final presentation
DESCRIPTION
Final Presentation. Team: India Plant: Resources Recovery Members: Lynette Hernandez, Hsin Ting Hsieh, Jose L. Ortiz, and Alexander J. Palmas Scribe: Alexander J. Palmas Mentor: Patrick H. Shannon, Middough. 1. Where we are located. 2. Outline for Final Presentation. - PowerPoint PPT PresentationTRANSCRIPT
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Final Presentation
Team: India
Plant: Resources Recovery
Members:
Lynette Hernandez, Hsin Ting Hsieh, Jose L. Ortiz, and Alexander J. Palmas
Scribe: Alexander J. Palmas
Mentor: Patrick H. Shannon, Middough
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Where we are located
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Outline for Final Presentation• Overall PFD and Design Basis for
Water and CO2
• Total Production of Plant • Plant Layout• Initial Control Scheme • Overall Energy Requirements • Economics • Recommendations • Conclusion • Acknowledgements
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Water Overall PFD
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To Fertilizer and CHP plant
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Water Design Basis
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CO2 PFD
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CO2 Design Basis
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What's Produced
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Stream Flowrate Units
Total Water Waste 748,821 lb/day
Water Sent to Fertilizer Plant
690,446 lb/day
Water Sent to CHP 243,935 lb/day
CO2 Sold for EOR 129,378 lbmol/day
CO2 Waste to CHP 2,168 lbmol/day
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Plant Layout
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Process Waste Water and Frac Water Coming In and Process Water Out
CO2 Sold for EOR
Incoming CO2
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Initial Control Scheme
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Overall Energy Requirement
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Unit Horsepower
PSA 2,200
CO2 Compressor 2,339
UF Unit 38
RO Unit 470
DAF 100
Pumps 65
Total 5,212
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Economics
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Economics
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Recommendations
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• Use a crystallizer/evaporator o Allow flow of free energy o Lower electricity cost by using low
pressure steam that's already produced within the shale gas complex
• Look into other alternatives for waste disposal other than landfill o Recycle/sell waste oils
• Obtain a competitive CO2 Compressor quote
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Conclusion
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• Project life of 20 years
• Plant needs to be built o Allows site to reach EPA
requirements o Essential to entire plant
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Acknowledgements
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• Patrick Shannon • David Field • Professor Perl • Other mentors
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