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Page 1: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]
Page 2: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Global Optimisation of Chiller Sequencing and Load Balancing Using Shuffled Complex Evolution

IAIN STEWARTA (MENG)LU AYEA (FAIRAH, FAIE, PHD)

TIM PETERSONB (PHD)

A Renewable Energy and Energy Efficiency Group, Department of Infrastructure Engineering,The University of Melbourne, Vic 3010, AustraliaB Environmental Hydrology and Water Resources Group, Department of Infrastructure Engineering, The University of Melbourne, Vic 3010, Australia

Page 3: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Evolutionary Chiller Optimisation (ECO)

• The why?

• A brief history of building controls

• Chillers and VSDs

• The how? Improving system efficiency

• Aims- Optimising equipment loading

• Model- Structure, inputs & outputs

• Results- Modelled savings

Page 4: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Why?

• Energy costs

• Carbon emissions

• Peak demand reduction

Page 5: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

40%

35%

15%

20%

Typical Commercial Building End Use Energy

HVAC

Lighting

Equipment

Other

92PJ

22MtCO2

Page 6: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

A Brief History of Building Controls

Pneumatic controls….

Page 7: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Direct Digital Control (DDC)

A Brief History of Building Controls

Page 8: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Building Management System (BMS)

A Brief History of Building Controls

Page 9: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Reciprocating vs Centrifugal Chillers

Page 10: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Chiller COP vs Loading

0

2

4

6

8

10

12

0% 25% 50% 75% 100%

Ch

iller

CO

P

Chiller Load %

New centrifugal variable speed chiller

Old reciprocating chiller

100%300%

Page 11: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Variable Speed Drives (VSDs)

Page 12: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Variable Speed Drives (VSDs)

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100%

Ener

gy C

on

sum

pti

on

Pump Speed

Pump Speed vs Energy Consumption

<50%

10% 80%

Page 13: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Technological improvements

• Capabilities of Building Management Systems

• Improved chiller part load efficiency

• Affordability of Variable Speed Drives

Page 14: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Current Control Technique

• Return water temperature staging

Switch-on thresholds Switch-off thresholds

From 1 chiller to 2 chillers: Trtn > 11.94 °C From 2 chillers to 1 chiller: Trtn < 9.28 °C

From 2 chillers to 3 chillers: Trtn > 11.85 °C From 3 chillers to 2 chillers: Trtn < 10.10 °C

From 3 chillers to 4 chillers: Trtn > 11.81 °C From 4 chillers to 3 chillers: Trtn < 10.51 °C

Trtn = Temperature of return chilled water from the building

Page 15: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

The Opportunity

• Maximize cooling system efficiency [COP]

– Non linear efficiency curves

– Multiple pieces of equipment

– Inherently difficult for humans

Page 16: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Aims

• Accurately simulate waterside plant equipment

• Optimise equipment loading for cooling loads

– Maximise plant COP for all cooling loads

Page 17: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

”All models are wrong but some are useful” – George Box

Page 18: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

ECO

1. Simulate waterside plant– Energy inputs

• Flow rates• Mechanical work• Efficiencies• Physical limits

– Refrigeration delivered2. Optimise equipment staging and loading using genetic algorithm for a range of cooling loads

Page 19: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Modelling assumptions

• Chiller turn down ratio = 10:1

• Condenser and chilled water pumps operate at minimum flow rate when chillers are at minimum output (eg. 50% pump speed when chiller is at 10% capacity)

• Pumps speed increases linearly with chiller energy

• Maximum temperature difference across chillers = 7°C

• Fans excluded from simulation

Page 20: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Plant layout

Page 21: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Plant Simulation

Inputs Simulation Output

Simulation of chilled water plant (Chillers &

Pumps)*Fans excluded

Cooling Load [kWr]

Low load chiller energy [kW]

High load chiller 1 energy [kW]

High load chiller 2 energy [kW]

Input energy [kWe]

System COP

Page 22: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Plant simulation

Ǘ𝑄𝑟 = Ǘ𝑚cw𝑐𝑤(𝑇𝑖 − 𝑇𝑜)

• where, Ǘ𝑚cw is the mass flow rate of the chilled water [kg s-1]

• 𝑐𝑤is the specific heat of chilled water [kJ kg-1K-1]

• 𝑇𝑖 and 𝑇𝑜 are the inlet and outlet chilled water temperatures [°C] across the chiller.

Page 23: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Regression analysis

Ǘ𝑄𝑟 = aP + bP2

where, Ǘ𝑄𝑟 is the refriegeration energy [kWr], P is the chiller input power [kWe], and a & b are scalars to be

calculated in the regression analysis

Page 24: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

y = -0.0185x2 + 8.8461xR² = 0.9224

0

200

400

600

800

1000

1200

1400

0 50 100 150 200

Co

olin

g ca

pac

ity

[kW

r]

Input Energy [kWe]

Regression of Chiller [kWr vs kWe]

Page 25: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]
Page 26: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Results of chiller regression analysis

Chiller #Input Power

[kWe]Nominal

Capacity [kWr] a b R2

1 59 289 8.7957 -0.0699 0.9236

2 178 988 8.8461 -0.0185 0.9224

Page 27: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Modelling Structure

InputSimulation & Optimisation

Outputs

Simulation of chilled water plant (Chillers &

Pumps)*Fans excluded

Cooling Load [kWr]

Low load chiller energy [kW]

High load chiller 1 energy [kW]

High load chiller 2 energy [kW]Shuffled complex

evolution algorithmObjective function:

∑ Plant equipment energy

Page 28: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Shuffled Complex Evolution

• Deterministic & probabilistic

• Competitive evolution

• Clustering

• Steepest decent

Page 29: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

0 500 1000 1500 2000 2500 3000 3500

Ch

ille

r In

pu

t P

ow

er

[kW

r]

Cooling Load [kWr]

Chiller Input Power [%] vs Cooling Load [kWr]

Low LoadChiller

High LoadChiller 1

High LoadChiller 2

Page 30: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

5.9

5.95

6

6.05

6.1

6.15

6.2

6.25

6.3

6.35

0 500 1000 1500 2000 2500 3000 3500

Syst

em

CO

P

Cooling Load [kWr]

System COP vs Cooling Load [kWr]

Page 31: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

5.9

5.95

6

6.05

6.1

6.15

6.2

6.25

6.3

6.35

0 500 1000 1500 2000 2500 3000 3500

Syst

em

CO

P

Cooling Load [kWr]

System COP vs Cooling Load [kWr]

Page 32: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Response surface, COP vs Chiller Loading [%]

Page 33: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

0

20

40

60

80

100

120

140

0 500 1000 1500 2000 2500 3000 3500

Ene

rgy

Savi

ngs

[kW

e]

Cooling Load [kWr]

Energy Savings [kWe] vs Cooling Load [kWr], aggregated into bins of 100kWr

Page 34: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

0

20

40

60

80

100

120

140

0 500 1000 1500 2000 2500 3000 3500

Ene

rgy

savi

ngs

[kW

e]

Cooling Load [kWr]

Energy savings [kWe] vs Cooling load [kWr]

Page 35: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

148,269

18,683

166,952

21,579

11,594

33,173

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

100%

Chillers Pumps Total

Modelled Energy Savings, 2016 [kWh]

Modelled energy consumption 2016 Energy savings from observed consumption

Page 36: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Results

Chiller 1 Chiller 2 Chiller 3 Pumps Total

2016 actual [kWh] 95,254 71,480 3,114 30,277 200,125

Modelled control strategy [kWh] 82,014 50,877 15,378 18,683 166,952

Energy savings [kWh] 13,240 20,603 (12,264) 11,594 33,173

% Savings 13.9% 28.8% -393.8% 38.3% 16.6%

Page 37: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

40%

35%

15%

20%

Typical Commercial Building End Use Electricity

HVAC

Lighting

Equipment

Other

92PJ

22MtCO2

Savings

15PJ

4MtCO2

15-25% Peak

demand reduction

Page 38: Global Optimisation of Chiller - AIRAH · Plant simulation 𝑄Ǘ 𝑟=𝑚Ǘcw𝑐𝑤(𝑇𝑖−𝑇𝑜) •where, 𝑚Ǘcwis the mass flow rate of the chilled water [kg s-1]

Next steps…

• Test ECO in real world

• Represent chillers and fans using neural networks to increase optimisation opportunities (adaptive control)

• Incorporate ambient conditions and fan/condenser pump speed modulation (dynamic control)