHS particle diameter 1 µm and density 912 kg/m3, channel height 0.02 m and mean velocity 29 m/s Stokes number is about 0.004. For Stokes number smaller than one particle, fluid streamlines were followed closely. The tested area was illuminated with a light sheet generated using a neodymium laser. An scientific Complementary Metal–Oxide–Semiconductor (sCMOS) camera, with its optical axis oriented perpendicularly to the plane of the laser sheet, recorded two pictures in a short interval. Each measurement consisted of a series of double pictures captured at a frequency of 15 Hz. The pictures were then sent to a PC, where dedicated software calculated instantaneous velocity fields, which were subsequently averaged over time.
Numerous initial tests were carried out prior to conducting the actual measurements. Optimal measuring conditions were determined on the basis of these tests and defects of the test station, e.g., a local leak of the channel, were identified and removed. It was ascertained that the length of the test station was sufficient for obtaining the required development of the velocity profile. During each of the measurements, the air velocity in the channel was controlled with a Pitot tube installed at the outlet and connected to a TSI Incorporated, Minnesota, USA Airflow meter. The Reynolds number, based on height H = 0.02 m and the average velocity in the initial, i.e., smooth section of the channel, was Re = 32,500.