Question

The cyclization reaction of acetylene to benzene occurs at approximately 400°C and 4 atm. Gaseous acetylene...

The cyclization reaction of acetylene to benzene occurs at approximately 400°C and 4 atm. Gaseous acetylene is fed to the reactor at a rate of 20 L/min STP along with an equal amount of nitrogen. The stream exiting the reactor is at the same conditions as the reactor and has a volumetric flow rate of 21.4 L/min. This stream is sent to a condenser where it is cooled to 25°C (still at 4 atm), here only the benzene partially condenses. Assume that all gas streams can be treated ideally. a) Draw and label a flowchart for this system. b) Is this ideality assumption valid? Prove this. c)What is the reaction conversion? d) What is the flow rate of the benzene product stream from the condenser?

Homework Answers

Answer #1

The reaction is 3C2H2 --à C6H6

Moles of Acetylene= PV/RT= 20*4/(0.0821*(400+273.15) =1.45 moles/min

Moles of nitrogen = 1.45 moles/min

Since all the Acetylene gets reacted, moles of Benzene= 1.45/3= 0.483 moles/min

Nitrogne does not participate in the reaction, moles of product= Benzene+ moles of Nitrogen= 0.483+1.45 =1.933 moles/min

Volume of this gas at 400 deg. c and 4 atm, V= nRT/P

1.933*0.0821*673.15/4=26.66 Lits/min but the given volume is onlyy 21.4 L/min suggesting at these conditions gas law is not valid.

Moles of product formed ( assumig gas law is valid)= 21.6*4/ (0.0821*673.15)= 1.563 moles/min

Nitrogen = 1.45 moles/min remaining is Benzene= 1.563-1.45=0.113 moles/min

Moles of C2H2 reacted= 0.113*3= 0.339 moles/min

Moles supplled= 1.45 moles/min

Conversion = 100*0.339/1.45=23.38%

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
8- The mass flow rate of the first gaseous feed stream, containing the component I only...
8- The mass flow rate of the first gaseous feed stream, containing the component I only , is 6,000 g\s .The total volumetric flow rate of the second gaseous feed stream, containing 67w%A and 33 wt%B,is 8,000 liter/s at 15 atm and 300k. These two gaseous feed streams are mixed and combined ,and then the combined gaseous feed stream is fed into a flow reactor at 420 k and 10 atm. All the componets are assumed to be ideal gases....
Solids soaked with liquid hexane are dried by being contacted with nitrogen at an elevated temperature....
Solids soaked with liquid hexane are dried by being contacted with nitrogen at an elevated temperature. The gas stream leaving the dryer is at 80°C, 1 atm absolute and 50% relative saturation. (a) One of several possibilities for recovering the hexane from the gas is to send the stream to a cooling condenser. The gas stream leaving the condenser would contain 5.00 moles of hexane (out of 100 total moles), and hexane condensate would be recovered at a rate of...
Pure gaseous A at about 3 atm and 30°C (120 mmol/liter) is fed into a 1-liter...
Pure gaseous A at about 3 atm and 30°C (120 mmol/liter) is fed into a 1-liter mixed flow reactor at various flow rates. There it decomposes via A ?3R, and the exit concentration of A is measured for 20 each flow rate. From the following data find a rate equation to represent the kinetics of the decomposition of A. Assume that reactant A alone affects the rate. Q liter/min 0.06 0.48 2.5 8.1 CA mmol/liter 30 60 80 105 3.2....
A gas stream contains 40 mol% n-hexane in nitrogen (N2) and flows at 6600 L/min, 60◦C,...
A gas stream contains 40 mol% n-hexane in nitrogen (N2) and flows at 6600 L/min, 60◦C, and 1 atm from a soybean oil extraction process. You are to use a condenser to liquefy and recover nhexane to recycle back to the oil extraction process. The current process specifications call for the condenser to operate at 15◦C. A liquid condensate stream is produced that is in equilibrium with the exiting gas stream. (a) (15) Perform a degree-of-freedom (DoF) analysis to demonstrate...
he elementary liquid-phase reaction: A + B -----> C is to be carried out non-isothermally in...
he elementary liquid-phase reaction: A + B -----> C is to be carried out non-isothermally in a flow system with reaction constant,k= 0.07 dm^3mol-1min-1at 300K. The concentrations of each feed stream of A and B is 2 mol dm-3. The volumetric flow rate of each feed stream is 5 dm^3min-1. The two steams are mixed immediately prior to entering the reactor system. This flow system is conducted at 300K with two reactors: a 200 dm^3 stainless steel CSTR and an...
ADVERTISEMENT
Need Online Homework Help?

Get Answers For Free
Most questions answered within 1 hours.

Ask a Question
ADVERTISEMENT