Question

In a production plant of sulphuric acid a catalytic converter is used to perform the oxidation...

In a production plant of sulphuric acid a catalytic converter is used to perform the oxidation reaction of SO2 to SO3. Given the exothermic nature of the process, the converter is made of 4 beds in series (each bed works as an independent reactor). In the first bed, a stream containing 5% of SO2, 12% of O2, 2% of water (vapor) and the balance of nitrogen (N2) is fed. The first bed has a conversion of 71% with respect to the SO2 fed to the bed. The resulting gases leave Bed 1 and go through a cooling device before they are fed to Bed 2. Bed 2 has a 77.3% conversion of the SO2 fed to this bed. Similarly, the product gases of Bed 2 go through a heat exchanger to decrease their temperature and then are introduced to the third catalytic bed where there is a 45.6% conversion of the incoming SO2 fed to this bed. Finally, the cooled gases are fed to the last bed where there is a 20.8% conversion.

a) Draw the flow diagram and the reaction that takes place

b) Find the flow and composition of every stream considering that 10,000 mol/h of gases are fed to Bed 1

c) Find the overall conversion of SO2

Homework Answers

Know the answer?
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for?
Ask your own homework help question
Similar Questions
It is from the book Elementary Principles of Chemical Processes, 4th Edition, Problem 5.66 The quantity...
It is from the book Elementary Principles of Chemical Processes, 4th Edition, Problem 5.66 The quantity of sulfuric acid used globally places it among the most plentiful of all commodity chemicals. In the modern chemical industry, synthesis of most sulfuric acid utilizes elemental sulfur as a feedstock. However, an alternative and historically important source of sulfuric acid was the conversion of an ore containing iron pyrites (FeS2) to sulfur oxides by roasting (burning) the ore with air. The following reactions...
Benzaldehyde is produced from toluene in the catalytic reaction C6H5CH3 + O2 ? C6H5CHO + H2O...
Benzaldehyde is produced from toluene in the catalytic reaction C6H5CH3 + O2 ? C6H5CHO + H2O Dry air and toluene vapor are mixed and fed to the reactor at 350.0°F and 1 atm. Air is supplied in 100.0% excess. Of the toluene fed to the reactor, 13.0% reacts to form benzaldehyde and 0.100% reacts with oxygen to form CO2 and H2O. The product gases leave the reactor at 379°F and 1 atm. Water is circulated through a jacket surrounding the...
A laboratory scale packed bed reactor (PBR) with catalytic particles is used to make experimentswith an...
A laboratory scale packed bed reactor (PBR) with catalytic particles is used to make experimentswith an irreversible 1st order gas phase reaction A → product at 500 K. The rate constant forthe reaction, determined by conditions where mass transport resistance could be neglected, is found to k '= 1,6237 m3/kcat S . The particles are spherical with a diameter of D = 2 mm and onedensity of 1200 kg / m3. Radius R=1x10-3 Thiele modul Ø=44,141 4.2 The product formed...
Task # 4 A laboratory scale packed bed reactor (PBR) with catalytic particles is used to...
Task # 4 A laboratory scale packed bed reactor (PBR) with catalytic particles is used to make experimentswith an irreversible 1st order gas phase reaction A → product at 500 K. The rate constant forthe reaction, determined by conditions where mass transport resistance could be neglected, is found tok '= 7E15 exp (-18000 / T) m3 / (kgcat s). The particles are spherical with a diameter of D = 2 mm and onedensity of 1200 kg / m3. 4.2 The...
Ethylene oxides is produced by the catalytic oxidation of ethylene: C2H4 (g)+ (1/2)O2---> C2H4O (g) An...
Ethylene oxides is produced by the catalytic oxidation of ethylene: C2H4 (g)+ (1/2)O2---> C2H4O (g) An undesired competing reaction is the combustion of ethylene to CO2. The feed to a reactor contains 2 mol C2H4/mol O2. The conversion and yield in the reactor are respectively 25% and 0.70 mol C2H4O produced/mol C2H4 consumed. A multiple-unit process separates the reactor outlet stream component: C2H4 and O2 are recycled to the reactor, C2H4O is sold, and CO2 and H2O are discarded. The...
Task # 4 A laboratory scale packed bed reactor (PBR) with catalytic particles is used to...
Task # 4 A laboratory scale packed bed reactor (PBR) with catalytic particles is used to make experimentswith an irreversible 1st order gas phase reaction A → product at 500 K. The rate constant forthe reaction, determined by conditions where mass transport resistance could be neglected, is found to k '= 7E15 exp (-18000 / T) m3 / (kgcat s). The particles are spherical with a diameter of D = 2 mm and onedensity of 1200 kg / m3. 4.1...
Reactions 1-4 below describe the industrial process used to synthesize sulfuric acid starting from sulfur, oxygen...
Reactions 1-4 below describe the industrial process used to synthesize sulfuric acid starting from sulfur, oxygen gas, and water. Reaction 1:    S(s) + O2(g) → SO2(g) Reaction 2: 2 SO2(g) + O2(g)  → 2 SO3(g) Reaction 3: H2SO4(l) + SO3(g) → H2S2O7(l) Reaction 4: H2S2O7(l) + H2O(l) → 2 H2SO4(l) Overall Reaction (1-4): 2 S(s) + 3 O2(g) + 2 H2O(l) → 2 H2SO4(l) A. The industrial production of sulfuric acid involves proper control of temperatures and flow rates of...