Ncbc 2010 Chilled Water Commissioning Villani

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    Chilled Water System Commissioning:Variable Primary Flow

    John D. Villani, P.E.Associate

    Grumman/Butkus

    Associates

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    Learning Objectives

    1. History of chilled water system configurations2. Variable Primary Flow (VPF) chilled water systemconfiguration3. Design and Controls Considerations for properoperation of VPF chilled water systems4. Things to look for when commissioning VPF chilledwater systems

    AIA Quality Assurance

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    Chilled Water System History

    Constant Primary Flow1

    Constant Primary Flow was used before

    primary/secondary Advent of low delta T problem

    1000 ton1000 ton

    2 gpm/ton

    1000 gpm 1000 gpm

    12dT 10dT

    Loss of capacityand capital

    investment916 tons

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    Chilled Water System History

    Primary/Secondary (Balanced) 1

    Constant Primary Flow / Variable Secondary

    Flow has been the industry standard fordecades.2

    1000 ton 1000 ton

    2 gpm/ton

    1000 gpm

    12dT 10dT

    998 gpm

    2000 gpm

    1998 gpm53 Deg F

    2

    gpm4

    2DegF

    53 Deg F

    42 Deg F

    54 Deg F Design

    916 tons

    VF

    D

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    Chilled Water System History

    Primary/Secondary (Imbalanced) 1

    Problems propagate when secondary load

    and flow exceed primary

    1000 ton 1000 ton

    2 gpm/ton

    1000 gpm

    12dT 10dT

    1200 gpm

    2000 gpm

    53DegF20

    0gpm

    ADDED

    54 Deg F Design

    42 Deg F

    VF

    DRampsup

    2200 gpm53 Deg F53 Deg F 1008 tons

    SCHWS Temp increases

    Flow throughchiller remains

    constant

    47 Deg F

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    Chilled Water System History

    Primary/Secondary1

    Constant Primary Flow / Variable Secondary

    Flow with check valve, one of many options

    1000 ton 1000 ton

    2 gpm/ton

    1000 gpm

    12dT 10dT

    1200 gpm

    Check valveprevents

    secondaryflow fromexceeding

    primary flow

    VF

    D

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    Chilled Water System History

    Variable Primary1

    Variable Primary Flow with Low Flow Bypass

    Variable Flow

    VF D

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    Chilled Water System History

    Why is Variable Primary Flow (VPF) New?

    (According to survey of chiller manufacturers1

    ) Always technicallyfeasible

    Practical application limited by on-board

    controls in use prior to mid-1990sCapacity modulation

    Freeze protection

    Flow detection Improvements in all areas have increasedmanufacturer support for variable primary flow

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    VPF Design Considerations

    Design Issues

    Pumps are controlled by load differential pressure(dP), not staged with chillers

    Low Flow Bypass is critical to maintain minimumchilled water flow through the chillers

    Flow Rate Range Limits

    Typical 3

    12 ft/s tube velocity range

    maximum turn down to ~25%

    Rate of change of flow

    Do not exceed rate of change greater than 30% ofdesign flow per minute3

    Older constant speed chillers, do not exceed 10%3

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    VPF Controls Considerations

    Controls Complications with VPF

    Differential Pressure (dP) pumping control

    Low Flow Bypass controls

    Chiller staging effect on flow through chillers

    Chiller modulating flow control valves tobalance flow through multiple chillers inoperation

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    VPF Controls Considerations

    Differential Pressure (dP) pumpingcontrol

    Common chilled water systems feed multipleloads, air handlers and buildings System configurations typically have multiplerisers and/or buildings

    Resulting in varying dP requirements

    throughout the system

    VPF pumps need to satisfy the hydraulicallymost critical zone, which is the zone furthestbelow set point

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    VPF Controls Considerations

    Differential Pressure (dP) pumpingcontrol

    Need a sequence to stage pumps

    Pumps can be staged to keep several pumps

    running at a lower speed Dont let pump speed go below 40% or24Hz, pump will not flow water, look at the

    pump curve Stage up/down at 80%, 60%, 53% Put in a dP dead band so pumps dont hunt!!

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    VPF Controls Considerations

    Differential Pressure (dP) pumpingcontrol

    LOADdP STPT

    16 psi

    LOADdP STPT

    12 psi

    VF D

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    (dP) pumpingcontrol2 zones

    Evaluates

    one zone vs.other zones

    If both zones areunder setpoint,

    determine which

    has a greater %under set point

    Calculate %under

    setpoint

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    VPF Controls Considerations

    Low Flow Bypass controls

    Valve type and actuator must be fast acting

    Bypass control proportional, integral,derivative (PID) loop must be fast acting Bypass control loop must be able to handlechanges in system operation such as a

    failure of a load (air handler) which suddenly

    shuts the CHW control valve

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    Case Study Results

    Case Study - Low Flow Bypass

    (3) electric centrifugal 400 ton chillers

    2 gpm chilled water design flow rate per ton 800 gpm per chiller Minimum Flow Rate = 210 gpm Chilled water header = 10

    Low Flow Bypass Line Size = 6

    Lesson Learned: size the bypass lineappropriately and select a fast actingmodulating actuator; controllability of thebypass can be extremely difficult

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    Case Study Results

    Case Study - Low Flow Bypass

    6ChilledWater

    BypassfromCHWS

    Header

    10 ChilledWaterBypassControlValve

    BrayButterfly

    Valve

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    VPF Controls Considerations

    Chiller Staging

    Pumps are controlled by system dPs

    Chillers are staged based on leaving chilledwater supply water temperatureAND

    Chiller chilled water flow rates or differentialpressure across evaporator

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    VPF Controls Considerations

    Chiller Staging Problems

    Due to decoupled pumps and chillers

    Load can increase demanding more pumping

    Chillers may be able to still meet the leaving

    CHW setpoint Flow through chiller may exceed the systemallowable

    pressure drop and cause loss of

    pressure in the field

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    Excess Flow causes increased PD

    DESIGN

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    Chiller Staging Problems

    Chiller Staging Problems

    1 Chiller operating near full load

    CHWS temperature setpoint may be low 42 F

    VF D

    1000 gpm 1200 gpm

    2000 gpm(design)

    2200 gpm(actual)

    MM OPENCLOSED

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    Chiller Staging Problems

    Chiller Staging Problems

    Staging on the second chillers

    Valves must be modulating and slow acting

    VF D

    1000 gpm 1200 gpm

    2000 gpm(design)

    1100 gpm(actual)

    MM OPENOPEN

    2000 gpm(design)

    1100 gpm(actual)

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    Chiller Staging Problems

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    Chiller Staging Problems

    Chiller Staging Problems

    Rate of change limit 30%, 2000 gpm = 600 gpm

    Flow drops 1100 gpm, need to take 2 minutes toopen second chillers control valve

    VF D

    1000 gpm 1200 gpm

    2000 gpm(design)

    1100 gpm(actual)

    MM OPENOPEN

    2000 gpm(design)

    1100 gpm(actual)

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    Chiller Staging Suggestions

    Chiller Staging Sequence Suggestions

    Before staging on next chiller, raise the

    operating chillers setpoint This should be done a few minutes beforeopening the second chillers evaporator flow

    control valve

    This will back off how hard the first chiller is

    working and help prepare it for the suddendrop in chilled water flow

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    Chiller Staging Suggestions

    Chiller Staging Sequence Suggestions

    After the second chiller is staged on for a

    period of several minutes, start resetting theCHWS temp setpoint back down

    LOCK THE PUMPS at their current speed

    while staging chillers on and off

    You dont want to pump control sequence to

    start speeding up pumps due to a drop insystem pressure as the second chiller stageson, this will cause faster flow through the

    chiller

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    Staging & Hydraulically Most Remote Chiller

    Chiller Staging Problems

    Plants consist of both variable speed chillers and

    constant speed chillers of different capacities

    Need to assess pressure drop across chillers & piping

    VF D

    1050 ton3 pass

    1500 gpm28.6 ft wg

    MM OPEN Modulate

    750 ton3 pass

    1124 gpm25.1 ft wg

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    Staging & Hydraulically Most Remote Chiller

    Which chiller is hydraulically the most remote?

    Take piping into account when determining this

    How do you select which chiller valves areopen and which modulate?

    Chiller# 1 2 3 4ratedtonnage 1050 1050 750 1190#ofEvapPasses 3 3 3 2

    Evapgpm 1500 1500 1124 1783EvapPDftwg 28.6 28.6 25.1 20.5

    ChillerPerformanceCharacteristics

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    Staging & Hydraulically Most Remote Chiller

    DESIGN

    FLOW ANDPRESSUREDROP TOMATCHOTHER

    CHILLERS

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    Chiller Staging and Pressure Drop Problems

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    Chiller Staging and Pressure Drop Problems

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    VPF Cx Considerations and Realities

    Low Flow Bypass controls

    Review bypass valve size and actuator stroke

    time

    Hard to Cx without load on the building.Without load the system will operate withbypass open and no load on chillers

    Maximum turn down to 25% is optimistic.

    Too little water through the evaporator tokeep the system stable

    Expect some surging at low flow conditions

    and Low Evaporator Temperaturealarm trips

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    VPF Cx Considerations and Realities

    Sequence of Operations

    Request from the design team the chiller

    plant and pumping staging sequence

    Request a matrix on which chillers ANDpiping make the hydraulically most remotechillers and how to modulate the CHW flowcontrol valves

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    VPF Cx Considerations and Realities

    Chiller Performance Submittal

    Review chiller minimum and maximum flow

    rates

    Review chiller rated pressure drop Review chiller pressure drop curve This many not be provided in a standardchiller submittal and must be requested If all this information is not provided, there willbe guess work in the field

    C C

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    VPF Cx Considerations and Realities

    Controls

    Limit the speed at which the chilled water

    pump VFDs can speed up and down

    Limit the time span the chilled water flowcontrol valve actuators can stroke from min tomax

    Review the system dPs and how the pumps

    track to maintain the lowest from setpoint Put in a dead band so the pumps are notalways hunting due to system size and

    complexity

    VPFC S i M Effi i

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    VPF Cx Squeezing More Efficiency

    Controls

    TREND air handler control valves and bypass

    valve

    RESET chilled water supply temperaturesetpoint based something, valve position This will provide chiller electrical savings atthe expense of increased pumping Condenser water reset still works great!

    VPF C t k thi t ff !!

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    VPF Cx you cant make this stuff up!!

    Controls

    Johnson Controls buys York, Aug 2005

    May 2010, York startup tech says chilledwater reset is not a good idea and disallowsJCI from doing chilled water reset

    After a Cx discussion, the next days . . .

    York allows JCI access to do CHW reset

    Only to find out that now you have tocontrol the chillers demand limiting functionas well?? Limit to 80% for the first 30 min.

    4

    R f

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    References

    References1.

    William P. Bahnfleth, Eric B. Peyer, 2003, Variable Primary Flow: PotentialBenefits and Application Issues

    2.

    ASHRAE Handbook HVAC Systems and Equipment, 1996

    2.

    McQuiston, F., J. Parker and J. Spitler, 2000 Heating, ventilating and airconditioning

    analysis and design, 5th

    edition

    3.

    Carrier Corporation

    (Project and Chiller Specific, refer to your particular

    chiller manufacturers details)4.

    Johnson Controls Inc./York International Corporation

    (Project and Chiller

    Specific, refer to your particular chiller manufacturers details)

    AIA Q lit A

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    AIA Quality Assurance

    Portland Energy Conservation, Inc is a registered provider with TheAmerican Institute of Architects Continuing Education Systems. Creditearned on completion of this program will be reported to CES Recordsfor AIA members. Certificates of Completion for non-AIA members are

    available on request.

    This program is registered with the AIA/CES for continuingprofessional education. As such, it does not include content that maybe deemed or construed to be an approval or endorsement by the AIAof any material of construction or any method or manner of handling,using, distributing, or dealing in any material or product. Questions

    related to specific materials, methods, and services will be addressedat the conclusion of this presentation.

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    Questions AND thank you

    John D. Villani, P.E., LEED AP, C.E.M., QCxPGrumman/Butkus Associates

    [email protected]

    (847) 328-3555

    mailto:[email protected]:[email protected]