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Two containers are connected by stopcock as shown. If initially P_(O_(2))=P_(He)=P when stopcock is closed. Then after opening the stopcock (alter a long time keeping initial temperature in each same as initially). |
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Answer» <P>`P_("final")=P` `n'_(1)+n'_(2)=n_(1)+n_(2)` `(P_(f)xx10)/(Rxx300)+(P_(f)xx20)/(Rxx600)=(Pxx10)/(300R)+(Pxx20)/(600R)` For `O_(2) & He` before MIXING `(P_(O_(2))V_(O_(2)))/(n_(O_(2))T_(O_(2)))=(P_(He)V_(He))/(n_(He)T_(He))` `T=T_(He)=600K` For `O_(2)` in `1^(st)` container and `2^(nd)` container its MOLE distribution `(Pxx10)/(Pxx20)=((n_(O_(2)))_(1)xxRxx300)/((n_(O_(2)))_(2)xxRxx600)` `(n_(O_(2)))_(1)=(n_(O_(2)))_(2)=(X)/(2)` Similarily `(n_(O_(2)))_(1)=(X)/(2)` Partial pressure of `O_(2)` in any container `P_(O_(2))=x_(O_(2))P_("total")` `P_(O_(2))=(X//2)/(X)P=(P)/(2)` Partial pressure of He in any container `P_(He)=P-P_(O_(2))=(P)/(2)` T=600K A,B,D |
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