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Troyanec [42]
3 years ago
6

The first order, reversible reaction A<--> B + 2C is taking place in the membrane reactor. Pure A enters and B diffuses th

rough the reactor. Unfortunately, some of the reactant A also diffuses through the membrane.
A. Plot and analyze the flow rates of A, B and C down the reactor, as well as the flow rates of A and B through the membrane.

B. Compare the conversion profiles of a conventional PFR with those of a membrane reactor. What generalizations can you make?

C. Would the conversion of A be greater or smaller if C were diffusing instead of B?

D. Discuss qualitatively how your curves would change if the temperature were increased significantly or decreased significantly for an exothermic reaction. Repeat for an endothermic reaction.

Additional Info:

k= 10min-1

KC=0.01mol2/dm6

kCA=1min-1

kCB=40min-1

FA0=100mol/min

v0 = 100dm3/min

VReactor=20dm3

Please note that this problem only needs you to set up the system of equations, supporting equations, parameters and B.C's for ODE or equivalent solver.
Engineering
1 answer:
fomenos3 years ago
4 0
The answer is I need the points sorry
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The regulated voltage of an alternator is stated as 13.6 to 14.6 volts at 3000 rpm with the
lions [1.4K]

Answer:

  d)  1 volt​

Explanation:

The allowable range is 1 volt​. The allowed tolerance (deviation from nominal) depends on what the nominal voltage is.

5 0
4 years ago
4. A 25 km2 watershed has a time of concentration of 1.6 hr. Calculate the NRCS triangular UH for a 10-minute rainfall event and
Alika [10]

Answer:

The NRCS triangular UH for a 10-minute rainfall is Qp = 49.84 m³/s

Peak flow of the aggregated runoff hydrograph is 420.58 m³/s

The total volume of runoff is 2125000 m³/s

Explanation:

We have

A = 25 km²

tr = 10 min = 1/6 hr

tc = 1.6 hr

lag time = 0.6 tc = 0.96 hr

Tp = tr/2 + 0.6 tc = 1/12 + 0.96 = 1.043 hr

Qp = 2.08×25/1.043 = 49.84 m³/s

Tb = 8/3×Tp = 8/3×1.043 = 2.782 hr

 

Since the area is  

Time (min)           Runoff (cm)       Volume of runoff m³

0                   0                                     0

10                  4                                     1000000 m³

20                 2.5                                  625000 m³

30                 2                                      500000 m³

Total volume of runoff = 1000000 + 625000 + 500000 =  2125000 m³/s

For the 1st  10 minutes, we have

A = 25 km²

tr = 30 min = 1/2 hr

tc = 1.6 hr

lag time = 0.6 tc = 0.96 hr

Tp = tr/2 + 0.6 tc = 1/4 + 0.96 = 1.21 hr

Qp = 2.08×25×4/1.043 = 197.92 m³/s

Tb = 8/3×Tp = 8/3×1.21 = 3.227  hr

 

For the 2nd 10 minutes, we have

A = 25 km²

tr = 30 min = 1/2 hr

tc = 1.6 hr

lag time = 0.6 tc = 0.96 hr

Tp = tr/2 + 0.6 tc = 1/4 + 0.96 = 1.21 hr

Qp = 2.08×25×2.5/1.043 = 123.7 m³/s

Tb = 8/3×Tp = 8/3×1.21 = 3.227  hr

For the 3rd 10 minutes, we have

A = 25 km²

tr = 30 min = 1/2 hr

tc = 1.6 hr

lag time = 0.6 tc = 0.96 hr

Tp = tr/2 + 0.6 tc = 1/4 + 0.96 = 1.21 hr

Qp = 2.08×25×2.5/1.043 = 98.96 m³/s

Tb = 8/3×Tp = 8/3×1.21 = 3.227  hr

 

Peak flow of aggregate runoff is given by

Qp (total) = 98.96 + 123.7 +197.92 = 420.58 m³/s

Total volume of runoff is given by

Total volume of runoff = 1000000 + 625000 + 500000 =  2125000 m³/s

6 0
4 years ago
Power cords can be damaged by Which of the following?
Elena L [17]
What are the options??
3 0
3 years ago
Compute the volume percent of graphite, VGr, in a 3.9 wt% C cast iron, assuming that all the carbon exists as the graphite phase
kicyunya [14]

Answer:

Vgr = 0.122 = 12.2 vol %

Explanation:

Density of ferrite = 7.9 g/cm^3

Density of graphite = 2.3 g/cm^3

<u>compute the volume percent of graphite </u>

for a 3.9 wt% cast Iron

W∝ =  (100 - 3.9) / ( 100 -0 ) = 0.961

Wgr = ( 3.9 - 0 ) / ( 100 - 0 ) = 0.039

Next convert the weight fraction to volume fraction using the equation attached below

Vgr = 0.122 = 12.2 vol %

6 0
3 years ago
The velocity of the 7.7-kg cylinder is 0.49 m/s at a certain instant. What is its speed v after dropping an additional 1.28 m? T
alex41 [277]

Answer:

the velocity of the cylinder after dropping an additional 1.28 m is 1.15 m/s

Explanation:

Using the work energy system

T_1 + U_{1-2} + T_2

The initial kinetic energy T_1 is ;

T_1 = \dfrac{1}{2}m_cv_1^2 + \dfrac{1}{2}I_o \omega^2

T_1 = \dfrac{1}{2}m_cv_1^2 + \dfrac{1}{2}(m_d \overline k^2)(\dfrac{v_1}{r_i})^2

where;

m_c = mass of the cylinder = 7.7 kg

v_1 = initial velocity of the cylinder = 0.49 m/s

I_o= moment of inertia of the drum about O

m_d =mass of the drum = 10.5 kg

r_i = radius of gyration = 0.3 m

\omega = angular velocity of the drum

T_1 = \dfrac{1}{2}(7.7)(0.49)^2 + \dfrac{1}{2}(10.5*(0.3)^2(\dfrac{0.49}{0.275})^2

T_1 = 2.426 \ J\\

The final kinetic energy is also calculated as:

T_2= \dfrac{1}{2}m_cv_2^2 + \dfrac{1}{2}(m_d \overline k^2)(\dfrac{v_2}{r_i})^2

T_2= \dfrac{1}{2}(7.7)(v_2^2)^2 + \dfrac{1}{2}(10.5*(0.3)^2(\dfrac{v_2}{0.275})^2

T_1 =10.10 v_2^2

Similarly, The workdone by all the forces on the cylinder can be expressed as:

U_{1-2} = m_cg(h) - (\dfrac{M}{r_i})h

where;

g = acceleration due to gravity

h = drop in height of the cylinder

M = frictional moment at O

U_{1-2} = 7.7*9.81*1.28 - 18.4(\dfrac{1.28}{0.275})

U_{1-2} =11.04 \ J

Finally, using the work energy application;

T_1 + U_{1-2} + T_2

2.426 + 11.04 = 10.10 v_2^2

13.466 = 10.10 v_2^2

v_2^2 = \dfrac{13.466}{10.10}

v_2^2 = 1.333

v_2 = \sqrt{1.333}

v_2 = 1.15 \ m/s

Thus, the velocity of the cylinder after dropping an additional 1.28 m is 1.15 m/s

8 0
3 years ago
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