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Ammonia (NH_3) is produced from hydrogen and nitrogen according to the following

ID: 490388 • Letter: A

Question

Ammonia (NH_3) is produced from hydrogen and nitrogen according to the following reaction: 3H_2 + N_2 - 2NH_3 The fresh feed to the process contains hydrogen, nitrogen, and argon. The reactor effluent contains 200 mol H_2/S, 150 mol N_2/S, 1 mol Ar/s, and 75 mol NH_3/s. After the reactor, all of the ammonia is condensed and all of the gases (H_2, N_2, and Ar) leave the top stream from the condenser. Five percent of this stream is purged from the process and the rest is recycled and mixed with the fresh feed. Determine the composition of the purge stream. Determine the molar flow rate of each component in the reactor feed. Calculate the single-pass conversion of the limiting reactant. Determine the molar flow rate of each component in the process fresh feed. Calculate the overall conversions of both hydrogen and nitrogen. Suppose that the process is scaled up until the mass flow rate of ammonia production is 100 000 kg/h. What would the required fresh freed of H_2 be in kg/h?

Explanation / Answer

According to the equation

Step 1: Preliminary calculation

    3H2                              +   N2                                                  2NH3

3moles                   1 mole                                  2moles

If

  ?                                ?                                          75moles

(3x 75)/2              (1x 75)/2                                   75moles

112.5moles          37.5 moles                               75moles

From the above it is clear that to get 75 moles of ammonia, 112.5 moles of hydrogen and 37.5 moles of nitrogen must have reacted.

The unreacted gases must have come out as effluent along with 75moles of ammonia

Step 2: Calculation of feed composition

Therefore the feed must have been (effluent + reacted moles)

Hydrogen=200 moles (effluent)+112.5moles(reacted)=312.5moles

Nitrogen=150 moles (effluent)+37.5moles(reacted)=187.5moles

Argon= 1mole

Step 3: Calculation of purged stream ( 5% of the top stream)

Top stream has 200 moles of hydrogen+150 moles of nitrogen and 1 mole of argon

Total number of moles =351moles

Out of 100 moles = 5moles is purged

Therefore out of 200 moles=10moles of hydrogen

Therefore out of 150 moles=7.5moles of nitrogen

Therefore out of 1mole=0.05mole of argon

Step 4: finding out the limiting agent

According to the equation

    3H2                              +   N2                                                  2NH3

3moles                   1 mole                                  2moles

If

312.5moles            ?=104.7mole                                                            

?=562.5 mole        187.5moles

We donot have 562.5 moles of hydrogen. Hence hydrogen is the limiting agent       

Out of 312.5 moles of hydrogen   =112.5moles of hydrogen are converted into ammonia

Therefore if 100moles are there= 112.5x 100/ 312.5=36

Step 5: overall conversion of hydrogen and nitrogen

3H2                              +   N2                                                  2NH3

3moles                   1 mole                                  2moles

Out of 4(total) moles= 2moles of ammonia are formed

Therefore out of 100 moles=50moles of ammonia will be formed

Step 6: Calculation of required fresh feed of hydrogen in kg/h

          3H2                              +   N2                                                  2NH3

       3moles                                                             2moles

      ( 3x2)=6kg                                                          2(14+3)=34kg

   312.5moles                                                         75 moles

3moles of hydrogen= 6Kg

312.5 moles= 6x 312.5/3=625kg

2moles of ammonia= 34Kg

75 moles= 34x 75/2=1275kg

For the production of 1275kg of ammonia=625kg of hydrogen is required

Therefore for the production of 100000kg=625x100000/1275= 49019.61kg of hydrogen is required

Answers

10moles of hydrogen +7.5moles of nitrogen+ 0.05mole of argon

Therefore the feed must have been (effluent + reacted moles)

Hydrogen=200moles/h

Nitrogen=150moles/h

Argon= 1mole/h

Ammonia= 75/h

       c)Single pass conversion of limiting agent Hydrogen)= 36%

       d) Molar flow rate of the components in the fresh feed

Hydrogen=312.5moles/h

Nitrogen=187.5moles/h

Argon= 1mole/h

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