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Digester Heating 101
Tom Mossinger – Carollo Engineers PNCWA 2012
2012 Annual Conference Boise, ID
October 23, 2012
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Agenda
• Review hot water system theory and operation
• Discussion on typical components
• Highlight typical problems
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Heating System - Considerations
• Move heat from sources to uses
• Hydraulics
• Allow for future expansion and/or cogeneration
• Space requirements
• Complexity of system
• Flexibility
• Operations and maintenance
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Heating System Types
• Primary loop
• Primary-secondary loop
• Constant flow
• Variable flow
• Hybrid systems There are
Literally 100’s of configura7ons!
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Simplified Hot Water System Schematic
Cogeneration System
Main Loop
180°F
TIC TIT
BLR ~180°F
TIC
TIT
150° MAX
TIT
98°F
Sludge
Softened makeup
water
Expansion tank
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Typical Cogeneration System
Engine Generator
Waste Heat
HW System
Exhaust
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Typical Boiler System
Boiler
Exhaust TIC TIT
180°F
Internal Controls
On 150°F
Set Point 190-195°F Off 195-210°F
(Typical)
Main HW Loop
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Typical Digester Heating System
TIC
TIT
150° MAX
TIT
98°F
Sludge
Main HW Loop
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Hot Water System Pressure Control
Softened makeup
water
Expansion tank
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Typical Hot Water System Components
• Pumps
• Air separator
• Expansion tank
• Makeup water connection
• Chemical feeder
• Air relief valves
• Control valves
• Balancing Valves
• Strainers
• Pressure relief valves
• Boilers
• Valves
• Heat exchangers
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Digester Heat Exchangers
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Shell and Tube Sludge Heater
• Combined boiler and heat exchanger
• Hard to incorporate future hot water systems
• Least efficient
• Less flexible
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Tube-in-Tube Heat Exchangers
• Primarily used for thicker sludge or where plugging is likely
• More expensive
• Larger footprint
• Hard to predict heat transfer
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Spiral Heat Exchangers
• Most efficient
• Predictable heat transfer
• Less expensive
• Smallest footprint
• Easy to clean
• More likely to plug with thicker sludges or poor screening
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Typical Problems
• Corrosion – Air intrusion
– Water treatment
• Flow rate control – Balancing
• HW system expansion after expansion after expansion
• Complication!
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Heat Exchanger Scale – Vivianite, Baked on Sludge
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Ductile Iron is an Excellent Heat Conductor
F Temp
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Scaling Decreases Heat Transfer
F Temp
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Thermal imaging provides a quick non-destructive method to determine the
extent of scaling
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What is the extent of scaling in the digester piping?
100° F 125° F Temperature
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Prevention and planning can prevent scaling problems
• Tools available for cost-effective detection
• Mitigation involves removing conditions that favor scaling: – Remove phosphorus
– Prevent large temperature changes
– Prevent large pH changes
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Water Treatment
• Companies such as Nalco provide sampling and treatment chemical packages
• Chemicals typically include: – Scale inhibitor
– Oxygen scavenger
– Biocide
• Use water softener for all make-up
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Questions?