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Fundamentals of Water System Design - ibse.hkibse.hk/cpd/water-system/WSD_Chp_7.pdfAs a manual valve...

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© 2007 ASHRAE Hong Kong Chapter Slide 1 Fundamentals of Water System Design 17, 18, 24, 25 January 2007 ASHRAE Hong Kong Chapter Technical Workshop
Transcript
  • © 2007 ASHRAE Hong Kong Chapter Slide 1

    Fundamentals of Water System Design

    17, 18, 24, 25 January 2007

    ASHRAE Hong Kong Chapter Technical Workshop

  • © 2007 ASHRAE Hong Kong Chapter Slide 2

    Chapter 7:Piping System Development

    •Piping System design•Direct Return Analysis•Reverse Return Analysis•Primary-Secondary Analysis•Type of Pumps and Valves•Primary-Secondary Application Study•Antifreeze Solutions for Low Temperature Application•Pumping Design Factors

  • © 2007 ASHRAE Hong Kong Chapter Slide 3

    Piping System Design

  • © 2007 ASHRAE Hong Kong Chapter Slide 4

    Piping System Design Flowchart

  • © 2007 ASHRAE Hong Kong Chapter Slide 5

    Typical Building Layout

    Building usage•Hotel •Shopping Mall•Services apartment•Office•Mechanical floor

  • © 2007 ASHRAE Hong Kong Chapter Slide 6

    Piping System Design Flowchart

  • © 2007 ASHRAE Hong Kong Chapter Slide 7

    Determine Loads andConsult References

  • © 2007 ASHRAE Hong Kong Chapter Slide 8

    Piping System Design Flowchart

  • © 2007 ASHRAE Hong Kong Chapter Slide 9

    Determine the system to be used and develop a concept for part-load control

    SystemFCU + PAUVAV systemAHU (all air system)others

    PlantroomWater cooled chillersAir cooled chillersSplit system

    ControlApplicationOperation hourZoneIAQ/Energy consideration

    O&MMaintenance and Services

  • © 2007 ASHRAE Hong Kong Chapter Slide 10

    Piping System Design Flowchart

  • © 2007 ASHRAE Hong Kong Chapter Slide 11

    Develop Piping/PumpingSystem Concept

    Chiller combination• Full load/Part load/• Emergency• Standby

    Pumping system• Primary –Secondary• Variable Primary sys

    Water distribution system• Direct return• Reverse return• Direct + reverse return

  • © 2007 ASHRAE Hong Kong Chapter Slide 12

    Piping System Design Flowchart

  • © 2007 ASHRAE Hong Kong Chapter Slide 13

    Piping System Design Flowchart

  • © 2007 ASHRAE Hong Kong Chapter Slide 14

    What is Direct Return and Reverse Return?

    Coil Coil Coil Coil Coil

  • © 2007 ASHRAE Hong Kong Chapter Slide 15

    What is Direct Return and Reverse Return?

    CoilCoil Coil Coil Coil

    CoilCoil Coil Coil Coil

    Direct Return

    Reverse Return

  • © 2007 ASHRAE Hong Kong Chapter Slide 16

    Load System Example

  • © 2007 ASHRAE Hong Kong Chapter Slide 17

    Piping Detail at Load Coil

  • © 2007 ASHRAE Hong Kong Chapter Slide 18

    Friction Loss, Medium Steel Pipe

  • © 2007 ASHRAE Hong Kong Chapter Slide 19

    Direct Return Piping Layout

  • © 2007 ASHRAE Hong Kong Chapter Slide 20

    Direct Return System

    Flow

    Unit 3

    Unit 1

    Unit 2

    Unit 4

    A

    BB'

    CC'

    D D'

    EE'

    F

    Piping pressure drop

    Unit 1 80 kPaUnit 2 98 kPaUnit 3 108 kPaUnit 4 90 kPa

  • © 2007 ASHRAE Hong Kong Chapter Slide 21

    Direct Return System

    Flow

    Unit 3

    Unit 1

    Unit 2

    Unit 4

    A

    BB'

    CC'

    D D'

    EE'

    F

    Piping pressure drop and flow

    Unit 1 80 kPa 5.8 L/sUnit 2 98 kPa 5.2 L/sUnit 3 108 kPa 5 L/sUnit 4 90 kPa 5.5 L/s

    Design flow: 5L/s

    Assume coil pressure drop: 30kPa

  • © 2007 ASHRAE Hong Kong Chapter Slide 22

    Direct Return System

    Flow

    Unit 3

    Unit 1

    Unit 2

    Unit 4

    A

    BB'

    CC'

    D D'

    EE'

    F

    Design flow: 5L/s

    Assume coil pressure drop: 15kPa

    Piping pressure drop and flow

    Unit 1 65 kPa 6 L/sUnit 2 83 kPa 5.3 L/sUnit 3 93 kPa 5 L/sUnit 4 75 kPa 5.6 L/s

  • © 2007 ASHRAE Hong Kong Chapter Slide 23

    Reverse Return Piping Layout

  • © 2007 ASHRAE Hong Kong Chapter Slide 24

    Reverse Return System

    Unit 4Unit 1 Unit 2 Unit 3

    A B C D E

    F

    B' C' D' E'

    Piping pressure drop and flow

    Unit 1 139 kPa 5.36 L/sUnit 2 160 kPa 5 L/sUnit 3 160 kPa 5 L/sUnit 4 139 kPa 5.36 L/s

    Total 20.72 L/s

    Design flow: 5L/s

    Assume coil pressure drop: 30kPa

  • © 2007 ASHRAE Hong Kong Chapter Slide 25

    Reverse Return System

    Unit 4Unit 1 Unit 2 Unit 3

    A B C D E

    F

    B' C' D' E'

    Design flow: 5L/s

    Piping pressure drop and flow

    Unit 1 124 kPa 5.41 L/sUnit 2 145 kPa 5 L/sUnit 3 145 kPa 5 L/sUnit 4 124 kPa 5.41 L/s

    Total 20.82 L/sAssume coil pressure drop: 15kPa

  • © 2007 ASHRAE Hong Kong Chapter Slide 26

    Comparison

    Coil Pressure drop = 30kPa Coil Pressure drop = 30kPa

    flow flowUnit 1 80 kPa 5.8 L/s Unit 1 139 kPa 5.36 L/sUnit 2 98 kPa 5.2 L/s Unit 2 160 kPa 5 L/sUnit 3 108 kPa 5 L/s Unit 3 160 kPa 5 L/sUnit 4 90 kPa 5.5 L/s Unit 4 139 kPa 5.36 L/s

    Total 21.5 L/s Total 20.72 L/sPump kw = 2.3 kw Pump kw = 3.3 kw

    Coil Pressure drop = 15kPa Coil Pressure drop = 15kPa

    flow flowUnit 1 65 kPa 6 L/s Unit 1 124 kPa 5.41 L/sUnit 2 83 kPa 5.3 L/s Unit 2 145 kPa 5 L/sUnit 3 93 kPa 5 L/s Unit 3 145 kPa 5 L/sUnit 4 75 kPa 5.6 L/s Unit 4 124 kPa 5.41 L/s

    Total 21.9 L/s Total 20.82 L/s

    Pump kw = 2.1 kw Pump kw =3.1 kw

    Direct Return System Reverse Return System

  • © 2007 ASHRAE Hong Kong Chapter Slide 27

    Piping Detail: Load Coil Primary-Secondary

  • © 2007 ASHRAE Hong Kong Chapter Slide 28

    Primary-Secondary Piping

  • © 2007 ASHRAE Hong Kong Chapter Slide 29

    Primary/Secondary system

    Coil Pressure drop = 30kPa

    flowUnit 1 47.3 kPa 8 L/sUnit 2 65.3 kPa 5.8 L/sUnit 3 75.3 kPa 5 L/sUnit 4 57.3 kPa 6.6 L/s

    Total 25.4 L/sPrimary Pump kw = 1.9 kwSecondary Pump kw = 4 x 0.2 = 0.8 kw

    Total Pump kw = 2.7 kw

    Compare to direct return system, pump kw = 2.1 kw

  • © 2007 ASHRAE Hong Kong Chapter Slide 30

    Purpose of Pumping Systems

    Transport sufficient water through the piping system

    at the minimum differential pressurethat will satisfy all connected loads at

    different load conditions

  • © 2007 ASHRAE Hong Kong Chapter Slide 31

    Why balanced flow is important?

    Drawback of unbalanced system: Cannot meet the design flow and capacity at the air terminal unit Waste energyShort circuit (hydronic)Chiller hunting

  • © 2007 ASHRAE Hong Kong Chapter Slide 32

    How to balance the system?

    Add Balancing DeviceFixed orificeManual balancing valvesConstant flow valve Pressure Independent control valve

    Remember

    Flow rate Q = Cv ‧A ‧√ΔP

  • © 2007 ASHRAE Hong Kong Chapter Slide 33

    Method 1 & 2The manual balancing valve

    (Similar as orifice)

    Is an adjustable orifice - not a flow controller.Must be manually adjusted according to pressure differential.Introduces manual error into system performance.

  • © 2007 ASHRAE Hong Kong Chapter Slide 34

    The manual balancing valve adjustment

    Requires special equipment and training on procedure.Have to access valves on-site in ceilings etc. Commissioning after installation, system filling, & pump commissioning.Requires time for commissioning.Difficult to re-balance if the project completion will be in staged or modified

  • © 2007 ASHRAE Hong Kong Chapter Slide 35

    The manual balancing act

    As a manual valve is adjusted, it not only changes the coil flow, it changes the total flow in the common pipe. The pressure differentials and flows across parallel circuits are upset and then must be re-adjusted.

    - +- + + +

    Valve throttled & flow reduced

    Common pipe flow &

    pressure loss will be reduced

    Pressure differential & flow across the valve increased

    1

    It will be a static system, cannot response to a dynamic or variable flow system

  • © 2007 ASHRAE Hong Kong Chapter Slide 36

    BranchesRisers

    Branch and risers in Manual balancing system

    Don’t forget those additional regulating valves:

  • © 2007 ASHRAE Hong Kong Chapter Slide 37

    Method 1 & 2The manual balancing valve

    (Similar as orifice)

    After commissioning or adjustment of the manual balancing valves, the Cv and A (area) of each valve is fixed.The flow rate will then be pressure dependent.

    Flow rate Q = Cv ‧A ‧√ΔP

  • © 2007 ASHRAE Hong Kong Chapter Slide 38

    Method 3Constant Flow valve

    CharacteristicBelow the control range the cartridge is a fixed orifice & flow can be varied by a 2 way control valve In the dP control range, flow is limited to design +/-5%

    Flow

    Differential Pressure (dP)

    Range Minimum

    kPaD

    Design Maximum

    Range Maximum

    kPaD

    00

  • © 2007 ASHRAE Hong Kong Chapter Slide 39

    By using constant flow valve

    Either in 2-way or 3-way control valves system

    PROLess valves (not required in branch and riser)Reduce T&Cwork and time

    CONFlow modulating depend on control valves in part loadNot fully dynamic balancing system

  • © 2007 ASHRAE Hong Kong Chapter Slide 40

    Method 3Constant Flow valve

    After installation of the constant flow valves, the (Cv ‧A)of each valve will compensate the variation of the (√ΔP).The flow rate will then be kept constant.

    However, it is suitable for the constant flow application like,Constant flow chillers and pumpsMost of the FCU application (constant flow)

    Flow rate Q = Cv ‧A ‧√ΔP

  • © 2007 ASHRAE Hong Kong Chapter Slide 41

    Method 4Pressure Independent Control Valve

    Pressure independent control valveFunction:-1. System pressure independent2. Flow rate Modulating control3. Pre-set maximum flow

  • © 2007 ASHRAE Hong Kong Chapter Slide 42

    Pressure Independent Control Valve Characteristic

    Pre-set Maximum flow for each AHUFlow rate varies according to the temp

    controller or DDC input signal (2-10V or 4-20mA)

    valve will then hold the flow rate constant regardless of the change in pressure differential.

  • © 2007 ASHRAE Hong Kong Chapter Slide 43

    System using Pressure Independent Control valve

    CharacteristicLess valves, combine the control function.Elimination of branch balancing valves & reverse return pipe work.Valve authority = 100%Pre-set the max flow of each AHU and save lot of time in commissioning work.No need to re-balance the system even the project is staged or modified.

  • © 2007 ASHRAE Hong Kong Chapter Slide 44

    Method 4Pressure Independent Control Valve

    After installation of the pressure independent control valves, the (Cv ‧A) of each valve will compensate the variation of the (√ΔP) at various load at any time.The flow rate will then be pressure independent, only temperature / load dependent

    It is suitable for most of the modulating control applications,AHUsPrecise flow control FCUs

    Flow rate Q 1% Q 100% = (Cv ‧A) 1-100‧√ΔP

  • © 2007 ASHRAE Hong Kong Chapter Slide 45

    The pumping system will be required to operate under various load conditionsVariable flow system differential pressures throughout the system will be dynamic.Hydronic systems should be hydraulically modeled to design for full load and part load performance

    What happen when the system is in part load?

  • © 2007 ASHRAE Hong Kong Chapter Slide 46

    System at Part load

    Coil Coil Coil Coil Coil

    OFF

    60%load

    83%load

    31%load

    100%load

    ★Flow rate required for each AHU or branch is varying all the time

  • © 2007 ASHRAE Hong Kong Chapter Slide 47

    Valve must be perfectly sized to provide exact resistance for pressure differential when fully open to provide design flow

    What happen in typical Control valve for part load condition

  • © 2007 ASHRAE Hong Kong Chapter Slide 48

    Typical Control Valve is Pressure Dependence

    Standard 2 way valves vary opening area only – but not flow.As pressure differential varies, the flow varies.

    Q = dP * Orifice constant

    Typical Control valve for part load

  • © 2007 ASHRAE Hong Kong Chapter Slide 49

    Once below design flow, as each 2-way control valve reduces flow, it increases the pressure differential and flows across parallel circuits.

    T

    Time

    System pressure varies affect the flowrate passing through valves and coilsThe temperature is then altered due to the pressure fluctuation.

    Control valve for part load

  • © 2007 ASHRAE Hong Kong Chapter Slide 50

    A system using typical control valve and manual balancing valve

    VFD Coil

    Coil

    DP

    6.3 L/s35 kPa

    6.3 L/s35 kPa

    35 kPa192 kPa

    35 kPa12 kPa

    82 kPa262 kPa310 kPa

    PUMP Coil #1 REMOTE LOAD0

    480PR

    ESSU

    RE

    kPa

    Typical control valve

    Manual balancing valve

  • © 2007 ASHRAE Hong Kong Chapter Slide 51

    A system using typical control valve and manual balancing valve

    PRESSURE DROP OF CONTROL VALVE AND MANUAL BALANCING VALVE

    AT VARIOUS LOAD CONDITIONSFull Flow

    75% Flow

    50% Flow

    25% Flow

    10% Flow

    Branch Flow (L/s) 6.3 4.7 3.2 1.6 0.6

    Branch ∆P (kPa) 262 262 262 262 262

    Coil ∆P (kPa) 35 19 9 2 0.7Manual, Balancing Valve ∆P (kPa)

    192 109 48 12 2

    Control Valve ∆P (kPa) 35 134 205 248 259

    As ∆P across typical control valve increase

    seriously during part load

    Waste energy

  • © 2007 ASHRAE Hong Kong Chapter Slide 52

    Balancing Considerationsin Variable Flow Systems

    • Too large a balancing valve pressure drop will affect the performance and flow characteristic of the control valve.• ASHRAE 2003 Applications Handbook, page 37.8

  • © 2007 ASHRAE Hong Kong Chapter Slide 53

    Options to Consider• No manual balancing valves at coils• Automatic differential pressure control to reduce

    differential pressure• Pressure-independent control valves (with Flowrate

    pre-set function)

    Options NOT to Consider:• Balancing valves for variable speed pumps

    Balancing Considerationsin Variable Flow Systems

  • © 2007 ASHRAE Hong Kong Chapter Slide 54

    Four-Zone Heating System

  • © 2007 ASHRAE Hong Kong Chapter Slide 55

    Typical Building Layout

    Building usage•Hotel •Shopping Mall•Services apartment•Office•Mechanical floor

  • © 2007 ASHRAE Hong Kong Chapter Slide 56

    Primary-Secondary Pumping, Four-Zone Heating System

  • © 2007 ASHRAE Hong Kong Chapter Slide 57

    Primary-Secondary Bridge Energy

  • © 2007 ASHRAE Hong Kong Chapter Slide 58

    Primary-Secondary Pumping, Four-Zone Heating System

  • © 2007 ASHRAE Hong Kong Chapter Slide 59

    Coil With Glycol Heat Exchanger and Pump

  • © 2007 ASHRAE Hong Kong Chapter Slide 60

    Pumped Coil WithFace-Bypass Dampers

  • © 2007 ASHRAE Hong Kong Chapter Slide 61

    Specific Heats ofAqueous Ethylene Glycol

  • © 2007 ASHRAE Hong Kong Chapter Slide 62

    Specific Heats ofAqueous Propylene Glycol

  • © 2007 ASHRAE Hong Kong Chapter Slide 63

    One-Shot Chemical Feeder

  • © 2007 ASHRAE Hong Kong Chapter Slide 64

    Thank you

    Edward Tsui

    Email: [email protected]

    Fundamentals of Water System DesignChapter 7:�Piping System DevelopmentPiping System DesignPiping System Design FlowchartTypical Building LayoutPiping System Design FlowchartDetermine Loads and�Consult ReferencesPiping System Design FlowchartDetermine the system to be used and develop a concept for part-load controlPiping System Design FlowchartDevelop Piping/Pumping�System ConceptPiping System Design FlowchartPiping System Design FlowchartWhat is Direct Return and Reverse Return?What is Direct Return and Reverse Return?Load System ExamplePiping Detail at Load CoilFriction Loss, Medium Steel PipeDirect Return Piping LayoutDirect Return SystemDirect Return SystemDirect Return SystemReverse Return Piping LayoutReverse Return SystemReverse Return SystemComparisonPiping Detail: Load Coil Primary-SecondaryPrimary-Secondary PipingPrimary/Secondary systemPurpose of Pumping SystemsWhy balanced flow is important?How to balance the system?Method 1 & 2� The manual balancing valve�(Similar as orifice)The manual balancing valve adjustmentThe manual balancing actBranch and risers in Manual balancing systemMethod 1 & 2� The manual balancing valve�(Similar as orifice)Method 3�Constant Flow valveBy using constant flow valveMethod 3�Constant Flow valveMethod 4�Pressure Independent Control ValvePressure Independent Control Valve CharacteristicSystem using �Pressure Independent Control valveMethod 4�Pressure Independent Control ValveSystem at Part loadWhat happen in typical Control valve �for part load conditionTypical Control Valve is Pressure DependenceA system using typical control valve �and manual balancing valveA system using typical control valve �and manual balancing valveBalancing Considerations�in Variable Flow SystemsBalancing Considerations�in Variable Flow SystemsFour-Zone Heating SystemTypical Building LayoutPrimary-Secondary Pumping, Four-Zone Heating SystemPrimary-Secondary Bridge EnergyPrimary-Secondary Pumping, Four-Zone Heating SystemCoil With Glycol Heat Exchanger and PumpPumped Coil With�Face-Bypass DampersSpecific Heats of�Aqueous Ethylene GlycolSpecific Heats of�Aqueous Propylene GlycolOne-Shot Chemical FeederThank you


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