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A case study related to capacity management of a buffer tank in a petrochemical plant is presented.
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The system is composed of a water electrolysis unit, a hydrogen buffer tank, a metal hydride tank and a polymer electrolyte membrane fuel cell (PEMFC).
Gel and buffers were equilibrated at 4 °C before electrophoresis and buffer tank was placed in an ice bath during electrophoresis to maintain the low temperature (less than 15 °C).
Gels and buffers were equilibrated at 4°C before electrophoresis, and the buffer tank was placed in an ice bath during electrophoresis to maintain the low temperature.
Gels and buffers were equilibrated at 4 °C before electrophoresis, and the buffer tank was placed in an ice bath during the electrophoresis to keep the temperature of the gel below 15 °C.
In order to minimize the negative influence of mixed conditions at the entrance of a rotodynamic multiphase pump (MPP), a buffer tank was designed and installed in front of the pump.
Gels and buffers were equilibrated at 4 °C, and the buffer tank was cooled during electrophoresis in an ice bath.
The MPC generated the dynamic temperature set-point profiles of the zone air and buffer tank water which resulted in the operating cost reduction of the equipment without violating the thermal comfort constraints.
The test is carried out with a constant level of liquid helium in the dewar and constant pressure in the buffer tank.
Western blot transfers were carried out for 2 hours at 400 mA at 4°C in a Hoeffer transfer tank in a buffer containing 200 mM tris base, 1.5 M glycine, and 20% methanol.
The control performance is further improved after a buffer tank is installed upstream of the process.
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