Page 103 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
P. 103

(3)

                    13.






                         (4)








                         The conversion of ethanol is typically 60%. The yields for each reaction are approximately:


                         (1)  acetaldehyde 92%


                         (2)  ethyl acetate 4%


                         (3)  butanol 2%


                         (4)  acetic acid 2%


                         a. For this process, generate a process concept diagram showing all the input and output chemicals.


                         b. Develop two alternative preliminary process flow diagrams for this process.


                         Consider the following process in which liquid feed material A (normal BP of 110°C) is reacted with
                         gaseous feed material G to produce main product C and by-products R and S via the following
                         reactions:




                         A + G → C + S


                         G + C → R



                         Both feeds enter the process at ambient temperature and pressure. Both reactions occur in the gas
                         phase at moderate temperature and pressure (250°C and 10 bar). The normal boiling points of G, S,
                         and C are less than –120°C. By-product R has a normal boiling point of 75°C and is highly soluble in

                    14.  water. Product C is very soluble in water but G and S are insoluble. The single-pass conversion
                         through the reactor is low for feed A, and the ratio of G to A in the feed to the reactor should be
                         maintained in excess of 4 to minimize the chance of other unwanted side reactions. Using this

                         information, and assuming that both A and G are expensive, do the following.

                         a. Draw a preliminary process flow diagram identifying the main unit operations (reactors,
                         compressors, pumps, heat exchangers, and separators), and identify the recycle structure of the

                         process.
   98   99   100   101   102   103   104   105   106   107   108