$C_H=1\mathrm{.}34{10}^{-2}\sqrt[\phantom{2}]{P{H}_2}$exp$(-\frac{27\mathrm{.}2K\frac{J}{m}ol}{R}T)$

$--$Given Values$-$

$-$Given Values$--$ Membrane Thickness $(mm)=4\mathrm{.}4$

Membrane Thickness $(mm)=$ Temperature in Celsius $=384$

Part A:

What is the concentration of hydrogen at the low $-$ pressure $($or B$)$ side in w $\%?$ Write your answer in Engineering Notation.

Your Answer

Incorrect.

Part B:

What is the concentration of hydrogen at the low $-$ pressure $($or A$)$ side in w $\%?$ Write your answer in Engineering Notation.

Your Answe

Incorrect.

Part C:

What is the concentration of hydrogen at the B face in kilograms of $H$ per cubic meter $($Density for Hydrogen is $7\mathrm{.}87\frac{g}{c}{m}^3)?$ Write your answer in Engineering Notation.

Your Answer $=$

Incorrect.

Part D:

What is the concentration of hydrogen at the A face in kilograms of $H$ per cubic meter$($Density for Hydrogen is $7\mathrm{.}87\frac{g}{c}{m}^3??$ Write your answer in Engineering Notation.

Your Answer

$|$Incorrect$.$

Part E:

What is the concentration gradient $(\frac{C}{x})$ in $k\frac{g}{m^4}?$ Write your answer as positive to the thousandth place.

Your Answer $=-15*4$

$|$Incorrect$.$

Part F:

Calculate the diffusion coefficient, $D,$ in $\frac{m^2}{s}$ at the specified temperature. Write your answer in Engineering Notation

Your Answer $=45\mathrm{.}94$

$]$ Incorrect.

Part G:

Compute the diffusion flux in $k\frac{g}{m^2}-s.$ Write your answer in Engineering Notation

Your Answer $=0\mathrm{.}5193E$

Incorrect.