This study presents results from an experimental investigation of head-losses and the hydrodynamic performance of six angled trash-rack types with 15 mm bar spacing, varying bar-setup (vertical-streamwise, vertical-angled and horizontal bars) and bar profiles (rectangular and drop shape) under steady flow conditions.
Furthermore, we confirmed that the EIT-like feature could be controlled by simply varying the bar length of two different SRs.
The bond properties of the OPSC specimen with varying reinforcing bar diameters (12 and 16 mm), concrete cover sizes (50, 75 and 100 mm) and compressive strengths (25 and 35 MPa) were explored.
For the results using the time-varying (bar {gamma } k)), the window length is E=20 and when the number of updates in the window is less than 4, we assume the algorithm is in the steady-state period.
For the SM-NLMS algorithm, we consider three cases: fixed (bar {gamma }) with unknown noise bound (blue solid line), fixed (bar {gamma }) with known noise bound B=0.11 (cyan solid line), and time-varying (bar {gamma } k)), defined as (sqrt {5sigma _{n}^{2}}) during the transient period and (sqrt {9sigma _{n}^{2}}) during the steady-state, with unknown noise bound (green solid line).
All specimens showed pullout mode of failure under varying embedment length, bar type, bar diameter and concrete type.
Based on experimental and Code based analyses, the following conclusions were drawn: All specimens showed pullout mode of failure under varying embedment length, bar type, bar diameter and concrete type.
In our problem, on varying beam orientation, temperature ((bar K)), or damping rate, one may increase or decrease the number of unstable modes in the system and expect similar results as in the previously mentioned finite domain case.
The model is based on kinetic data obtained by volumetric titration measurements within a range of experimental conditions varying from 0 bar to 35 bar and from 100 °C to 190 °C.
The model is based on kinetic data obtained by volumetric titration measurements performed on each of the two absorption steps of sodium alanate, within a range of experimental conditions varying from 10 bar to 110 bar and from 100 °C to 180 °C.
