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    ENGINEERING ADVANTAGE

    ENERGY INSIGHTS

    OPTIMISING HYDRONIC SYSTEMS

    FOR ENERGY SAVINGS

    Tom Pak

    May 9th 2012

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    ENGINEERING ADVANTAGE

    Copyright

    TAHydronicsSA.Allrightsreserved

    .

    World's energy consumption

    2

    40% of the world's energy

    consumption is used in buildings*

    50% of this is in HVAC systems alone*

    (*) Sources: European Commission EPBD (point 6, pp1) &

    US Department of Energys Buildings Energy Data Book

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    ENGINEERING ADVANTAGE

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    .

    Energy savings on HVAC in buildings

    3

    HVAC installation Use of new technologies System approach of

    hydronic design

    Shorter pay-back times

    HVAC installation Use of new technologies System approach of

    hydronic design

    Shorter pay-back times

    Building structure(insulation, double glazing, )

    Best way to save energy Larger energy savings

    Long pay-back times

    Building structure(insulation, double glazing, )

    Best way to save energy Larger energy savings

    Long pay-back times

    Human factor Avoid interferences with

    the HVAC system

    Educate tenants andmaintenance team

    Never-ending task

    Human factor Avoid interferences with

    the HVAC system

    Educate tenants andmaintenance team

    Never-ending task

    Building modifications require

    adaptation or modernization of

    the HVAC installation to take into

    account new heat gains/losses

    When modifying a HVAC

    installation one must take into

    account the capabilities of

    people using the installation

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    ENGINEERING ADVANTAGE

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    .

    Energy savings via hydronic optimization

    4

    Optimising a building's HVAC

    system can reduce its energy

    consumption by 30% :

    By avoiding the deterioration

    of production unit

    efficiencies,

    By optimizing the energy

    efficiency of the hydronic

    distribution,

    By guaranteeing a stable and

    accurate room temperature.

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    IMPROVING

    PRODUCTION UNIT

    EFFICIENCIES

    12

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    ENGINEERING ADVANTAGE

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    .

    Coefficient of Performance (COP) isused to indicate chiller efficiency:

    Heat transfer (and thus COP) is good when Log Mean Temperature Differencebetween water and refrigerant is kept high

    Evaporator refrigerant temperature remains constant

    Supply water temperature Tsis usually kept constant

    Thus return water temperature Trmust be kept "high"

    to keep LMTD high

    Keeping a high Tr(thus a high T = T

    s-T

    r) provides higher COP at partial load

    Chillers

    24

    Evaporator

    Condenser

    Chilled water

    Tr Ts645.2

    KK

    =compressor

    evaporator

    P

    PCOP

    Refrigerant saturated

    suction temp.

    Tr

    Ts

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    ENGINEERING ADVANTAGE

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    Effect of a decrease of the return water temp. on COP

    25

    Example :

    Chiller: 200 tons (703 kW)

    Water condenser temperatures: 29,5/35C

    Supply temperature of chilled water Ts

    : 7C

    A reduction of return temperature of chilled water can lead to a

    15% drop of the COP

    Return temp. chilled water Tr [C]

    COP

    5

    4,6

    4,4

    4,24

    4,2

    4,4

    4,6

    4,8

    5

    5,2

    10,5 11 11,5 12 12,5 13

    15%

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    ENGINEERING ADVANTAGE

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    6,0

    8,0

    10,0

    12,0

    14,0

    16,0

    18,0

    20,0

    22,0

    24,0

    26,0

    0% 20% 40% 60% 80% 100%

    Variable flow proportional control

    26

    Re

    turntemp.Tr

    2-way circuit (variable flow)

    Flow through terminal unit

    Temperature regime:

    Ts/Tr/Ti = 7/12/24C

    qp

    STAD

    H

    C

    Variable flow circuit

    The T through a terminal unit increases

    when the flow reduces.

    Thus the return water temperature increases

    when the flow reduces.

    All benefits for chiller COP.

    Cooling

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    ENGINEERING ADVANTAGE

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    Constant flow system proportional control

    27

    Returntemp.T

    r

    qs

    qbSTAD-B C

    H

    STAD-P

    qp

    Flow through terminal unit

    3-way diverting circuit (constant flow)

    6,0

    8,0

    10,0

    12,0

    14,016,0

    18,0

    20,0

    22,0

    24,0

    26,0

    0% 20% 40% 60% 80% 100%

    Variable flow circuit

    Constant flow circuit

    The T through a terminal unit increases

    when the flow reduces.

    But the flow through the terminal unit is

    reduced by bypassing an increasing fractionof the primary flow (at temperature Ts).

    Thus the return water temperature decreases

    when the flow reduces !!!Constant

    flow

    Variable

    flow

    Temperature regime:

    Ts/Tr/Ti = 7/12/24C

    Cooling

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    ENGINEERING ADVANTAGE

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    shut

    Variable flow system with 2-way on-off control

    28

    When some CV are closed:

    there is less total flow and Dp in piping

    and thus more available Dp everywhere in the system

    open valves receive a flow that is higher than design flow

    At partial load in the system,

    if a valve is open: q >= qdesignopen

    qd

    openopen

    open openopen

    qd

    qd

    qd

    qd

    qd

    shut

    > 0 >

    > >0

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    ENGINEERING ADVANTAGE

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    On-off control Flow increase at partial load

    Manually balanced variable flow on-off control system

    100 identical units; Pump head 150 kPa; Terminal unit 20

    kPa; On-off CV 5 kPa

    Temperature regime:

    Ts/Tr/Ti = 7/12/24C

    0%

    10%

    20%

    30%

    40%

    50%

    60%

    70%

    80%

    90%

    100%

    0% 20% 40% 60% 80% 100%

    To

    talsystemflow

    System load

    At 50% load, the total flow in system reaches 73% of the total design flow.

    This is a 46% increase w.r.t. the required flow (50%) at 50% load.

    Seasonal flow increase lead to an estimated increased pumping energy

    consumption equal to +3% of total plant energy consumption

    29

    3%

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    ENGINEERING ADVANTAGE

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    d.

    0%

    20%

    40%

    60%

    80%

    100%

    120%

    0% 20% 40% 60% 80% 100% 120% 140% 160%

    On-off control Emission at partial load

    At flow that is near design flow,

    emitted power does not increase

    much with the flow

    Control signal switches on/off when

    room temperature deviates much

    beyond the thermostat differential

    Flow

    Emission

    30

    Roomt

    Designset-point

    24C

    Time

    At partial load in the system,if a valve is open:

    k

    TqP

    =

    (Troom - Tset-point) >=< q qdesign

    P PdesignT Tdesign

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    ENGINEERING ADVANTAGE

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    d.

    0

    2

    4

    6

    8

    10

    12

    14

    0% 20% 40% 60% 80% 100%

    Return water temp. degradation

    Re

    turntemp.T

    r

    System load

    Temperature regime:

    Ts/Tr/Ti = 7/12/24C

    Below 50% of the load, which represents typically 70% of the cooling

    season, the return water temperature is degraded by 1.5 to 2C.

    This will result approximately in a 3 to 4% increase in seasonal chiller

    energy consumption

    Manually balanced variable flow on-off control system

    100 identical units; Pump head 150 kPa; Terminal unit 20

    kPa; On-off CV 5 kPa

    31

    3%

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    d.

    6,0

    8,0

    10,0

    12,0

    14,0

    16,0

    18,0

    20,0

    22,0

    24,0

    26,0

    0% 20% 40% 60% 80% 100%

    6,0

    8,0

    10,0

    12,0

    14,0

    16,0

    18,0

    20,0

    22,0

    24,0

    26,0

    0% 20% 40% 60% 80% 100%

    Return water temp. proportional vs on-off control

    32

    Returntemp.T

    r

    2-way proportional

    3-way proportional

    Temperature regime:

    Ts/Tr/Ti = 7/12/24C

    Cooling

    Flow through terminal unit

    Returntemp.T

    r

    System load

    2-way on-off, MBV

    3-way on-off, MBV

    Proportional control On-off control

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    ENGINEERING ADVANTAGE

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    d.

    Case Study - Local University campus buildings

    33

    Renovation of 2 University buildings with a total of 9840 m2

    Installed cooling capacity: Building 1 : 1452 tons refrig.

    Building 2 : 1730 tons refrig.

    Work performed during summer 2010

    Results compared for Oct.-Nov. 2009 vs 2010

    DP controllers paired with manual balancing valves installed

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    d.

    Local University campus building 1 chiller saving

    34

    Variable secondary flow

    with differential pressure

    bypass

    Dp controllers at on-off

    control FCU groups and

    PAU/AHUs

    and re-balanced

    Annualized 22%

    chiller energy

    savingCooling load [kW]

    Powerinput[kW]

    2009

    2010

    Chiller Power Input vs. Cooling Load

    34

    22%

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    d.

    Local University campus building 2 chiller saving

    Variable flow primary-secondary system

    Addition of Dp controllersat FCU groups zones and

    pressure independent

    control valves for

    PAU/AHU and re-balanced

    Annualized 16.5%

    chiller energy

    savingCooling load [kW]

    Powerinpu

    t[kW]

    2009

    2010

    Chiller Power Input vs. Cooling Load

    35

    16%

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    Case study - business hotel at Sheung Wan

    > First LEED and BEAM Plus Platinum

    certifications of new-built hotel

    > 38 floors, 274 rooms

    > Chiller capacity 667 kW x 2 nos

    > Variable primary flow design

    > Hydronic balancing design

    > Chiller plant balancing> Dp control at each floor and

    modulating terminals

    > Balancing and control valve at FCUs

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    Hydronic balancing in variable primary flow

    Balanced chiller plant

    1

    Proper fail-safe bypass valve

    sizing and characteristic

    2

    Balancing & control

    valve for proportional

    balancing

    4

    DP stabilization against large

    Dp fluctuations in part load

    3

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    Computerized hydronic system design

    TA Select 4

    hydronic system calculation

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    Computerized hydronic system design

    > Pipe sizing per BEC recommendations

    > Balancing valve sizing and pre-settings for easy and efficient

    commissioning

    > Minimum control valve authority checks (suggest > 0.25) to ensure

    indoor comfort with stable temperature control

    > Correct Index circuit identification to help determining optimal VFD

    sensor location and set-point

    > Pump head optimization:

    > Initial : 350 kPa

    > Select 4 : 236 kPa (-33%)

    > Final set : 250 kPa (-29%)

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    Computerized hydronic system design

    > Bypass valve sizing calculation

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    ed.

    Tips for reliable and energy efficient VPF system

    > Make use of computerized software for hydraulic design calculations

    > Chiller plant must be balanced to avoid uneven distribution of flow

    > Proper bypass valve sizing and select with good rangeabilty, linear

    characteristic (or equal percentage characterisitic at 0.25 authority) valve> Use of high precision flow meter and local controller to monitor total return

    flow as fail-safe measure against chiller minimum flow

    > Use of DP controllers

    > to stablize Dp fluctuations to avoid overflow and low dT problems

    > to maintain good control valve authority necessary for stable temperature control

    > as flow/DP/DT/energy measuring station for energy audit purpose

    > Make system sustainable and adaptive to future changes

    > Locate VSP sensor at index circuit and adjust set-point to the DP of the most

    demanding stablized circuit potentially up to 40% pump energy saving

    > Make use of computerized balancing method and instrument to produce

    balancing report without manual record of measurements and verfications

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    Conclusion

    92

    Important energy savings can be achieved by taking care of: Maintaining cold/warm return water temperature

    to condensing boilers/chillers (~15%),

    Having an adequate pressurisation avoiding scaling/foulingin boilers/evaporators (~5-10%).

    Minimising pumping costs requires having (up to 40% on 7-17% in cooling):

    A good pressure maintenance to avoid corrosion leading to aging and fouling,

    An optimized hydronic distribution design (Dp control),

    A systematic methodology of balancing and commissioning.

    Stable and accurate room t control gives (~5-20%) energy savings by:

    Avoiding oversizing in on-off systems,

    Using state-of-the-art thermostatic radiator valves,

    Sizing of modulating control valves for good minimum authority.

    The approach "He who can do more can do less" is to be avoided

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    ed.

    [email protected]

    [email protected]

    93


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