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Tests were conducted using a small-scale stainless steel pressure vessel pressurized with helium to 2 bar or 5 bar at room temperature.
The high-pressure reactors were pressurized with nitrogen gas up to 15 MPa (equivalent to 1,500 m DWH well depth).
For QUENCH-L0 each rod was separately pressurized with krypton with initial pressures from 35 to 55 bar.
Subsequently, 100 mg of yellow palladium (II) hexafluoroacetylacetonate, Pd(hfa 2, and a microcellular HDPE support were placed into the high-pressure reactor at 90°C and pressurized with 100 atm of CO2 for the supercritical impregnation process.
A beaker filled with 2.5 g of white HDPE beads (circular flat white beads with an average diameter, height, and weight of 3 mm, 1.5 mm, and 14 mg, respectively; Tm = 130°C) is placed in a 20-mL high-pressure reactor at 140°C and pressurized with 200 atm of CO2 for the supercritical foaming process.
The specimen is introduced into a pressure chamber at room temperature and rapidly pressurized, with cooling provided by liquid N2 flow through the metal sample holder.
The fire that killed the Apollo 1 crew in a launch pad test spread so rapidly because the capsule was pressurized with pure but at slightly more than atmospheric pressure, instead of the normal pressure that would be used in a mission.
2.5 min after the onset of mixing, cement was applied in the acetabular model, and pressurized with 80 N for 1.5 min using a conventional pressurizer (Smith and Nephew), which was fitted into the Instron machine.
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High-pressure reactors (right, made from stainless steel and bronze, max. pressure 40 MPa, pressurizing with N2 gas, 160 mL volume) and aluminum control reactors (left, max. 0.1 MPa, 160 mL volume) were used for cultivation of hydrocarbon degraders at high and ambient pressure.
The reaction was started by pressurizing with H2 and recirculating the liquid/gas mixture by means of a high pressure pump.
The length of time to pressurize with gas was proportional to gas viscosity and the square of the length of column packing and inversely proportional to bed permeability and particle size.
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