determining the best heat recovery system to maximize...
TRANSCRIPT
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Determining the BestHeat Recovery System to Maximize Boiler Efficiency
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Overview
• Background• Reduce facility operating costs• Waste heat recovery
• Boiler Economizer • Benefits• Flow types• Applications• Designs
• Blowdown Heat Recovery• Benefits• Types
• Flash tank economizer• Blowdown heat recovery unit
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Thermodynamic Laws
First Law• The energy of the universe is
constant – it can be neither created or destroyed, but only transferred and transformed
• Heat and mechanical energy can be converted one to another
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Thermodynamic Laws
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Second Law• Heat travels from hot to cold
THIS IS TODAY’S TOPIC
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212º F200º F
100º F
32º F
0º F16
Temperature-Heat Diagram For 1 lb
Btu per pound of water
Steam – Basic Concepts
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180
1 lb water at 212O F
970
1 lb steam at 212O F
144
1 lb water at 32O F
Sensible Latent Sensible Latent
Of Water At Atmospheric Pressure (14.7 psia)
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Design Considerations For Heat Transfer
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• Proportionality between heat flux/unit area and Delta T
Heat Transfer Coefficient
• Logarithmic average Delta T between hot and cold streams at each end of Hx
LMTD
• Ratio of inertia forces to viscous forces: <2000 = Laminar, >4000 = Turbulent
Reynolds #
• Rate of heat transfer over an area
U Factor
• Depends on the foulent and temperature
Fouling Factor
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Heat Transfer
Typical Boiler Tube
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Heat Transfer
Cleaver-Brooks Advanced Heat Transfer Tube
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Economizer Flow Types – Parallel
• Fluids flow in the same direction• Hot side inlet temperature is in contact with the
cold side inlet temperature• Delta T narrows• Used in applications where minimum temperature is adequate
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Economizer Flow Types – Counter
• Fluids flow opposite direction and enter heat exchangerat opposite ends
• Most efficient when comparing heat transfer rate per unit surface area• Average T (difference in temperature) between the two fluids
over the length of the heat exchanger is maximized
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Economizer Flow Types – Cross
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Economizer Flow Types – Cross
• Fluids flow perpendicular to each other• Can be most practical design for high
mass flows and space restrictions• Still maintains high Delta T throughout the
exchanger
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HT Coefficient And High Reynolds
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Boiler Economizers
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Economizer Design
Non-Condensing• Most common design• Recover sensible heat only• Single stage• Cross or counter flow• Applications
• Steam boiler feedwater preheat• Proportional feedwater control• On/off feedwater control
• Process water (higher temperatures)
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Economizer Design
Condensing• Recover sensible and latent
• Saturation temperature• Natural gas ~135ºF
• Single stage• Condense on natural gas only
• Applications – water temperature less than ~120ºF
• Cold make-up water• Process flow (lower temperature)• Hot water return
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Economizer Design
2 Stage Condensing• 2 Stages
• 1st stage – sensible heat recovery• Standard (non-condensing)
economizer• 2nd stage – sensible and latent heat
• Condensing economizer• Condense on natural gas only
• Applications• 1st stage
• Preheat boiler feedwater (MFWV)
• On/off feedwater control• 2nd stage
• Any cool liquid stream (50-120ºF)• Make-up water • Process water
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Economizer Applications
Steam Boiler Feedwater
PreheatMake-up water Process Water
• Run feedwater from a boiler feed system or deaerator through the economizer and into the boiler• Modulating boiler
feedwater control• On/off feedwater
control
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Economizer Applications:Steam Boiler Feedwater Preheat With MFWV
Inlet
Outlet
Non-condensing
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Economizer Applications:On/Off Feedwater Control
Non-condensing
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Economizer Applications:Make-Up Water
Condensing or Non-condensing
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Economizer Applications:Process Flow
Condensing or Non-condensing
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Economizer Benefits
•Dependent on product design and application
Increase Boiler Room Efficiency By 3-8%
Reduce NOx Emissions
•Average total payback: 12-18 months
Save Operating Costs
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Blowdown Heat Recovery Types:Blowdown Heat Recovery Unit
• Proportional blowdown heat recovery system • Atmospheric feed or deaerator• Automatically controls TDS• Single or multiple boilers • Blowdown is cooled before discharge (code compliance)
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Blowdown Heat Recovery Types:Flash Tank Economizer
• Recover blowdown energy(latent and sensible heat)
• Use flash steam for LP use• Blowdown is cooled before
discharge (per code)• Used for single or multiple boilers
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Calculating Flash Steam %
For example, a boiler operating at 200 psig with discharge @ 5 psig:
362 – 196 = 166166 / 961 = 17% Flash
BTUs SAVEDWater and sewer charges SAVED
Chemicals SAVED
HF1 – HF2 / HFG2 = % Flash
HF1: Sensible BTUs inHF2: Sensible BTUs outHFG2: Latent BTUs out
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Integration
• Reclaim heat loss and reduce facility operating costs• Economizer• BDHR• TDS control • Include O2 trim• HTDB• Parallel positioning• VSD• Integrated lead lag• DA control• Draft control
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Integrating The System
Bypass DamperDeaerator
WaterTreatment
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Questions?