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In this work, we report an optimal design strategy for another DR-PSA process cycle configuration: feed to low pressure bed and pressure swing using heavy gas.
The effect of operational parameters such as temperature, pressure, bed porosity and mean particle diameter of dried plant were investigated in this process by a statistical approach.
In the grouting process, the selection of the physical forms of fly ash as grouting material is based on factors including grouting pressure, bed separation volume, and slant angle of the coal seam.
Systematic parametric study of the effect of jacket temperature, head-space pressure, bed depth, and gas- and liquid-phase relative permeability has been performed.
Four operating parameters, including the water content, suction pressure, bed height, and type of hearth layer, were selected and all experimental campaigns were conducted on a pilot-scale sinter pot to simulate various sintering operating conditions of a real-scale sinter plant.
[A5] "they just send them anywhere they can to get them out of [the regional hospital]…they have to get them out of there… you know within four days....[because of] funding, pressure, bed block … pressure to get them out, get them going, send them home".
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The SARS isolation unit required negative pressure beds.
Admissions to negative pressure beds were decided case-by-case and were based on the assessment of the referring physician, the hospital's infectious disease representative, and the hospital intensivist.
Feed to the high-pressure bed and equalisation, pressurisation and blowdown with the strongly adsorbed component is favoured at low concentrations of heavy component in the feed gas.
Feed to the low-pressure bed and equalisation, pressurisation and blowdown with weakly adsorbed component is favoured for high concentrations of heavy component in the feed gas.
Within the constraint of DR-PSA, there are several options: feed to the low- or high-pressure bed and equalize, repressurize and blowdown with either the weakly or strongly adsorbed gas (opposite ends of the adsorption column).
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