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Model vacuum distillation unit

Well over 50 large-scale EO model-based RTO applications have been deployed for petroleum refining processes. These model applications have been deployed in petroleum refineries Liporace et al., 2009 Camolesi et al., 2008 Mudt et al., 1995, both on separation units (crude atmospheric and vacuum distillation units) and on reactor units (including fluidized catalytic crackers (FCC), gasoline reformers, and hydrocrackers). [Pg.134]

A mixture of 2-iodotoluene (8.78 g, 0.04 mol) and trimethyl phosphite (24.8 g, 0.20 mol) was placed in a 45-ml, double-jacketed silica reaction vessel. The mixture was degassed by flushing with dry nitrogen for 5 min and irradiated with a 450-watt Hanovia (Model 679A-10) high-pressure quartz mercury vapor lamp fitted with an aluminum reflector head. The lamp was placed 5 cm from the inner portion of the reaction vessel. The reaction temperature was maintained at 0°C by the circulation of coolant from a thermostatically controlled refrigeration unit. Irradiation was continued at this temperature for 24 h. At the end of this time, the volatile materials were removed with a water aspirator, and the residue was vacuum distilled (96 to 97°C/0.25 torr) to give the dimethyl 2-methylphenylphosphonate (7.28 g, 91%). [Pg.179]


See other pages where Model vacuum distillation unit is mentioned: [Pg.132]    [Pg.117]    [Pg.511]    [Pg.513]    [Pg.31]    [Pg.74]    [Pg.515]    [Pg.217]    [Pg.76]    [Pg.66]    [Pg.30]    [Pg.217]    [Pg.1661]    [Pg.66]    [Pg.71]    [Pg.124]   
See also in sourсe #XX -- [ Pg.124 , Pg.135 ]




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