Thermal cracking of ethane in tubular reactor

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Balances dC j mass = Rj j = BR , 1, R2, M dt 0 2 , b ( ) ( ) , , , , −ka C − C = R C C dC L v H g H s H j H s H 2 2 2 2 ( ) ( ) , , , , ( ) , , 1 1 1 = + ka ka ka L dt v = ka C −C −ka C −C L v H g H b S S H b H s = ka C − C + R S S H b H s H 2 2 2 2 2 2 2 L v S S Indian Institute of Science

Page 1 and 2: Thermal cracking of ethane in tubul
Page 3 and 4: Ethane cracking reactor Typical ope
Page 5 and 6: Simulation of ethane reactor Indian
Page 7: Reactions 1/2 , 1 4 H 5 6 r −r
Page 11 and 12: Ammonia synthesis ‣ Major demand
Page 13 and 14: Ammonia synthesis - balances mass d
Page 15 and 16: Optimal temperature 4// /-8 34/ /-7
Page 17 and 18: Ammonia - Multibed reactor Conversi
Page 19 and 20: Ammonia - Autothermal 300 1000 T to

Thermal cracking of ethane in tubular reactor

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