The phrase "a practical operating" is not correct and does not convey a clear meaning in written English.
It may be intended to describe something that is functional or useful in a practical context, but it lacks clarity and completeness.
Example: "The team developed a practical operating procedure to enhance efficiency in the workflow."
Alternatives: "a functional operation" or "a useful process".
As a practical operating guideline, it is recommended that flow rates be limited to <0.4Qc for reliable performance of any μPCF used for quantitative analysis.
In this work, a low-Ni methanation catalyst was tested in a differential reactor to derive a kinetic model that could determine a practical operating scheme for the first methanation step of a typical bio-SNG process.
Says Caretta: "To be able to have a practical operating logic or memory racetrack device, you have to write the bit, so that's what we talk about in creating the magnetic quasi particle, and you have to make sure that the written bit is very small and you have to translate that bit through the material at a very fast rate," Caretta says.
The practical-sized MEA using Pt/TiN + 47 vol% AB showed 1.5 times greater mass activity and a comparable performance under a practical operating condition for micro-CHP applications, compared with the MEA using a commercial graphitized carbon black-supported platinum catalyst.
The experimental data enable precise determination of the switching loss in each device in a high-power converter at any practical operating condition.
At a typical practical operating condition, the forced-convection subcooled boiling phenomenon occurs in the cooling water circuit of the probe.
Global cross flows are a commonly encountered practical operating condition, particularly in the cooling of electronics.
Over a range of practical operating points, the separator showed very high collection efficiencies (>90%), low-pressure drop, and robust operation.
The composite catalysts (PtRu/C + metal oxide) are also used in a direct ethanol fuel cell under practical operating conditions and assessed against the benchmark PtRu catalyst.
Simulation of the model so formulated using the kinetic and physical parameters which are within the practical operating range, reveals that a substrate response minimum occurs in all the cases under consideration.
The gas cooled reactor faces with the problem of gas condensate formation and two phase flow in the practical operating conditions owing to a high temperature drop in the last 2 m of the reactor length.
