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Chilled Water System Presentation
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Constant Volume Distribution
Constant Volume Distribution
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Air-conditioning System Components
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Constant Volume System Components
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Typical 3-way Valve Zone
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Full Load Condition
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Fully Loaded Coil
• Supply water temperature 45°F
• Design return water temp. 55°F
• Coil design flow 100 GPM
• Coil design pressure drop 20 FT
• Load (flow x 10°F∆ x 500) 500,000 Btuh
• Coil ∆P @ design flow 20 FT
• Bypass flow 0 GPM
• Bypass ∆P 3-way valve closed
• 3-way valve pressure drop 10 FT
• Pump flow and head 100 GPM @ 30 FT
• Actual return water temp 55 °F
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Unloaded Condition
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Unloaded Coil
• Supply water temperature 45°F
• Design return water temp. 55°F
• Coil design flow 0 GPM
• Coil design pressure drop 3-way valve closed
• Load (flow x 10°F∆ x 500) 0.0 Btuh
• Coil ∆P @ design flow 0 FT
• Bypass flow 100 GPM
• Bypass ∆P 20 FT
• 3-way valve pressure drop 10 FT
• Pump flow and head 100 GPM @ 30 FT
• Actual return water temp 45 °F
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So What?
• When the load on the coil is zero, the valve is returning “unused”
chilled water at essentially supply temperature.
• Cold return water “unloads” the chillers, causing them to operate
inefficiently.
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Part Load Condition
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Partially Loaded Coil
• Supply water temperature 45°F
• Design return water temp. 55°F
• Coil design flow 50 GPM
• Coil design pressure drop 20 FT
• Load (flow x 10°F∆ x 500) 250,000 Btuh
• Coil ∆P @ design flow 5 FT
• Bypass flow ??? GPM
• Bypass ∆P 3-way partially closed
• 3-way valve pressure drop 10 FT
• Pump flow and head ??? GPM @ 30 FT
• Actual return water temp ?? °F
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125
100
75
50
25
0
% Valve Stroke
25 50 75 100
%
Flow 1/2 Through Coil
1/2 Through Bypass
Full
Flow
Through
Coil
Full
Flow
Through
Bypass
3-way Valve Characteristic
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What’s Really Happening?
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Coil with 3-way Valve at Mid-position
• Supply water temperature 45 °F
• Design return water temp. 55 °F
• Load (flow x 10°F∆ x 500) 250,000 Btuh
• Coil design pressure drop 20 FT
• Coil flow 62.5 GPM
• Coil ∆P @ 62.5% flow 7.8 FT
• Coil leaving water temp 53 °F
• Bypass flow 62.5 GPM
• Bypass ∆P 7.8 FT
• 3-way valve pressure drop 10 FT
• Pump flow and head 125 GPM @ 30 FT
• Actual return water temp 49 °F (62.5 GPM @ 53 °F+
62.5 GPM @ 45 °F)
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Head2 = Head1(Flow2/ Flow1)2
Head2 = 20(.625/1)2
Head2 = 20(.3906 )
Head2 = 7.8
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∆T = Load/ Flow X 500
∆T = 250,000/62.5 X 500
∆T = 8
Therefore, LWTcoil = 45 + 8 = 53
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RWT = (Flow1 X EWT + Flow2 X LWT)/ Flow1 + 2
RWT = (62.5 X 45 + 62.5 X 53)/125
RWT = 49
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3-way Valve in Mid Position
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1.Low return water temperatures.
2.Robs chilled water from other coils at part
load conditions.
3.Increases flow in primary piping.
4.Adds additional chillers on line.
5.Chiller performance is reduced.
3-way Valve System Deficiencies
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1.1
20 30 40 50 60 70 80 90 100
10
1.0
0.9
0.8
0.7
0.6
0.5
KW
per
Ton
Percent Load
Chiller Performance Curve
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Pump Sizing
• Select for full chiller flow
• Head must be adequate for:
– Chiller evaporator
– Longest circuit
– Coil
– Three way valve
– Air separator
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System Configuration
Constant Volume
Any Questions?
Variable Volume Constant Speed
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Primary – Secondary System
Primary – Includes Chillers & Primary Pump.
Circuit Constant water flow through the chiller
is maintained and chilled water is
produced
Secondary – Chilled water is circulated to the
Circuit demand area (load) by using
Secondary pumps.
Variable Volume Constant Speed
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PRIMARY - SECONDARY
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Other Famous Names of Primary-
Secondary
Primary – Production Loop
Secondary – Distribution Loop
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Fundamental Idea
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No Secondary Flow
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Primary = Secondary
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Primary > Secondary
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Primary < Secondary
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Control Valve in Secondary
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• Use the flow of the largest chiller
– Chiller staging at half of this flow is common
• Head loss in common <1 1/2 ft
– Distribution pipe size is often used where reductions would be
inconvenient
• Three pipe diameters between tees
– Excessive length increases total head loss
• Low velocities in system piping
Common Pipe Design Criteria
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Variable flow through coil
Constant flow through system
Three Way Valve
Variable flow through coil
Variable flow through system
Two Way Valve
Control Valve in Secondary
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PRIMARY – SECONDARY CIRCUIT
Variable Volume Constant Speed
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Head
F1 F2 F3
H1
H2
H3
Flow
Control Valves Change the Secondary
System Curve
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% Flow
125
100
75
50
25
150
25 50 75 100
HD
Varying differential pressure
absorbed by control valve
System resistance
TDH of pump
Pump curve
Head Absorbed by 2-way Valves
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HP
125
100
75
50
25
150
25 50 75 100
% Design Flow
Primary Pumps = V/V
Secondary Pumps +
Constant Flow Primary Pumps, only
Pump Horsepower Comparison
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% Flow
90
80
70
60
50
40
30
20
10
0 10 100
90
80
70
60
50
40
30
20
100
110
120
130
140
150
Base
Design
HP %
% Full Load
(Design) HP
Pump Over-haded by 150%
Constant Flow, C/S Pump
(3 Way Valve)
Constant Flow, C/S Pump
(3 Way Valve)
C/S Pump
(2 Way Valve)
Pump HD Matched
to System @
Design Flow
C/S
Pump (2 W
ay Valve)
Constant vs Variable Volume
Any Questions?
Step Function of Chillers
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Production = Distribution
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Distribution > Production
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Production > Distribution
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“Loading” a Chiller
• A chiller is a heat transfer device. Like most equipment, it is
most efficient at full load.
• To “load” a chiller means:
– Supply it with its rated flow of water
– Insure that water is warm enough to permit removal of rated Btu
without freezing the water
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Chiller Performance Curve
1.1
20 30 40 50 60 70 80 90 100
10
1.0
0.9
0.8
0.7
0.6
0.5
KW
per
Ton
Percent Load
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Check Valve in Common?
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What can we do?
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What else can we do?
Reset Supply Temperature
• Lower chiller set point when mixing occurs to maintain a constant
temperature to the system.
• Expect increases in cost of chiller operation at lower set point: 1-3% per
degree of reset.
• Delays start of the next chiller.
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What else can we do?
• Coils that are selected at higher supply temperatures will not be
impaired by small changes.
• Loads that require fixed temperatures may use a small chiller to
reverse the effects of mixing.
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Multiple Chillers
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60/40 Chiller Split to Help Minimize Low Part Load Operation
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0-10 30-40 60-70 90-100
0
5
10
15
20
25
30
0-10 30-40 60-70 90-100
%
Time
% Load
Typical Load Profile
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Three Unequally Sized Chillers
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% Load
Time
Approaching Flow = Load
Any Questions?Alternate
Pumping Methods
Comparison
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Two Pipe Direct Return
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Two Pipe Reverse Return
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Primary-Secondary Pumping.
• Simplest to install.
• Simplest to operate.
• Flexible in design for present and future.
• Efficient to operate.
• May over-pressurize near zones.
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Primary-Secondary-Tertiary
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Primary-Secondary-Tertiary Pumping.
• Best piping flexibility.
• Best expansion flexibility.
• Provides hydraulic decoupling.
• Efficient to operate.
• May require added horsepower.
• Requires additional pumps and piping.
• Increased controls complexity.
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Primary-Secondary-Tertiary Hybrid
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Primary-Secondary-Tertiary Hybrid Pumping.
• Low present horsepower.
• Low future horsepower.
• Good piping flexibility.
• Good expansion flexibility.
• Provides hydraulic decoupling.
• May require added horsepower
• Requires additional pumps and piping.
• Increased controls complexity.
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Primary-Secondary Zone Pumping
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Primary-Secondary Zone Pumping.
• Low ‘built out’ horsepower.
• Low system head.
• Increased control complexity.
• Present horsepower total higher due to future needs.
• Present pumps sized for future requirements.
• Difficult to apply in retrofits projects.
Any Questions?
Variable Volume Variable Speed
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Why Do We Need Variable Speed
Secondary Pumps ???
•For Energy Saving….
•For better & optimise operation….
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How Do We Achieve This Reduction In Power
Consumption ??
By Using Variable Frequency Drive and Logic controller
with the Secondary Pumps….
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Power Comparison at Reduced Speed
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Basic Law which helps in achieving this – Affinity
law
1. Flow2 = Flow1(Speed2/ Speed1)
2. Head2 = Head1(Speed2/ Speed1)2
3. BKW2 = BKW1(Speed2/ Speed1)3
If Diameter of Impeller is to be trimmed then instead of
speed the same can be used in above formulas.
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0
50
100
150
200
250
300
350
400
450
50 100 150 200 250 300 350 400 450 500
Motor Horsepower
Annual
Operating
Cost
$1000
$0.10/kWh
Operating Cost
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Head
Flow
Pump
Curve
System
Curve
System Curve
as two way
valves close
Variable flow system
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Q
H
Pump
Curve
System Curve
at design flow
System Curve
at part load
Increased
head loss
Energy savings offset
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Head
Flow
Single
Pump
Pumps in
Parallel
System
Curve
Pumps in parallel
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Horsepower
%
100
90
80
70
60
50
40
30
20
10
00 10 20 30 40 50 60 70 80 90 100
Flow
%
Single Large Pump
Two Parallel
Pumps
Single Parallel
Pump
Parallel pumping power savings
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Theoretical Savings
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100 %
90 %
80 %
70 %
60 %
50%
40 %
30 %
80 %
85 %
80 %
70 %
60 %
50 %
85 %
% Speed Curves
Constant
Efficiency
Curve
% Efficiency
Head,
Feet
GPM
Establishing Efficiency Curves
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750
900 1150 1450 1770
600
900
1150
1450
1770
600
A
B
C
D
E
4500 gpm @ 100 FT, 85.9 %
Variable Speed Efficiencies
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“No Valve” System Curve
Flow
piping head
loss curve
Distribution
Pump
TDH
Overall
system curve
Head
80
60
40
20
110
0
200 400 600 800 1000 1200 1400 1600
0
100
Set Point
25 FT Differential Head
Maintained Across Load
(Set Point)
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Effect of Constant Set Point
piping head
loss curve
Distribution
Pump
TDH
Overall system curve
Head
80
60
40
20
110
0
200 400 600 800 1000 1200 1400 1600
0
Flow
100
Control curve
Set point,
25 FT
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100%
75%
50%
Flow
Head
Control
Curve
Variable
Head
Loss
∆P
P1 P2
Control curve
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Annual
Operating
Cost
($1000/year
@
$0.10/kwh)
50
45
40
35
30
25
20
15
10
05
00
1000 2000 3000 4000 5000
Total Equivalent Pipe Length
(feet)
Single C/S Pump, No Overheading
S
i
n
g
l
e
C
/
S
P
u
m
p
,
2
0
0
%
O
v
e
r
h
e
a
d
e
d
Variable Speed Pump
Large systems, long pipe runs
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Variable Head Loss Ratio
Percent
Design
BHP
% Flow
90
80
70
60
50
40
30
20
10
0 10 100
90
80
70
60
50
40
30
20
100
C/S, Constant Flow System Pump Head Matched to
System at Design Flow
C/S, Variable Flow
V/S, 0% Variable Hd Loss, 100% Constant ∆ Hd
V/S, 25% Variable Hd Loss, 75% Constant ∆ Hd
V/S, 50% Variable Hd Loss, 50% Constant ∆ Hd
V/S, 75% Variable Hd Loss, 25% Constant ∆ Hd
V/S, 100% Variable Hd Loss, 0% Constant ∆ Hd
Base
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Variable Head Ratio w/ Overheading
90
80
70
60
50
40
30
20
10
0 10 100
90
80
70
60
50
40
30
20
100
110
120
130
140
150
Base
Design
HP %
% Full Load
(Design) HP
Pump O’Headed by 150%
Constant Flow, C/S Pump
(3 Way Valve)
Constant Flow, C/S Pump
(3 Way Valve)
C/S Pump
(2 Way Valve)
Pump HD Matched
to System @
Design Flow
* 25/75 Means:
25 % Variable HD Loss
75 % Constant HD Loss
C/S Pump (2 Way Valve)
V/S, 100%
Constant HD
V/S, 25/75*
V/S, 50/50
V/S, 75/25
V/S, 100%
Variable HD
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Locations of Sensor
Where to install the Sensor?
What type of Sensor?
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Chillers
Primary Pumps
Secondary
Pumps
Load
Balancing Valve 2 – Way
Valve
Panel with
PLC & VFD`s
Air -
Separator
Common
Single Point Pressure
Sensing
Single Point Pressure Sensor
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Single Point Pressure Sensor
Is Single Point Pressure Sensor Correct?
Wrong !!
Why?
-Pump is a differential pressure device.
-A single point is only influence by pressure. This is good for booster only.
-In a closed loop system, system pressure rises due to thermal expansion,
pumps will slow down.
-When static pressure decrease, pumps will speed up.
-This is self-defeating since now the pump speed is not influence by the
system load changes, but rather by system water pressure.
-Therefore, single pressure sensor are a misapplication in a closed loop
HVAC system.
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Chillers
Primary Pumps
Secondary
Pumps
Load
Balancing Valve 2 – Way
Valve
Panel with
PLC & VFD`s
Air -
Separator
Common
Primary - Secondary Circuit With Variable Speed
Secondary Pumps
DPT
Single Point Differential Pressure Sensor
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Opening/Closing of 2- Way Valve
-Signal from the sensor, installed at load
regulates the valve opening & closing.
-This way differential across 2-way valve also
changes & accordingly output signal is given to
PLC.
`
`
`
Temperature Sensor
Load
Output to PFU from DPT
2 Way Valve Control
Question:
Can we put the DPT across coil
alone?
Question:
Across the pumps?
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Primary - Secondary Circuit With Variable Speed
Secondary Pumps
Single Point Differential Pressure Sensor
To Maximize energy system, we must maximize the
variable head loss in the system. This is done by locating
the sensor at the most remote zone ( hydraulically) in the
system.
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piping head
loss curve
Distribution
Pump
TDH
Overall
system curve
Ft
Hd
80
60
40
20
110
0
200 400 600 800 1000 1200 1400 1600
0
Flow, gpm
100
Control curve
Set point,
25 FT
System Control Curve
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Variable vs Constant Head Loss
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The “Active Zone”
• Zone set points do not have to be the same.
• Pump controller scans all zones often, comparing process
variable to set point in each case.
• Pumps are controlled to satisfy the worst case.
• What happens to the rest of the zones?
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PFU
PMU
4 – 20 mA
Set Value
From Field
Sensor (DPT)
PFU – Pump Functional Unit
PMU – Pump Management Unit
Basic Concept
Output
To
VFD/Pump
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Chillers
Secondary
Pumps
Balancing Valve
DPT
DPT
Common
Panel with
PLC & VFD`s
Load
Different Sensor Signal To Common PFU Panel
Multi Point Differential Pressure Sensor
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PFU
PMU
Set Value
Multiple Process Signals
From Field Sensors
POSSIBILITY OF MULTIPLE PROCESS
SIGNALS FROM DIFFERENT ZONES
All zones can have different set values
Module
VFD
VFD
Multi Point Differential Pressure Sensor
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PFU
PMU
Set Value
Multiple Process Signals
From Field Sensors
POSSIBILITY OF MULTIPLE PROCESS
SIGNALS FROM DIFFERENT ZONES
All zones can have
different set values
Signal
Comparator
VFD
VFD
Multi Point Differential Pressure Sensor
Signal
Comparator
4 – 20 mA Sig
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HVAC Control System
DPT Signal Comparator
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HVAC Control System
DPT Signal Comparator
- High and Low Signal Selections
- Signal Averaging
- High/Low Limit Control
The module has the addition following features :
1) LED status indications
2) Accepts voltage or milliamp input signal
3) DIP switch-selectable operating modes
4) Accepts 24 VAC/DC power
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HVAC Control System
DPT Signal Comparator
Benefits
1) We are able to supply VFD systems with multiple inputs signals ranges to compete
with our competitors.
2) We are able to use Grundfos PFU 2000 as the main processor to control the full system
operations.
3) We will be minimising outsourcing or external controller in order to serve the HVAC
market.
4) The MM allows us to integrate into the system multiple sensor control at a more cost
effective price.
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Other Types of
Systems
HVAC System
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Chillers
Primary Pumps
Balancing
Valve
Secondary
Pumps
Air -
Separator
Expansion
Tank
Load
Panel with
PLC & VFD`s
Common
DPT
2 – Way
Valve
DPT
Separate System for Each Zone
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Systems In Multi - Zones
Two options:
1. Separate Systems can be used for
different zones. So each zone will
have its own sensor.
2. Signal from different zone sensors is
given to the common PFU and most
deviated signal, from the set point, is
given as output.
Separate System for Each Zone
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Chillers
Primary Pumps
Balancing
Valve
Air -
Separator
Expansion
Tank
Load
Common
DPT
2 – Way
Valve
DPT
VFD pumps For Each Zone
E-pumps
E-pumps
Tertiary Pumping System
Secondary
Pump
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Reverse Return Pumping
Load
Air -
Separator
Chillers
Primary
Pumps
Secondary
Pumps
Balancing Valve
Panel with
PLC & VFD`s
Common DPT
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Reverse Return Pumping
Benefits :
1) Equalize the pressure drops of each zone.
2) Selections of the sensor becomes easier.
3) If load are similar or symmetrical, 1 centrally located sensor
is adequate.
4) As in direct return system, multiple sensor can still provide a
benefit to the end user.
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Type of VFD Systems
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Possible Options of Variable Speed panels
Type ME - Multiple Pumps &
Multiple VFDs.
Type MF - Common VFD for Multiple
Pumps.
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Signal from Field
Sensor(s) (DPT)
Panel with
PFU & PMU
VFD - 1 VFD - 2
Secondary Pumps
System with Multi Pumps & Multi VFDs
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Signal from Field Sensor(s) (DPT)
VFD
Panel with
PFU & PMU
Secondary Pumps
System with Common VFD for All Pumps
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APPROVAL FROM INTERNATIONAL
AGENCIES
Approval from – CE, U/L
Conforms to - Electromagnetic compatibility
(89/336/EEC) to standard EN 50 081 – 1 and EN 50
082 – 2 and Electrical equipment design 73/23/EEC
standard to EN 60 204-1.
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PFU
PMU
Single PMU For Control of 8 Zones/Pumps
PFU
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PFU
PMU
Single PMU For Control of 8 Zones/Pumps
PFU
PFU PFU
The End

chilled-water-system-presentation.pdf

  • 1.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chilled Water System Presentation
  • 2.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Constant Volume Distribution Constant Volume Distribution
  • 3.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Air-conditioning System Components
  • 4.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Constant Volume System Components
  • 5.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Typical 3-way Valve Zone
  • 6.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Full Load Condition
  • 7.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Fully Loaded Coil • Supply water temperature 45°F • Design return water temp. 55°F • Coil design flow 100 GPM • Coil design pressure drop 20 FT • Load (flow x 10°F∆ x 500) 500,000 Btuh • Coil ∆P @ design flow 20 FT • Bypass flow 0 GPM • Bypass ∆P 3-way valve closed • 3-way valve pressure drop 10 FT • Pump flow and head 100 GPM @ 30 FT • Actual return water temp 55 °F
  • 8.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Unloaded Condition
  • 9.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Unloaded Coil • Supply water temperature 45°F • Design return water temp. 55°F • Coil design flow 0 GPM • Coil design pressure drop 3-way valve closed • Load (flow x 10°F∆ x 500) 0.0 Btuh • Coil ∆P @ design flow 0 FT • Bypass flow 100 GPM • Bypass ∆P 20 FT • 3-way valve pressure drop 10 FT • Pump flow and head 100 GPM @ 30 FT • Actual return water temp 45 °F
  • 10.
    COMMERCIAL BUILDING SERVICESFLOW THINKING So What? • When the load on the coil is zero, the valve is returning “unused” chilled water at essentially supply temperature. • Cold return water “unloads” the chillers, causing them to operate inefficiently.
  • 11.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Part Load Condition
  • 12.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Partially Loaded Coil • Supply water temperature 45°F • Design return water temp. 55°F • Coil design flow 50 GPM • Coil design pressure drop 20 FT • Load (flow x 10°F∆ x 500) 250,000 Btuh • Coil ∆P @ design flow 5 FT • Bypass flow ??? GPM • Bypass ∆P 3-way partially closed • 3-way valve pressure drop 10 FT • Pump flow and head ??? GPM @ 30 FT • Actual return water temp ?? °F
  • 13.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 125 100 75 50 25 0 % Valve Stroke 25 50 75 100 % Flow 1/2 Through Coil 1/2 Through Bypass Full Flow Through Coil Full Flow Through Bypass 3-way Valve Characteristic
  • 14.
    COMMERCIAL BUILDING SERVICESFLOW THINKING What’s Really Happening?
  • 15.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Coil with 3-way Valve at Mid-position • Supply water temperature 45 °F • Design return water temp. 55 °F • Load (flow x 10°F∆ x 500) 250,000 Btuh • Coil design pressure drop 20 FT • Coil flow 62.5 GPM • Coil ∆P @ 62.5% flow 7.8 FT • Coil leaving water temp 53 °F • Bypass flow 62.5 GPM • Bypass ∆P 7.8 FT • 3-way valve pressure drop 10 FT • Pump flow and head 125 GPM @ 30 FT • Actual return water temp 49 °F (62.5 GPM @ 53 °F+ 62.5 GPM @ 45 °F)
  • 16.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Head2 = Head1(Flow2/ Flow1)2 Head2 = 20(.625/1)2 Head2 = 20(.3906 ) Head2 = 7.8
  • 17.
    COMMERCIAL BUILDING SERVICESFLOW THINKING ∆T = Load/ Flow X 500 ∆T = 250,000/62.5 X 500 ∆T = 8 Therefore, LWTcoil = 45 + 8 = 53
  • 18.
    COMMERCIAL BUILDING SERVICESFLOW THINKING RWT = (Flow1 X EWT + Flow2 X LWT)/ Flow1 + 2 RWT = (62.5 X 45 + 62.5 X 53)/125 RWT = 49
  • 19.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 3-way Valve in Mid Position
  • 20.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 1.Low return water temperatures. 2.Robs chilled water from other coils at part load conditions. 3.Increases flow in primary piping. 4.Adds additional chillers on line. 5.Chiller performance is reduced. 3-way Valve System Deficiencies
  • 21.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 1.1 20 30 40 50 60 70 80 90 100 10 1.0 0.9 0.8 0.7 0.6 0.5 KW per Ton Percent Load Chiller Performance Curve
  • 22.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Pump Sizing • Select for full chiller flow • Head must be adequate for: – Chiller evaporator – Longest circuit – Coil – Three way valve – Air separator
  • 23.
    COMMERCIAL BUILDING SERVICESFLOW THINKING System Configuration Constant Volume
  • 24.
  • 25.
  • 26.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary – Secondary System Primary – Includes Chillers & Primary Pump. Circuit Constant water flow through the chiller is maintained and chilled water is produced Secondary – Chilled water is circulated to the Circuit demand area (load) by using Secondary pumps. Variable Volume Constant Speed
  • 27.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PRIMARY - SECONDARY
  • 28.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Other Famous Names of Primary- Secondary Primary – Production Loop Secondary – Distribution Loop
  • 29.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Fundamental Idea
  • 30.
    COMMERCIAL BUILDING SERVICESFLOW THINKING No Secondary Flow
  • 31.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary = Secondary
  • 32.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary > Secondary
  • 33.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary < Secondary
  • 34.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Control Valve in Secondary
  • 35.
    COMMERCIAL BUILDING SERVICESFLOW THINKING • Use the flow of the largest chiller – Chiller staging at half of this flow is common • Head loss in common <1 1/2 ft – Distribution pipe size is often used where reductions would be inconvenient • Three pipe diameters between tees – Excessive length increases total head loss • Low velocities in system piping Common Pipe Design Criteria
  • 36.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Variable flow through coil Constant flow through system Three Way Valve Variable flow through coil Variable flow through system Two Way Valve Control Valve in Secondary
  • 37.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PRIMARY – SECONDARY CIRCUIT Variable Volume Constant Speed
  • 38.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Head F1 F2 F3 H1 H2 H3 Flow Control Valves Change the Secondary System Curve
  • 39.
    COMMERCIAL BUILDING SERVICESFLOW THINKING % Flow 125 100 75 50 25 150 25 50 75 100 HD Varying differential pressure absorbed by control valve System resistance TDH of pump Pump curve Head Absorbed by 2-way Valves
  • 40.
    COMMERCIAL BUILDING SERVICESFLOW THINKING HP 125 100 75 50 25 150 25 50 75 100 % Design Flow Primary Pumps = V/V Secondary Pumps + Constant Flow Primary Pumps, only Pump Horsepower Comparison
  • 41.
    COMMERCIAL BUILDING SERVICESFLOW THINKING % Flow 90 80 70 60 50 40 30 20 10 0 10 100 90 80 70 60 50 40 30 20 100 110 120 130 140 150 Base Design HP % % Full Load (Design) HP Pump Over-haded by 150% Constant Flow, C/S Pump (3 Way Valve) Constant Flow, C/S Pump (3 Way Valve) C/S Pump (2 Way Valve) Pump HD Matched to System @ Design Flow C/S Pump (2 W ay Valve) Constant vs Variable Volume
  • 42.
  • 43.
  • 44.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Production = Distribution
  • 45.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Distribution > Production
  • 46.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Production > Distribution
  • 47.
    COMMERCIAL BUILDING SERVICESFLOW THINKING “Loading” a Chiller • A chiller is a heat transfer device. Like most equipment, it is most efficient at full load. • To “load” a chiller means: – Supply it with its rated flow of water – Insure that water is warm enough to permit removal of rated Btu without freezing the water
  • 48.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chiller Performance Curve 1.1 20 30 40 50 60 70 80 90 100 10 1.0 0.9 0.8 0.7 0.6 0.5 KW per Ton Percent Load
  • 49.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Check Valve in Common?
  • 50.
    COMMERCIAL BUILDING SERVICESFLOW THINKING What can we do?
  • 51.
    COMMERCIAL BUILDING SERVICESFLOW THINKING What else can we do? Reset Supply Temperature • Lower chiller set point when mixing occurs to maintain a constant temperature to the system. • Expect increases in cost of chiller operation at lower set point: 1-3% per degree of reset. • Delays start of the next chiller.
  • 52.
    COMMERCIAL BUILDING SERVICESFLOW THINKING What else can we do? • Coils that are selected at higher supply temperatures will not be impaired by small changes. • Loads that require fixed temperatures may use a small chiller to reverse the effects of mixing.
  • 53.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Multiple Chillers
  • 54.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 60/40 Chiller Split to Help Minimize Low Part Load Operation
  • 55.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 0-10 30-40 60-70 90-100 0 5 10 15 20 25 30 0-10 30-40 60-70 90-100 % Time % Load Typical Load Profile
  • 56.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Three Unequally Sized Chillers
  • 57.
    COMMERCIAL BUILDING SERVICESFLOW THINKING % Load Time Approaching Flow = Load
  • 58.
  • 59.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Two Pipe Direct Return
  • 60.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Two Pipe Reverse Return
  • 61.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary Pumping. • Simplest to install. • Simplest to operate. • Flexible in design for present and future. • Efficient to operate. • May over-pressurize near zones.
  • 62.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary-Tertiary
  • 63.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary-Tertiary Pumping. • Best piping flexibility. • Best expansion flexibility. • Provides hydraulic decoupling. • Efficient to operate. • May require added horsepower. • Requires additional pumps and piping. • Increased controls complexity.
  • 64.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary-Tertiary Hybrid
  • 65.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary-Tertiary Hybrid Pumping. • Low present horsepower. • Low future horsepower. • Good piping flexibility. • Good expansion flexibility. • Provides hydraulic decoupling. • May require added horsepower • Requires additional pumps and piping. • Increased controls complexity.
  • 66.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary Zone Pumping
  • 67.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary-Secondary Zone Pumping. • Low ‘built out’ horsepower. • Low system head. • Increased control complexity. • Present horsepower total higher due to future needs. • Present pumps sized for future requirements. • Difficult to apply in retrofits projects.
  • 68.
  • 69.
  • 70.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Why Do We Need Variable Speed Secondary Pumps ??? •For Energy Saving…. •For better & optimise operation….
  • 71.
    COMMERCIAL BUILDING SERVICESFLOW THINKING How Do We Achieve This Reduction In Power Consumption ?? By Using Variable Frequency Drive and Logic controller with the Secondary Pumps….
  • 72.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Power Comparison at Reduced Speed
  • 73.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Basic Law which helps in achieving this – Affinity law 1. Flow2 = Flow1(Speed2/ Speed1) 2. Head2 = Head1(Speed2/ Speed1)2 3. BKW2 = BKW1(Speed2/ Speed1)3 If Diameter of Impeller is to be trimmed then instead of speed the same can be used in above formulas.
  • 74.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 0 50 100 150 200 250 300 350 400 450 50 100 150 200 250 300 350 400 450 500 Motor Horsepower Annual Operating Cost $1000 $0.10/kWh Operating Cost
  • 75.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Head Flow Pump Curve System Curve System Curve as two way valves close Variable flow system
  • 76.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Q H Pump Curve System Curve at design flow System Curve at part load Increased head loss Energy savings offset
  • 77.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Head Flow Single Pump Pumps in Parallel System Curve Pumps in parallel
  • 78.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Horsepower % 100 90 80 70 60 50 40 30 20 10 00 10 20 30 40 50 60 70 80 90 100 Flow % Single Large Pump Two Parallel Pumps Single Parallel Pump Parallel pumping power savings
  • 79.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Theoretical Savings
  • 80.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 100 % 90 % 80 % 70 % 60 % 50% 40 % 30 % 80 % 85 % 80 % 70 % 60 % 50 % 85 % % Speed Curves Constant Efficiency Curve % Efficiency Head, Feet GPM Establishing Efficiency Curves
  • 81.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 750 900 1150 1450 1770 600 900 1150 1450 1770 600 A B C D E 4500 gpm @ 100 FT, 85.9 % Variable Speed Efficiencies
  • 82.
    COMMERCIAL BUILDING SERVICESFLOW THINKING “No Valve” System Curve Flow piping head loss curve Distribution Pump TDH Overall system curve Head 80 60 40 20 110 0 200 400 600 800 1000 1200 1400 1600 0 100 Set Point 25 FT Differential Head Maintained Across Load (Set Point)
  • 83.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Effect of Constant Set Point piping head loss curve Distribution Pump TDH Overall system curve Head 80 60 40 20 110 0 200 400 600 800 1000 1200 1400 1600 0 Flow 100 Control curve Set point, 25 FT
  • 84.
    COMMERCIAL BUILDING SERVICESFLOW THINKING 100% 75% 50% Flow Head Control Curve Variable Head Loss ∆P P1 P2 Control curve
  • 85.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Annual Operating Cost ($1000/year @ $0.10/kwh) 50 45 40 35 30 25 20 15 10 05 00 1000 2000 3000 4000 5000 Total Equivalent Pipe Length (feet) Single C/S Pump, No Overheading S i n g l e C / S P u m p , 2 0 0 % O v e r h e a d e d Variable Speed Pump Large systems, long pipe runs
  • 86.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Variable Head Loss Ratio Percent Design BHP % Flow 90 80 70 60 50 40 30 20 10 0 10 100 90 80 70 60 50 40 30 20 100 C/S, Constant Flow System Pump Head Matched to System at Design Flow C/S, Variable Flow V/S, 0% Variable Hd Loss, 100% Constant ∆ Hd V/S, 25% Variable Hd Loss, 75% Constant ∆ Hd V/S, 50% Variable Hd Loss, 50% Constant ∆ Hd V/S, 75% Variable Hd Loss, 25% Constant ∆ Hd V/S, 100% Variable Hd Loss, 0% Constant ∆ Hd Base
  • 87.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Variable Head Ratio w/ Overheading 90 80 70 60 50 40 30 20 10 0 10 100 90 80 70 60 50 40 30 20 100 110 120 130 140 150 Base Design HP % % Full Load (Design) HP Pump O’Headed by 150% Constant Flow, C/S Pump (3 Way Valve) Constant Flow, C/S Pump (3 Way Valve) C/S Pump (2 Way Valve) Pump HD Matched to System @ Design Flow * 25/75 Means: 25 % Variable HD Loss 75 % Constant HD Loss C/S Pump (2 Way Valve) V/S, 100% Constant HD V/S, 25/75* V/S, 50/50 V/S, 75/25 V/S, 100% Variable HD
  • 88.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Locations of Sensor Where to install the Sensor? What type of Sensor?
  • 89.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chillers Primary Pumps Secondary Pumps Load Balancing Valve 2 – Way Valve Panel with PLC & VFD`s Air - Separator Common Single Point Pressure Sensing Single Point Pressure Sensor
  • 90.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Single Point Pressure Sensor Is Single Point Pressure Sensor Correct? Wrong !! Why? -Pump is a differential pressure device. -A single point is only influence by pressure. This is good for booster only. -In a closed loop system, system pressure rises due to thermal expansion, pumps will slow down. -When static pressure decrease, pumps will speed up. -This is self-defeating since now the pump speed is not influence by the system load changes, but rather by system water pressure. -Therefore, single pressure sensor are a misapplication in a closed loop HVAC system.
  • 91.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chillers Primary Pumps Secondary Pumps Load Balancing Valve 2 – Way Valve Panel with PLC & VFD`s Air - Separator Common Primary - Secondary Circuit With Variable Speed Secondary Pumps DPT Single Point Differential Pressure Sensor
  • 92.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Opening/Closing of 2- Way Valve -Signal from the sensor, installed at load regulates the valve opening & closing. -This way differential across 2-way valve also changes & accordingly output signal is given to PLC. ` ` ` Temperature Sensor Load Output to PFU from DPT 2 Way Valve Control
  • 93.
    Question: Can we putthe DPT across coil alone?
  • 94.
  • 95.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Primary - Secondary Circuit With Variable Speed Secondary Pumps Single Point Differential Pressure Sensor To Maximize energy system, we must maximize the variable head loss in the system. This is done by locating the sensor at the most remote zone ( hydraulically) in the system.
  • 96.
    COMMERCIAL BUILDING SERVICESFLOW THINKING piping head loss curve Distribution Pump TDH Overall system curve Ft Hd 80 60 40 20 110 0 200 400 600 800 1000 1200 1400 1600 0 Flow, gpm 100 Control curve Set point, 25 FT System Control Curve
  • 97.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Variable vs Constant Head Loss
  • 98.
    COMMERCIAL BUILDING SERVICESFLOW THINKING The “Active Zone” • Zone set points do not have to be the same. • Pump controller scans all zones often, comparing process variable to set point in each case. • Pumps are controlled to satisfy the worst case. • What happens to the rest of the zones?
  • 99.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PFU PMU 4 – 20 mA Set Value From Field Sensor (DPT) PFU – Pump Functional Unit PMU – Pump Management Unit Basic Concept Output To VFD/Pump
  • 100.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chillers Secondary Pumps Balancing Valve DPT DPT Common Panel with PLC & VFD`s Load Different Sensor Signal To Common PFU Panel Multi Point Differential Pressure Sensor
  • 101.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PFU PMU Set Value Multiple Process Signals From Field Sensors POSSIBILITY OF MULTIPLE PROCESS SIGNALS FROM DIFFERENT ZONES All zones can have different set values Module VFD VFD Multi Point Differential Pressure Sensor
  • 102.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PFU PMU Set Value Multiple Process Signals From Field Sensors POSSIBILITY OF MULTIPLE PROCESS SIGNALS FROM DIFFERENT ZONES All zones can have different set values Signal Comparator VFD VFD Multi Point Differential Pressure Sensor Signal Comparator 4 – 20 mA Sig
  • 103.
    COMMERCIAL BUILDING SERVICESFLOW THINKING HVAC Control System DPT Signal Comparator
  • 104.
    COMMERCIAL BUILDING SERVICESFLOW THINKING HVAC Control System DPT Signal Comparator - High and Low Signal Selections - Signal Averaging - High/Low Limit Control The module has the addition following features : 1) LED status indications 2) Accepts voltage or milliamp input signal 3) DIP switch-selectable operating modes 4) Accepts 24 VAC/DC power
  • 105.
    COMMERCIAL BUILDING SERVICESFLOW THINKING HVAC Control System DPT Signal Comparator Benefits 1) We are able to supply VFD systems with multiple inputs signals ranges to compete with our competitors. 2) We are able to use Grundfos PFU 2000 as the main processor to control the full system operations. 3) We will be minimising outsourcing or external controller in order to serve the HVAC market. 4) The MM allows us to integrate into the system multiple sensor control at a more cost effective price.
  • 106.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Other Types of Systems HVAC System
  • 107.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chillers Primary Pumps Balancing Valve Secondary Pumps Air - Separator Expansion Tank Load Panel with PLC & VFD`s Common DPT 2 – Way Valve DPT Separate System for Each Zone
  • 108.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Systems In Multi - Zones Two options: 1. Separate Systems can be used for different zones. So each zone will have its own sensor. 2. Signal from different zone sensors is given to the common PFU and most deviated signal, from the set point, is given as output. Separate System for Each Zone
  • 109.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Chillers Primary Pumps Balancing Valve Air - Separator Expansion Tank Load Common DPT 2 – Way Valve DPT VFD pumps For Each Zone E-pumps E-pumps Tertiary Pumping System Secondary Pump
  • 110.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Reverse Return Pumping Load Air - Separator Chillers Primary Pumps Secondary Pumps Balancing Valve Panel with PLC & VFD`s Common DPT
  • 111.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Reverse Return Pumping Benefits : 1) Equalize the pressure drops of each zone. 2) Selections of the sensor becomes easier. 3) If load are similar or symmetrical, 1 centrally located sensor is adequate. 4) As in direct return system, multiple sensor can still provide a benefit to the end user.
  • 112.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Type of VFD Systems
  • 113.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Possible Options of Variable Speed panels Type ME - Multiple Pumps & Multiple VFDs. Type MF - Common VFD for Multiple Pumps.
  • 114.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Signal from Field Sensor(s) (DPT) Panel with PFU & PMU VFD - 1 VFD - 2 Secondary Pumps System with Multi Pumps & Multi VFDs
  • 115.
    COMMERCIAL BUILDING SERVICESFLOW THINKING Signal from Field Sensor(s) (DPT) VFD Panel with PFU & PMU Secondary Pumps System with Common VFD for All Pumps
  • 116.
    COMMERCIAL BUILDING SERVICESFLOW THINKING APPROVAL FROM INTERNATIONAL AGENCIES Approval from – CE, U/L Conforms to - Electromagnetic compatibility (89/336/EEC) to standard EN 50 081 – 1 and EN 50 082 – 2 and Electrical equipment design 73/23/EEC standard to EN 60 204-1.
  • 117.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PFU PMU Single PMU For Control of 8 Zones/Pumps PFU
  • 118.
    COMMERCIAL BUILDING SERVICESFLOW THINKING PFU PMU Single PMU For Control of 8 Zones/Pumps PFU PFU PFU
  • 119.