Item Description 1st classa (JSCE) Test results Construction condition Minimum gap between reinforcements (mm) 30 60 – Flowability Slump-flow (mm) 600 700 655 Segregation resistance ability Time required to flow through V-funnel (s) 9 20 10.64 Time required to reach 500 mm of slump-flow (s) 5 20 6.61 Self compacting ability Filling height of U-box (mm) ≥300 ≥300 aData taken from JSCE (2005).
To achieve one mm of slump-flow, Mix 2, Mix 8, and Mix 12 require a dosage of HRWRA between 1875, 1730, 2960 ml/m3, respectively.
For a heat exchanger with a louver angle of 27°, fin pitch of 2.1 mm and flow depth of 27.9 mm, a series of tests are conducted for the air-side Reynolds numbers of 80 400, with variation of inlet humidity condition.
Raja et al. [ 30] evaluated Treg cells in both peripheral blood and bone marrow in a larger number of cases of MM using flow cytometry.
Then, all the goals were optimized together, considering the priority of the goals, and the optimum results were found to be fin width of 14 mm, fin height of 150 mm, spanwise distance between fins of 20 mm, streamwise distance between fins of 10 mm and flow velocity of 4 m/s.
Figure 2 shows the UV-visible spectra of AuNPs synthesized from a chloroauric acid concentration of 0.03 mM at flow rates of 16.9, 25.5, and 37.0 mL/min (Figure 2A, B, C).
The optimum combination of parameters consisting of smaller beads size (0.8 mm), higher flow rate of 90 ml/min and glucose concentration of 10 g/l were found to be the maximum condition for ethanol production.
Optimum EtBr degradation was achieved by applying a current of 0.90 A, 9.0 mM Na2SO4, flow rate of 400 ml min−1 and pH 6.2 at 60 min of electrolysis, being reduced color by 80.2% and COD by 29.7%, with an energy consumption of 398.32 kW h (kg COD)−1 and a general current efficiency of 10.1%.
The effects of pulse repetition frequency (PRF) in the range of 10 300 kHz, number of pulses in the range of 1 50 (≈2.9–145 mJ), equivalence ratio in the range of 0.55 0.65, gap distance in the range of 0.5 2.5 mm, and flow velocity in the range of 2.5 10 m/s are explored.
The gas liquid mixture from a y-shaped mixing chamber was forced to pass through a plenum inlet and entered 21 parallel rectangular micro-channels 40 mm long in the direction of flow.
