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Plant transport system vapor pressure

In solvent recovery plants, temperature-swing processes are most frequently used. The loaded adsorbent is direct heated by steam or hot inert gas, which at the same time serves as a transport medium to discharge the desorbed vapor and reduce the partial pressure of the gas-phase desorpt. As complete desorption of the adsorpt cannot be accomplished in a reasonable time in commercial-scale systems, there is always heel remaining which reduces the adsorbent working capacity. [Pg.1513]

Results from MELCOR (Version 1.8.0) calculations of three accident sequences in a W-PWR 900 Mwe three loop plant are presented. The scenarios considered include an AB sequence and two V type events a rupture of the Low Pressure Coolant Injection System in the auxiliary building, and the rupture of ten steam generator tubes in all cases without the intervention of the active emergency core cooling systems. Emphasis is put on the release and transport of core materials. It has been found that deposition of vapors from the most volatile species is high within the core structures. Later in the accident, revaporization induced by decay heat takes place, at times in coincidence with the production of steam due to core slumping, what may change the nature and composition of source terms. [Pg.401]


See other pages where Plant transport system vapor pressure is mentioned: [Pg.475]    [Pg.604]    [Pg.480]    [Pg.9]    [Pg.20]    [Pg.480]    [Pg.480]    [Pg.582]    [Pg.442]   
See also in sourсe #XX -- [ Pg.248 ]




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Plant system

Plant transport system

Plants transport

Pressure systems

Pressurizing system

Systemic Transport

Transport systems

Transport systems/transporters

Vapor pressure systems

Vapor system

Vapor transport

Vaporizers system

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