UC Davis Presentation (2012)

H
Combined Hydrogen, Heat, and
Power (CHHP) Plant Design
Presenter: Mengjing (Irene) Yu
Team Members: Maya Biery Maggie Mei
Elisha Clerigo, Abigail Bonifacio, Suzann Muy, Dustin Cutler,
Roshni Varghese, Farah Quader
Faculty Advisor: Julie Schoenung, Paul Erickson
University of California, Davis
CHHP Overview
Manure
Rice Straw
Anaerobic
Digestion
Biogas
Treatment Biogas
DFC 300
Air
Exhaust Heat
Fuel Cell Exhaust
Water-Gas Shift
Reaction
Vapor-Liquid
Separation
Pressure Swing
Adsorption
Compressed
Hydrogen Storage Hydrogen
Cylinders
Heat Recovery
Unit
Greenhouse
Hydrogen
Community
Electricity Substation
CHHP
Campus
Greenhouse
Hot Water
CO2
Water
Steam
Feedstock Overview
• The feedstock for DFC300 is biogas produced from digesting
manure and rice straw, both readily available in Davis.
• Collectable manure can come from cattle, milk cow, horse,
sheep, lamb, and goat. Total manure available per day is
27,387 kg.
• 95% of rice production in California takes place within 161km
of Sacramento. Annually, California produces 1.3 billion kg of
straw waste.
• Combination of manure and rice straw gives good carbon-
nitrogen ratio and optimum moisture content.
+ =
Technical Design
Hydrogen Purification
Hydrogen Purification
Water-Gas Shift Reaction
Reactor Design:
• Fixed Bed Plug Flow Reactor with Shell and
Tube Configuration
• Optimum Temperature is 350°C
• Cooling Water Jacket
• Catalyst is Iron Oxide containing 5-15%
Cr2O3
CO + H2O CO2 + H2
Vapor-Liquid Separation
Hydrogen Purification
Vessel Specifications:
• Vessel Dimension is
Calculated using
Design Heuristic
• Liquid Hold-Up Time
is 3 to 5 Minutes
• An Entrainment
Wire Mesh Served
as Mist Eliminator
Hydrogen Purification
Pressure Swing Adsorption (PSA)
• H2-CO2 Mixture is
Compressed to 200
psig Before Entering
PSA
• Catalyst is Zeolite,
Activated Carbon,
Silica Gel
• Cycling Schedule:
Pressurization,
Regeneration,
Repressurization
• Minimum of 2
Adsorbers Photo Credit: Full System Engineering Co., LTD.
Hydrogen Storage
• Hydrogen is Stored at 5000 psig
• Hydrogen Flow Rate is 29 scfm
• Composite Material for the Tank
• Tuffshell® Fuel Storage Systems
Photo Credit: Lincoln Composites
Hydrogen End Use
• DFC300 produces 62 kg hydrogen per day
• Hydrogen is transported to the Hydrogen Community
using hydrogen cylinders
• A 60 kW and a 5 kW Altergy Freedom Energy PEM
fuel cell is used to generate electricity
• Capable of supporting approximately 51 households
Photo Credit: Altergy Freedom Energy
Heat and Electricity End Use
Exhaust Heat
Exhaust heat is recovered to produce
steam and hot water. Steam is used for
steam heating greenhouses. Hot water
is mainly for nearby buildings and
facilities.
Electricity
A substation including meters, breakers,
transformer, and transmission lines is
built to support the interconnection.
CHHP itself consumes about 126 kW of
electricity, so net electricity available is
about 154 kW.
1 of 10

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UC Davis Presentation (2012)

  • 1. Combined Hydrogen, Heat, and Power (CHHP) Plant Design Presenter: Mengjing (Irene) Yu Team Members: Maya Biery Maggie Mei Elisha Clerigo, Abigail Bonifacio, Suzann Muy, Dustin Cutler, Roshni Varghese, Farah Quader Faculty Advisor: Julie Schoenung, Paul Erickson University of California, Davis
  • 2. CHHP Overview Manure Rice Straw Anaerobic Digestion Biogas Treatment Biogas DFC 300 Air Exhaust Heat Fuel Cell Exhaust Water-Gas Shift Reaction Vapor-Liquid Separation Pressure Swing Adsorption Compressed Hydrogen Storage Hydrogen Cylinders Heat Recovery Unit Greenhouse Hydrogen Community Electricity Substation CHHP Campus Greenhouse Hot Water CO2 Water Steam
  • 3. Feedstock Overview • The feedstock for DFC300 is biogas produced from digesting manure and rice straw, both readily available in Davis. • Collectable manure can come from cattle, milk cow, horse, sheep, lamb, and goat. Total manure available per day is 27,387 kg. • 95% of rice production in California takes place within 161km of Sacramento. Annually, California produces 1.3 billion kg of straw waste. • Combination of manure and rice straw gives good carbon- nitrogen ratio and optimum moisture content. + =
  • 5. Hydrogen Purification Water-Gas Shift Reaction Reactor Design: • Fixed Bed Plug Flow Reactor with Shell and Tube Configuration • Optimum Temperature is 350°C • Cooling Water Jacket • Catalyst is Iron Oxide containing 5-15% Cr2O3 CO + H2O CO2 + H2
  • 6. Vapor-Liquid Separation Hydrogen Purification Vessel Specifications: • Vessel Dimension is Calculated using Design Heuristic • Liquid Hold-Up Time is 3 to 5 Minutes • An Entrainment Wire Mesh Served as Mist Eliminator
  • 7. Hydrogen Purification Pressure Swing Adsorption (PSA) • H2-CO2 Mixture is Compressed to 200 psig Before Entering PSA • Catalyst is Zeolite, Activated Carbon, Silica Gel • Cycling Schedule: Pressurization, Regeneration, Repressurization • Minimum of 2 Adsorbers Photo Credit: Full System Engineering Co., LTD.
  • 8. Hydrogen Storage • Hydrogen is Stored at 5000 psig • Hydrogen Flow Rate is 29 scfm • Composite Material for the Tank • Tuffshell® Fuel Storage Systems Photo Credit: Lincoln Composites
  • 9. Hydrogen End Use • DFC300 produces 62 kg hydrogen per day • Hydrogen is transported to the Hydrogen Community using hydrogen cylinders • A 60 kW and a 5 kW Altergy Freedom Energy PEM fuel cell is used to generate electricity • Capable of supporting approximately 51 households Photo Credit: Altergy Freedom Energy
  • 10. Heat and Electricity End Use Exhaust Heat Exhaust heat is recovered to produce steam and hot water. Steam is used for steam heating greenhouses. Hot water is mainly for nearby buildings and facilities. Electricity A substation including meters, breakers, transformer, and transmission lines is built to support the interconnection. CHHP itself consumes about 126 kW of electricity, so net electricity available is about 154 kW.