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Supercritical fluid technology safety

Supercritical fluid technology is potentially hazardous and should not be used by "beginners" is very often, home-designed and home-made equipments do not incorporate all the safety levels that are required, according to us moreover, it is extremely important that operators be trained by specialists prior to work on supercritical fluid equipments. [Pg.631]

An exhaustive search for new propellants was made at the time of the switch away from CFCs, and it is unlikely that new ones will be found with the necessary physicochemical properties combined with an excellent safety profile. New surfactants are possible, but there is the major cost hurdle of drug toxicity studies to NCE standards. Particle engineering may provide benefits, e.g., production by supercritical fluid technology. [Pg.371]

Ultimately, chemical engineering methods and technology are needed to transform this molecular and empirical chemistry into a real process. This chemistry must be understood in terms of many scale-up, design and simulation issues that will influence the economics of the process. For example, process equipment and operating procedures in supercritical fluids require special attention to safety issues because of the high pressures involved. There is an economic penalty in achieving the compression required to reach operating pressures and to recover products at ambient conditions. Sometimes extensive pretreatment of feeds is required or a specialized co-solvent may have to be added. [Pg.288]

While hexane is widely accepted as the most effective solvent used today, there are concerns about its flammability, exposure, and environmental impacts. Research has focused on various alternative solvents in the hopes of finding one with acceptable performance while providing greater safety. Alternative solvents that have received some attention include isopropyl alcohol, supercritical carbon dioxide, and other fluids. However, no economical alternative to n-hexane has been accepted at this point, and the best available control technology emphasizes containment and limiting fugitive hexane emissions. [Pg.2425]

Phase Equilibria. From recent research (Schneider and Peters) it became apparent that in the near-critical region of certain ternary carbon dioxide mixtures, due to co-solvency effects of the two solutes relative to each other, the fluid multiphase behavior can be quite complex. Phenomena like immiscibility windows and holes are not unusual, which have their consequences for separations in near-critical processing. Peters stressed that for many applications in supercritical technology carbon dioxide is not an appropriate choice since for many solutes it is a poor solvent that would require the use of a cosolvents. If safety and environmental constraints permit, it is certainly worthwhile to consider alternatives for carbon dioxide. Gulari, Schneider and Peters emphasized the importance of studying representative model systems in order to obtain insight into the systematic variations of the complex phase behavior that may occur in near-critical multicomponent mixtures. Debenedetti stressed the importance of focusing on complex fluids like emulsions. [Pg.561]


See other pages where Supercritical fluid technology safety is mentioned: [Pg.686]    [Pg.242]    [Pg.258]    [Pg.1075]    [Pg.81]    [Pg.316]    [Pg.867]    [Pg.159]    [Pg.160]    [Pg.395]    [Pg.67]    [Pg.84]    [Pg.190]    [Pg.566]    [Pg.297]    [Pg.171]    [Pg.53]   
See also in sourсe #XX -- [ Pg.2919 ]




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