Continuous Production of Nylon-6,6

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Presentation transcript:

Continuous Production of Nylon-6,6 Justin Cournoyer, Ryan Lacey, Courtney McLoud and Shannon Murphy This is only a template. You may chose to use or not use this format. I highly recommend you use a format that works for your group. Objectives and Introduction Produce 85 million lb of nylon-6,6 Inherently safe continuous process $3.7 Billion Industry Textile and Automotive: 44% Market Block Flow Diagram Polymerization Reactor Separation Adipic Acid HMDA Water Extruder Nylon-6,6 Water, Ammonia, HMDA, Adipic Acid, Phosphoric Acid Final Polymerization Reactor Phosphoric Acid Continuous Material Balance 100% Component (lb/hour) Stream 1 Stream 2 Stream 3 Stream 4 Stream 5 Stream 6 Stream 7 Stream 8 Stream 9 Stream 10 Stream 11 Stream 12 Stream 13 Stream 14 Stream 15 Stream 16 Stream 17 Stream 18 Stream 19 Stream 20 Stream 21 Adipic Acid 8823.025 882.302 294.1 588.2 HMDA 7015.713 701.5716 701.713 Water 20590.36 144.897 20445.463 20300.566 20155.669 14568.79 5586.879 5000 586.879 Phosporic Acid 364.3 Ammonia 46.26923 46.26 Nylon Salt 14254.87 Nylon 6,6 10732.32 Total 36839.6728 438.997 36400.8152 35961.8182 35522.8212 15680.9216 19841.749 11319.199 Critical to Quality Variables Product Efficiency Purity Packaging Ammonia by-product removed Cleaning and Maintenance Full Separation of Raw Materials Extruded into Pellets Spun into Fibers Temperature Control Economic Analysis Conclusions & Recommendations Continuous design is profitable DCFRR = 66% Continuous process is inherently safer than the semi-batch alternative Safety and Other Considerations Inherently Safe Substitute Moderate Minimize Simplify HAZOP R-110 Q-150 Material & Health Concerns AA and HMDA, Ammonia Relief Valves Other Considerations From both a safety and economic standpoint, the proposed continuous design is recommended as a GO Acknowledgements Dynamic Tension would like to thank Professor Halpern for his support throughout the last semester DCFRR=66% ROI=84%