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Integrated Systems + Principles Approach. Manufacturing Energy End-Use Breakdown. Source: California Energy Commission (2000). Energy Systems. Lighting Motor drive Fluid flow Compressed air Steam and hot water Process heating Process cooling Heating, ventilating and air conditioning - PowerPoint PPT Presentation
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Integrated Systems + Principles Approach
Source: California Energy Commission (2000)
Manufacturing Energy End-Use Breakdown
Energy Systems– Lighting– Motor drive– Fluid flow– Compressed air– Steam and hot water– Process heating– Process cooling– Heating, ventilating and air conditioning– Cogeneration
Principles of Energy Efficiency
Inside Out Analysis Understand Control Efficiency Think Counter-flow Avoid Mixing Match Source Energy to End Use Whole-system, Whole-time Frame Analysis
Integrated Systems + Principles Approach
Integrated systems + principles approach (ISPA) = Systems approach + Principles of energy efficiency
Electrical Lighting Motors Fluid FlowCompress
Air SteamProcess Heating
Process Cooling HVAC CHP
Lean Energy Analysis BaselineInside Out AnalysisMinimum Theoretical EnergyConversion and Control EfficiencyMatch Source Energy to End UseMaximize Counter-flowAvoid MixingWhole-system, Whole-time Frame Analysis
ISPA is both effective and thorough.
1. Inside-out Approach
Conversion Distribution UseEnergySupply
Energy Use
Inside-Out Analysis Approach
Inside-out Approach
Conversion Distribution Use
EnergySupplySavings
Energy End–Use Savings
Inside-Out Analysis Approach
Inside-out: Amplifies Savings
Reduce pipe friction: Savings = 1.00 kWhPump 70% eff: Savings = 1.43 kWhDrive 95% eff: Savings = 1.50 kWhMotor 90% eff: Savings = 1.67 kWhT&D 91% eff: Savings = 1.83 kWhPowerplant 33% eff: Savings = 5.55 kWh
Inside-out: Reduces Costs
Original design: 95 hp in 14 pumps Re-design:
– Bigger pipes: Dp = c / d5
• (doubling d reduces Dp by 97%)– Layout pipes then equipment
• shorter runs, fewer turns, valves, etc…– 7 hp in 2 pumps
Avoid Outside-in Thinking
Ein PrimaryEnergy
Conv ers ion Equipment
EnergyDis tribution
Sy s tem
Manufac turing
Plant Boundary
Proc es s andEquipment
E E Was teTreatment
Sy s tem
Was teDis pos alW W Wout
Inside-out analysis sequence for reducing energy
Inside-out analysis sequence for reducing waste streams
Traditional Analysis Sequence
for Reducing Energy Use
Traditional Analysis Sequence for
Reducing Waste
Result: Incremental improvement at high cost
Think from Inside Out!
Ein PrimaryEnergy
Conv ers ion Equipment
EnergyDis tribution
Sy s tem
Manufac turing
Plant Boundary
Proc es s andEquipment
E E Was teTreatment
Sy s tem
Was teDis pos alW W Wout
Inside-out analysis sequence for reducing energy
Inside-out analysis sequence for reducing waste streams
Inside-Out Analysis Sequence for
Reducing Energy Use
Inside-Out Analysis Sequence for
Reducing Waste
Result: Significant improvement at minimal cost
2. Understand Control Efficiency
Systems design for peak load, but operate at part-load
System efficiency generally changes at part load Recognize and modify systems with poor part-
load (control) efficiency
Control Efficiency
Energy
Production
Poor
Excellent
Air Compressor Control
FP = FP0 + FC (1 – FP0)
0.00
0.25
0.50
0.75
1.00
0.00 0.25 0.50 0.75 1.00
Fraction Capacity (FC)
Frac
tion
Pow
er (F
P)
Blow Off
Modulation
Load/Unload
Variable Speed
On/Off
Power and Flow Control
10% 20% 30% 40% 50% 60% 70% 80% 90% 100%0%
20%
40%
60%
80%
100%
By-pass Outlet Damper
Variable Inlet Vane Variable Frequency Drive
Volume Flow Rate (%)
Pow
er (%
)
Chiller Control
Boiler Control
Data Scatter Indicates Poor Control
2001 Gas Usage vs. Lime Production
0
5,000
10,000
15,000
20,000
25,000
30,000
0 500 1,000 1,500 2,000 2,500 3,000
Lime Production (tons)
Gas
Con
sum
ptio
n (m
cf)
3. Think Counter Flow
Heat transfer Fluid flow
Counter-flow Improves Heat Exchange
Q
T
T
x
x
Q
Parallel Flow
Counter Flow
Stack Furnace Pre-heats Charge
Reverb Furnace Stack Furnace
Molten Glass Transport:Each Exhaust Port Is A Zone
Counter-flow Within Zones
Increases convection heat transfer by 83%
Contact length = 2 x (5 + 4 + 3 + 2 + 1) = 30 feet
Contact length = (10 + 9 + 8 + 7 + 6 + 5 + 4 + 3 + 2 + 1) = 55 feet
Tile Kiln (Counter flow?)
TileExit Tile
Entrance
Counter Flow Cooling Enables Cooling Tower
Cross-flow cooling of extruded plastic uses 50 F water from chiller
4. Avoid Mixing
Availability analysis…Useful work destroyed with mixing
Examples– CAV/VAV air handlers– Separate hot and cold wells– Material reuse/recycling
HVAC Applications
Cooling Energy Use Heating Energy Use
Cooling Applications
Separate hot and cold water tanks
ProcessLoad 1
ProcessLoad 2
Chilled Water Tank
Cooling Tower
BypassValve
Tp2
Tc2 Process Pump
Tp1
Cooling Tower Pump
Tc1
5. Match Source Energy to End Use
0
50
100
150
200
250
300
Compressed air Open loopcooling
Chillers Cooling towers
$/m
mBt
u co
olin
g
Match Source Energy to End Use
Utilize Current Daylighting
Wright Brothers Factory, Dayton Ohio
Replace Colored / Fiberglass Windows with Corrugated Polycarbonate
Employ Skylighting
Skylights:– Highest quality light– Reduce lighting energy costs– Increase heating/cooling costs
6. Whole System Whole Time Frame Design
Design heuristic derived from natural evolution Nothing evolves in a vacuum, only as part of a system No optimum tree, fan, … Evolutionary perspective: ‘optimum’ synonymous with
‘perfectly integrated’ Optimize whole system, not components Design for whole time frame, next generation
Whole System “Lean” Manufacturing
400 ft/min 200 ft/min
200 ft/min
Whole System Energy EngineeringOptimum Pipe Diameter
Dopt = 200 mm when Tot Cost = NPV(Energy)+Pipe Dopt = 250 mm when Cost= NPV(Energy)+Pipe+Pump Energy250 = Energy200 / 2
Whole System Accounting
Budgeting and capital processes separate from operational processes
Organizational structures within companies constrains optimum thinking
Enlarge system boundary to include entire company
Whole-Time Frame Accounting“Efficiency Gap”
“Numerous studies conclude 20% to 40% energy savings could be implemented cost effectively, but aren’t…..”
Discrepancy between economic and actual savings potential called “efficiency gap”.
Puzzled economists for decades: “I can’t believe they leave that much change lying on the table.”
Don’t Eat Your Seed Corn
SP = 2 years is ROR = 50%
SP = 10 years is ROR = 10%