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Oil refineries frequently have both H_(2)S and SO_(2) to dispose of. The following reaction suggests a means of getting rid of both at once: 2H_(2)S(g)+SO_(2)(g)longleftrightarrow3S(s)+2H_(2)O(g)

Oil refineries frequently have both

H_(2)S

and

SO_(2)

to dispose of. The following reaction suggests a means of getting rid of both at once:\

2H_(2)S(g)+SO_(2)(g)longleftrightarrow3S(s)+2H_(2)O(g)

\ The feed to the reactor consists of

H_(2)S

and

SO_(2)

in their stoichiometric proportions; the reaction temperature is controlled at

450\\\\deg C

. Estimate the maximum mole fraction of

H_(2)O

in the product stream if the reactor pressure is\ a)1 bar\ b)

100 bar
image text in transcribed
Oil refineries frequently have both H2S and SO2 to dispose of. The following reaction suggests a means of getting rid of both at once: 2H2S(g)+SO2(g)3S(s)+2H2O(g) The feed to the reactor consists of H2S and SO2 in their stoichiometric proportions; the reaction temperature is controlled at 450C. Estimate the maximum mole fraction of H2O in the product stream if the reactor pressure is a) 1 bar b) 100bar Oil refineries frequently have both H2S and SO2 to dispose of. The following reaction suggests a means of getting rid of both at once: 2H2S(g)+SO2(g)3S(s)+2H2O(g) The feed to the reactor consists of H2S and SO2 in their stoichiometric proportions; the reaction temperature is controlled at 450C. Estimate the maximum mole fraction of H2O in the product stream if the reactor pressure is a) 1 bar b) 100bar

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