470 likes | 1.03k Views
Ethanol Production from Wastepaper. Ben Dalton Marie Labrie Cassia Davis Alex Saputa John Ozbek Steve Wild Murat Ozkaya 4/15/09. Outline. Project Purpose Assumptions Process Flow Pre-Treatment Saccharification & Fermentation Distillation/Purification Energy Utilization/Usage
E N D
Ethanol Production from Wastepaper Ben Dalton Marie Labrie Cassia Davis Alex Saputa John Ozbek Steve Wild Murat Ozkaya 4/15/09
Outline • Project Purpose • Assumptions • Process Flow • Pre-Treatment • Saccharification & Fermentation • Distillation/Purification • Energy Utilization/Usage • CO2/H2O Footprint • Economics • Summary
Project Purpose Design a facility that is: • State-of-the-art • Flexible • Adaptible • Bio-chemical processing plant • Optimizing Ethanol production
Project Purpose Optimizing includes: • Water usage • Energy usage • CO2 • Waste Stream Utilization/Cogeneration • Return on investment
Assumptions • 100 Tons of Waste Paper per Day • Waste Paper Contains 50% Cellulose • 81% Conversion of Cellulose to Ethanol in 24 hours • Target Purity: 99.5wt% Ethanol
WATER PAPER PRE-TREATMENT PURIFICATION YEAST & ENZYME PRODUCTION Ethanol SACCHARIFICATION & FERMENTATION
Pre-Treatment Undesirables
Enzymes-What are they? • Enzymes are catalysts that are biological molecules • Like all catalysts, enzymes dramatically increase the rate of reaction
Breaking up Cellulose (Saccharification) • Breaking up cellulose requires three enzymes collectively called cellulases
Where Do You Get Enzymes? • Trichoderma reesei (yeast) • Secretes cellulases • One of the most powerful secretors of cellulases known to date
+ Producing Enzymes Water Yeast Nutrients Water Nutrients Yeast Enzyme Production Culture 600 lbs 20 lbs/day Mixture 300 lbs/day Enzyme Yeast Pre-Culture 25 lbs
Saccharification by Enzymatic Hydrolysis Enzymes Cellulose C6H12O6 (Glucose)
Fermentation 2C2H5OH Yeast C6H12O6 + 2CO2
Non-Isothermal Continuous Saccharification and Fermentation (NCSF) Enzyme CO2 Slurry Ethanol Yeast Enzymatic Hydrolysis Fermentation
NCSF Material Balance Enzyme 20 Tons CO2 400 Tons H2O 50 Tons Cellulose 50 Tons Lignin 400 Tons H2O 21 Tons Ethanol 59 Tons Undigested Paper 50ºC 45ºC 40ºC 35ºC 30ºC Yeast
NCSF Energy Balance 55 MMBtu/Day 50ºC 45ºC 40ºC 35ºC 30ºC Cooling H2O 40 MMBtu/Day HPS
Distillation: Material Balance DISTILLATE D= 20 tons/day QC= 110 MMBtu/day XD= 90.6 wt% EtOH FEED F= 420 tons/day XF= 5.0 wt% EtOH BOTTOMS B= 400 tons/day QR= 200 MMBtu/day
Distillation: Column Specifications Sieve tray 1 stage 2 ft 40 ft 20 stages 11 ft
Water Adsorption by a Molecular Sieve 21 Tons EtOH + 2 Tons H2O 11 Tons Synthetic Zeolite ~21 Tons EtOH
Regeneration of the Molecular Sieve ~ 6 Tons Hot CO2 + 2 Tons H2O Vapor Per Day 11 Tons Synthetic Zeolite 6 Tons CO2/ Day 7.1 MMBtu/Day
Waste Stream Utilization Flue Gases 200 MMBtu/Day Steam Boiler Undigested Paper 720 MMBtu/Day High-Pressure Steam 520 MMBtu/Day
Energy: Ethanol from Wastepaper Cogenerated Electricity Papernol Plant 200 MMBtu/Day Ethanol 500 MMBtu/Day
Energy: Ethanol from Corn Corn Based Ethanol Plant Fossil Fuels Ethanol 500 MMBtu/Day 450-550 MMBtu/Day
CO2 Footprint Papernol Produces 120 tons CO2 / day Papernol Average CO2 released by vehicles in Chattanooga = 3,300 tons per /day
H2O Footprint Papernol Papernol Plant Uses 20 tons/day Grey Water
Capital Costs • Reactor Vessels $1.5M • Steam Boiler $1.0M • Enzyme Tanks $1.0M • Shredder/Conveyer $500K • Distillation Column $240K • Prep Tank $90K • Molecular Sieve $70K • Total $4.4 Million
Economic AnalysisCapital Costs Equipment Cost = $4.4M Plant Heuristic x (4.7) Total Capital Cost = $20M
Annual Operating Costs • Wastepaper $300K • Water $200K • Electricity $120K • Nutrients $86K • Enzyme & Yeast $33K • Cooling Water $21K • Total$1.2 Million
Production Costs $4M $1.2M 2.3M Gal $2.56/Gal • Annual Capital Cost • 5 Year Payback • Annual Operating Cost • Annual Production • Production Cost
Return On Investment 10 Year ROI 5 Year ROI $2.56/gal $1.66/gal
Summary • Project Purpose • Assumptions • Process Flow • Pre-Treatment • Saccharification & Fermentation • Distillation/Purification • Energy Utilization/Usage • CO2/H2O Footprint • Economics
Conclusion • Facility Produces 21 tons of Ethanol Daily • Net Energy Usage is (+)700 MMBtu/day • Return on Investment of 5 Years • Gives a Cost = $2.56/gallon