1 / 14

Aromatic Acylation with Cyclic Anhydride for Plasticizer Production

Aromatic Acylation with Cyclic Anhydride for Plasticizer Production ExxonMobil Research and Engineering Company. Peter Campbell, Karol Oldziej, Paul Wyka, Alex Gutwillig, Anthony Campesi, Andrew Accardi. Patent Description. To produce a high performance plasticizer

fredb
Download Presentation

Aromatic Acylation with Cyclic Anhydride for Plasticizer Production

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. Aromatic Acylation with Cyclic Anhydride for Plasticizer Production ExxonMobil Research and Engineering Company Peter Campbell, Karol Oldziej, Paul Wyka, Alex Gutwillig, Anthony Campesi, Andrew Accardi

  2. Patent Description • To produce a high performance plasticizer • Increases flexibility and workability of plastics • Used in PVC, sealants, vinyl products, etc.

  3. Introduction • In a Parr reactor HCl was added with OXO-C9 Benzoylbenzoate Ester, OXO-C9 Benzoylpropionate Ester or DINP. • Temperature maintained between 91 and 104 degrees Celsius inside the batch for 33 days. • Throughout the process, GC sampling was performed for monitoring of conversion.

  4. Process Variables

  5. Process Variables • The simulation consists of: • Controlled Variables: Temperature and reactant input • Manipulated Variable: Jacket coolant flow • Disturbance Variable: Random temperature fluctuations, including heat of reaction • Final Output: Reactant conversion and temperature profile

  6. Transfer Functions Above transfer function taken from relevant literature and modified for our situation Below transfer function was developed from graphical output of conversion weight percent

  7. Random Disturbance Generator Temperature vs Time

  8. Triglyceride Conversion %

  9. SAFETY

  10. Safety Features • The process is exposed to high temperatures and high pressures. • A cooling jacket installation to monitor temperature and vary flow of coolant. • Pressure indicators at high pressures can signal plant operators to relieve pressures by opening a valve. • If pressures are too high to indicate catastrophic failure or if no operator is around, installation of rupture disks would automatically release pressure.

  11. Conclusions • Our model reflects the conversion weight percent similarly to the graph shown on the patent. • Our model includes disturbances in temperature from ambient conditions and reaction inside the reactor. • Had we were given more time, a second-order function could have been developed to provide a more realistic scenario. • Instead, our transfer function was estimated to resemble the patent provided.

More Related