Incrt N2 (1-l-N2) H2 Inert * N2 (1-sl-N2) H2 0.080 0.230 0.230 0.690 156.5 0.690 4 N2 450.0 m5 H2 1350.0 n4 N2 450 800 N2 0245 n1 N2 600 2 H2 1800 n5 H, 1350 S NH3 300 Reactor H2 0.735 n3 Inert 156.5 m3 Inert 156.5 I 02 n6 NH3 300 The flowchart provided is for the production of Ammonia according to the reaction N2+3H2-->2NH3 using the information provided, calculate the flow rate of the purge stream (n,). Condenser
Incrt N2 (1-l-N2) H2 Inert * N2 (1-sl-N2) H2 0.080 0.230 0.230 0.690 156.5 0.690 4 N2 450.0 m5 H2 1350.0 n4 N2 450 800 N2 0245 n1 N2 600 2 H2 1800 n5 H, 1350 S NH3 300 Reactor H2 0.735 n3 Inert 156.5 m3 Inert 156.5 I 02 n6 NH3 300 The flowchart provided is for the production of Ammonia according to the reaction N2+3H2-->2NH3 using the information provided, calculate the flow rate of the purge stream (n,). Condenser
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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