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Anastasy [175]
3 years ago
11

A 0.50 molar aqueous solution of hydrochloric acid (HCl) flows into a process unit at 25°C and a rate of 1.25 m3/min. If the spe

cific gravity of the HCl solution is 1.03 at 25°C determine: a) HCl concentration in kg/m3 b) Mass flow rate in kg HCl/s c) MassfractioninkgHCl/kgsolution d) Mole ratio in mol HCl/mol water e) Molar flow rate in kmol HCl/s
Chemistry
1 answer:
Lerok [7]3 years ago
8 0

Answer:

a) 18,23 kgHCl/m³

b) 0,38 kg HCl/s

c) 0,018 kgHCl/kgsolution

d) 8,75x10⁻³ molHCl/molH₂O

e) 0,010 kmolHCl/s

Explanation:

The HCl solution is 0,50 mol/L; it flows in a rate of 1,25 m³/min; Its density is 1,03 kg/L. HCl weights 36,46 g/mol

a) The HCl concentration in kg/m³ is:

\frac{0,50molHCl}{L}×\frac{36,46gHCl}{mol}×\frac{1kg}{1000g}×\frac{1000L}{1m^3}= <em>18,23 kg HCl/m³</em>

b) As you have a concentration of 18,23 kgHCl/m³

\frac{18,23 kgHCl}{m^3}×\frac{1,25m^3}{min}×\frac{1min}{60s} = <em>0,38 kg HCl/s</em>

c) The mass fraction in kgHCl/kgsolution is:

\frac{18,23kgHCl}{m^3}×\frac{1m^3}{1000L}×\frac{1L}{1,03kg} = <em>0,018 kgHCl/kgsolution</em>

d) Supposing L of solution are just of water:

\frac{0,50 moleHCl}{Lsolution}×\frac{1L}{1,03kg}×\frac{1kg}{1000g}×\frac{18,02gH_{2}O}{1mole}= <em>8,75x10⁻³ molHCl/molH₂O</em>

<em>e) </em>As the flow is 0,38kg HCl/s:

\frac{0,38 kg}{s}×\frac{1kmole}{36,46kgHCl}= <em>0,010 kmolHCl/s</em>

I hope it helps!

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Answer:

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Explanation:

Hello,

In this case, the mass balance for each substance is given by:

Butane:z_bF=y_bD+x_bB\\\\Pentane: z_pF=y_pD+x_pB\\\\Hexane: z_hF=y_hD+x_hB

Whereas y accounts for the fractions at the outlet distillate and x for the fractions at the outlet bottoms. Moreover, with the 90 % recovery of butane, we can write:

0.9=\frac{y_bD}{z_bF}

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y_bD=0.9*z_bF=0.9*0.2*100mol=18mol

The total distillate flow:

y_bD=18mol\\\\D=\frac{18mol}{0.95} =18.95mol

And the total bottoms flow:

F=D+B\\\\B=F-D=100mol-18.95mol=81.05mol

Next, by using the mass balance of butane, we compute the molar fraction of butane at the bottoms:

x_b=\frac{z_bF-y_bD}{B} =\frac{0.2*100mol-18mol}{81.05} =0.025

Then, the molar fraction of pentane and hexane:

x_p=\frac{z_pF-y_pD}{B} =\frac{0.35*100mol-0.04*18.95mol}{81.05} =0.422

x_h=\frac{z_hF-y_hD}{B} =\frac{(1-0.2-0.35)*100mol-(1-0.95-0.04)*18.95mol}{81.05} =0.553

Therefore, the molar composition of the bottom product is 2.5 % butane, 42.2 % pentane and 55.3 % hexane.

NOTE: notice the result is independent of the value of the assumed feed, it means that no matter the basis, the compositions will be the same for the same recovery of butane at the feed, only the flows will change.

Regards.

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