Question

In: Other

The following data are obtained at 0°C in a constant-volume batch reactor using pure gaseous Time,...

The following data are obtained at 0°C in a constant-volume batch reactor using pure gaseous

Time, min

0

2

4

6

8

10

12

14

Partial pressure of A, mm Hg

760

600

475

390

320

275

240

215

150

The stoichiometry of the decomposition is A → 2.5 R. Find a rate equation which satisfactorily represents this decomposition.

Solutions

Expert Solution

The reaction is given as,

The rate of a reaction can be written as,

Where is the rate constant.

In terms of partial pressure of we can write,

So ,

Taking ln on both sides we can see,

This means that if we draw a graph of vs we will get a graph of slope and a y axis intercept of

So for finding , first we have to draw the graph of vs from the data given above,

We will do it in excel,

So adding the trendline we got the equation as for   vs as,

So, we can find as,

Now we will draw the graph of   vs ,

Now the equation can be written as,

Comparing both the equations we get,

and,

So the rate equation can be written as,

The temperature is given as,

So the rate equation can be written as,

Here is in mmHg and is in


Related Solutions

In a constant volume batch reactor, enzyme E catalyzes the transformation of reactant A to product...
In a constant volume batch reactor, enzyme E catalyzes the transformation of reactant A to product R as follows: A -----> R The rate of consumption of A is given as rA= 200CACE/(2 + CA) (mol/l min). If we introduce enzyme with an initial concentration of 0.001 mol/l and reactant with an initial concentration of CA0=10 mol/l into a constant volume batch reactor and let the reaction proceed, find the time needed for the concentration of reactant to drop to...
The reaction A + 2B  C + D is taking place in a batch reactor....
The reaction A + 2B  C + D is taking place in a batch reactor. (Cao =1M, Cbo = 3M k=0.001 (1/M^2*min)). a) Assuming an elementary rate law, find the time necessary to reach the conversion of 0.9. You can assume constant volume batch reactor with well mixing. Also form the stoichiometric table. (15 points) b) Sometimes it is hard to obtain numerical solutions to the complex integrals. Find the answer using trapezoidal, Simpson 1/3 and Simpson 3/8, Five-point...
Consider an irreversible 2nd-order reaction (A + B → C) in a batch reactor with the...
Consider an irreversible 2nd-order reaction (A + B → C) in a batch reactor with the initial molar ratio of ΘB=CB0/CA0. Find the relation between time (t) and conversion (XA). (Hint: You need to consider cases of both CA=CB and CA≠CB.)
The following reversible gas-phase reaction is carried out in a 10 L batch reactor. A <->C...
The following reversible gas-phase reaction is carried out in a 10 L batch reactor. A <->C -rA = CA – 0.5CC [mol/(L h)] Determine the pressure, temperature, and gas phase composition (mole fractions) in the reactor after 1 hour of operating adiabatically given the following initial conditions and physical properties and the assumption of ideal gas behavior: P0 = 100 kPa, yA0 = 0.5, yC0 = 0.1, yinert=0.4, T0 = 500 K. cpA = cpC = 10 J/mol K, cpinert...
The following reactions take place in a batch reactor: A+B--> C (desired product) B+C-->D (hazardous product)...
The following reactions take place in a batch reactor: A+B--> C (desired product) B+C-->D (hazardous product) As the reaction proceeds, D builds up in the reactor and could cause an explosion if its concentration exceeds 15 mol/L. To ensure the safety of the plant personnel, the reaction is quenched (e.g., by cooling the reactor contents to a low temperature) and the products are extracted when the concentration of D reaches 10mol/L. The concentration of C is measured in real-time, and...
The following data were obtained from a batch experiment for the reaction where A is converted...
The following data were obtained from a batch experiment for the reaction where A is converted to B. 1)Determine the order of the reaction             Time (min)      0           10        20        40        60        80        100             A (mg/lit)        100      74        55        30        17        9          5 2) Consider a first order reaction taking place in a batch reactor. Develop an expression for the detention time in the reactor.
Determine the reaction order and the rate constant for the following data set: Time (s) 0...
Determine the reaction order and the rate constant for the following data set: Time (s) 0 50 100 150 200 250 Concentration (M) 0.01000 0.00887 0.00797 0.00723 0.00662 0.00611
[BI A 30kVA, 3000/1 1 0 V transfomier, the following experimental data was obtained: 0.C test:...
[BI A 30kVA, 3000/1 1 0 V transfomier, the following experimental data was obtained: 0.C test: 3000 V, 0.5 A, 350 W S.C test: 150 V, 10 A, 500 W Calculate (a) the efficiency at full load, 0.8p.f. (b) the kVA output at which the efficiency is ma)cimum (comment on the obtained resu]ts)f 1 5 Marks]
Experiment data taken in a batch reactor predicted the CSTR conversion should be 50%. However, the...
Experiment data taken in a batch reactor predicted the CSTR conversion should be 50%. However, the concentration measured in the actual CSTR was 57%. Suggest a reason for the discrepancy between the predicted and measured conversion.
For each of the following functions, does a constant c > 0 exist such that the...
For each of the following functions, does a constant c > 0 exist such that the function is a joint probability density function? If yes, what is c? If not, why not? Part (a) gives 2 points, parts (b)–(d) give each one point. (a) f(x, y) = ( cxye −x−2y if x ≥ 0 and y ≥ 0, 0 otherwise. (b) f(x, y) = ( cxye −x−2y if x ≥ −1 and y ≥ 1, 0 otherwise. (c) f(x, y)...
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT