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Design diffusion coefficients are computed from the total chloride concentration curve of actual structures, which can be different from the experimental data obtained from the laboratory.
This chapter describes mathematical models for the design of basic batch and continuous reactors; the design of aerobic activated-sludge process; the mass transfer and diffusion correlations needed for design; diffusion through landfill; and diffusion of airborne pollutants.
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Designing diffusion tensor D is crucial to the diffusion process.
These plots may help in making trade-off decisions when designing diffusion imaging protocols.
Experiments based on an ad-hoc designed Diffusion Weighted T1−T2 pulse sequence have demonstrated that muscle and cartilage signals can be suppressed by using diffusion weighting.
This method was based on the use of a specifically designed diffusion cell where iodide was used as a soluble tracer.
Before establishing the model, some mass transfer experiments of thin film were conducted in a designed diffusion cell including vacuum and feeding system.
For some special BOF blowing technologies, such as steelmaking with high phosphorus hot metal, post combustion oxygen lance, hot metal pretreatment, etc, the difference between working oxygen pressure and designed diffusion pressure which is related to Mach-number is necessary, so that the velocity of the oxygen jet will be decreased because of shock wave for expected metallurgical results.
Diffusion, or Brownian motion, of tissues can be measured using specially designed diffusion-weighted imaging (DWI) sequences.
An obvious corollary here is that other properly designed diffusion-controlled matrix ASD systems in principle should exhibit advantageous kinetic solubility profiles and maintenance of supersaturation similar to that of the present hydrogel ASD system.
The design screams diffusion line.
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