Recycle for supercritical carbon dioxide
A carbon dioxide and catalytic oxidation technology, applied in liquefaction, inorganic chemistry, carbon compounds, etc., can solve the problems of not specifying the system or method, and economic feasibility cannot be fully relied on, so as to reduce cost and complexity, reduce production cost, reduce cost effect
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[0048] Table 1 gives values corresponding to the flow conditions and compositions of the various material streams of the process shown in FIG. 4 . In this example, the expanded stream undergoes phase separation at reduced temperature in vessel 38 and is warmed to ambient temperature before entering first distillation column 46 . Impurities considered should include oxygen, nitrogen, methane (introduced with the added liquid), water, hexane, propylene carbonate, acetone and ethyl acetate. For these impurities, reactor 44 and heat exchanger 80 between columns 46 and 58 are not required. Furthermore, condensers 48 and 82 are preferably operated in the same unit.
[0049] The individual energy flows are listed in Table 2. The cooling power can be estimated based on the usage of the ammonia refrigeration loop. It can be assumed that this loop can power the reboilers 41 and 44 and that the cold water for condensing the high pressure ammonia vapor in the refrigeration loop is av...
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