The spray drying was performed at the pressure, inlet and outlet temperatures of 552 Kpa, 160°C and 80 85°C, respectively.
In more details, the PRO simulation was performed at the hydraulic pressure of P t = (π D,t − π F,t )/2 (Eq. 7, at the maximum energy mode), and was stopped when water flux dropped below 0.5 LMH (L m−2 h−1).
The Y-type deposition of LB film was performed at the targeted pressure with a dipping speed of 10 mm min-1.
Blood gas analysis was performed at the end of each pressure support step (IL1620; Instrumentation Laboratory, Lexington, MA, USA).
The electrical measurements were performed at a pressure of about 10 Pa to minimize the influence of atmospheric humidity.
The transfers were performed at a pressure of 0.8-1.9 kg/cm for approximately 2 s up to 7 sequential transfers either to carriers or to food products.
The hydrogen absorption was performed at a pressure of 11 bars H2 and a temperature of 280 °C.
LPCVD was performed at a pressure of ∼0.57 Torr in a tube furnace under a CH4/H2 atmosphere at 1050 °C for 1 and 3 h.
Polyethylene glycol (PEG) ca. 500 ppm solutions over a range of specified molecular weights were used for evaluating the selectivity or rejection tests of polysulfone and PSu/PANI nanocomposites membrane and tests were performed at a pressure of 5 bars.
Dry sliding tests were performed at a pressure of 7 × 10− 6 torr and under ambient conditions, using a ball-on-disc configuration.
