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Background The hydrolysis of Penicillin G ( Pen - G ) yields phenylacetic acid ( PAA ) and 6 - amino - penicillanic acid (

Background
The hydrolysis of Penicillin G (Pen-G) yields phenylacetic acid (PAA) and 6-amino-penicillanic acid (6-APA)
(M=216gmol), the latter being an intermediate for a wide range of semi-synthetic antibiotics. The reaction
can be catalyzed in an aqueous solution with a strong acid, a strong base or an enzyme called Pen-G acylase.
On the order of 10,000 tons of 6-APA is produced worldwide on an annual basis, using batch processes that are
of moderate scale. The production-scale reactor available for your hydrolysis process is constructed from
stainless steel, with a maximum liquid volume of 20m3 and operating temperatures between 35C and 85C.
Design Calculations
Show all work on a separate page and report the final values below. Upload work with this answer sheet upon
submission. If a calculation is repeated multiple times, only one example calculation needs to be shown as work.
Rate Expression Development
Generate an expression for the rate of Pen-G hydrolysis as a function of reagent concentrations by modelling the
initial rate data provided in Table 1. This rate expression should have the general form:
Rate =k[ Pen-G]m[KOH]n
Pay particular attention to the units for each parameter of your kinetic model. Report your parameters below
and complete the last two columns of Table 1, including the units in the header row.
m=
n=
Table 1. Laboratory Data
Batch Reaction Times
Use your rate expression to predict the time in hours that is required to achieve 50%,95% and 99.9% conversion
pH remains essentially constant throughout the process. Recommend an overall reaction time at this condition
and calculate the mass of 6-APA that the process will provide from a single 20m3 batch. Report with units.
conversion =treact=m6-APA=
Please submit your completed assignment with work to OnQ at "VR Assignment Part 1: Design Prototyping
and Testing" submission folder.
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