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With CO2 in feed gas

This chapter describes P catalyst bed calculations with SO3 and CO2 in feed gas. Its objectives are to show how ... [Pg.189]

Intercept temperature decreases slightly with increasing CO2 in feed gas. Intercept % SO2 oxidized increases slightly. [Pg.157]

Table R.l First catalyst bed intercept calculations with SO and CO2 in feed gas... [Pg.442]

The experimental results are summarized in Table 2. CO2 permeance (Rco2), selectivity (oicx)2/N2) and CO2 recovery (Y) increased with decreasing CO2 mole fraction in feed gas. CO2 in the feed gas was successfully concentrated to 97-99 % by the single-stage operation. CO2... [Pg.410]

Another interesting aspect of Fig. 7.10 is that the permeance increases with decreasing CO2 partial pressure at any given temperature which is due to the fact that at higher feed pressures, the membrane is saturated with adsorbed CO2 (in the form of the surface carbamate species) which could either inhibit the surface transport process and/or block the CO2 in the gas phase while at lower partial pressures, the membrane is not totally saturated with CO2, and thus, it has a greater driving force within the pores or available active sites (amines) to hop from one amine strand to another. [Pg.234]

Table R.I. 1 catalyst bed intercept calculations with SOi and CO in feed gas. Note the 2 new CO2 columns, new input CO2 and C balance rows and 2 new CO2 result rows. The use of Eqn (17.1) in cell A14 is notable. Cells D28-H28 contain -H° values. Cells I28-M28 contain H° values. [Pg.359]


See other pages where With CO2 in feed gas is mentioned: [Pg.194]    [Pg.358]    [Pg.194]    [Pg.359]    [Pg.194]    [Pg.441]    [Pg.467]    [Pg.360]    [Pg.228]    [Pg.315]    [Pg.320]    [Pg.506]    [Pg.459]    [Pg.221]    [Pg.117]    [Pg.362]    [Pg.2017]    [Pg.422]    [Pg.607]    [Pg.892]    [Pg.906]    [Pg.363]   
See also in sourсe #XX -- [ Pg.194 , Pg.312 ]




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