1 / 12

Chapter 10

Chapter 10. Synthesis of the PFD from the Generic BFD. It is a common human trait to resist change more strongly as more effort is expended on a task, design, or product. We describe this as not wanting to abandon our “investment” in the activity. Information Needs and Sources.

snow
Download Presentation

Chapter 10

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. Chapter 10 Synthesis of the PFD from the Generic BFD

  2. It is a common human trait to resist change more strongly as more effort is expended on a task, design, or product. We describe this as not wanting to abandon our “investment” in the activity.

  3. Information Needs and Sources • Interactions with other engineers and scientists. • Reaction kinetics data.-main and by products, catalysts,patents. Without kinetics data a prelim PFD and cost analysis can be done.(~.10kg product/kg catalyst per hour. Ea 40-200kJ/mol) • Physical property data-material and energy balances

  4. Reactor Section • Phase of the reacton • Temperature and pressure ranges • Controlled by kinetics or equilibrium • Need a solid catalyst or is it homogeneous • Exothermic or endothermic (magnitude) • Side reactions and selectivity • Single pass conversion. • Reactor feed outside the explosive limits fro gas-phase oxidations

  5. General guidelines for choosing separation operations • Table 10.1 Guidelines for choosing separation units. • Table 10.2 Guidelines for sequencing separation units.

  6. Sequencing Distillation Columns • Figure 10.1 • Azeotropes- figure 10.4

  7. Feed preparation • Heat exchangers • Pumps • Compressors • Exothermic reaction feed temperatures need to be high in order to prevent reactor runaway due to buildup of unreacted material and cause a severe temperature spike.

  8. Recycle Section • Should be at same conditions of feed when combined.

  9. Environmental Control Section • Minimize or eliminate

  10. Major process control loops • Significant design improvements can occur through developing major control loops. • They provide focal points for optimizing the process.

  11. Flow Summary Table. • See Chapter 1

  12. Major Equipment Summary Table • See chapter 1.

More Related