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  • RCREEEA N M E

    RCREEE Energy Audit in BuildingTraining Course Program

    Tunis, Ist - 5th June 2010

    -MJzL "1

    VfEnergy audit of air-conditioning and

    cooling systemsQmby

    Adel MourtadaJS tmTW

    I

  • 1Content1

    - Refrigeration cycP- AC/Refrigeration Systems andComponents

    -Type of refrigeration

    -Assessment of refrigeration and AC

    -Energy Efficiency Measures

    -Energy Audit of HVAC System inCommercial Suiluing Utilities

    TTU?>.0

    i TI_

    -rAdel Mourtada

  • TXVr**

    Chiller:

    I

    J}Suction LinejK- Low SideHigh Side

    \

    i1TypicalRefrigeration

    Cycle

    c CompressorCiXL mmCondenser

    k* ReceiverS**H3B

    J

    Adel Mourtada 3

  • Thermodynamic Cycle4

    IWX.

    SATURATED V AA OR

    Otu 4 *

  • K.*! r? - Refrigeration cycle- AC/Refrigeration Systems anON

    -Type of refrigeration

    - Assessment of refrigeration and AC- Energy Efficiency Measures- Energy Audit of HVAC System inCommercial Building Utilities

    :

    3] rp

    t 9

    sAdel Mourtada

  • ComponentsT? TXVT\r y Refrigerant

    Evaporator/Chiller

    CompressorCondenser

    ReceiverThermostaticexpansionvalve (TXV)

    Chiller

    =Suction LineJLow SideHigh Side JI

    v

    t q Compressorr-MM

    Condenser

    0 *a &L.I ReceiverPCT' \

    X* 6Adel Mourtada

  • CompressorsThere is a large variety of

    | compressors. Some of variationsare:

    The compressor manufacturer

    Piston, vane, or scroll type

    The piston and cylinderarrangement

    How the compressor is mounted

    Style and position of ports

    Type and number of drive belts

    Compressor displacement

    Fixed or variable displacement

    A

    UL,

    fa r : r*ISf X-

    \ lrx f,i i;il.J -fi f*1.H: {ft*

    sJ* I

    ,n %

    *\ t, 1 fyl.1 >1

    *

    Ji'l#

    i i,W.; r (L frr *'# trIt1wm D* * ii* f * -i- *-1It* 1 71K731

    Adel Mourtada 7

  • Evaporator Types

    Plate evaporators, top, area series of stampedaluminum plates that arejoined together. Tube andfin evaporators, bottom,have tubes for therefrigerant that are joinedto the fins.

    :

    'l -

    J-.v!

    11JLirifiPv:V,

    vr

    mfis TTTT.V

    Jjj.-T-l

    |8i ii .'vTv-fl L--:i a

    Adel Mourtada B

  • f? RefrigerantJ* Desirable properties:

    High latent heat of vaporization - max cooling Non-toxicity (no health hazard) Desirable saturation temp (for operating pressure) Chemical stability (non-flammable/non-explosive) Ease of leak detection Low cost

    Readily availableCommonly named "FREON" (R-114, etc.)

    1

    I, >-

    9Adel Mourtada

  • Condenser Types;v

    Condensers A and C areround tube, serpentinecondensers.

    VA

    A

    {AI

    r

    'N B iu V )CE Condenser B is an

    oval/flat tube, serpentinecondenser.

    i;ir **_ B J'I- !1 VDS- .fl~ fr i y/' ** MIJV ICfl tN Condenser D is an

    oval/flat tube, parallelflow condenser.

    i+

    fas I;

    J

    sj

    Flat tube condensers aremore efficient.

    L

    zil

    Adel Mourtada 10

  • I Expansion Devicesy* The expansion device separates the high

    side from the low side and provides arestriction for the compressor to pumpagainst.

    There are two styles of expansiondevices:- The TXV can open or close to changeflow. It is controlled by the superheatspring, thermal bulb that sensesevaporator outlet temperature, andevaporator pressure- The OT is a tubular, plastic device with asmall metal tube inside. The color of theOT is used to determine the diameter ofthe tube. Most OT have a fixed diameterorifice.

    mji

    Jr"

    LA fc-s~\t) c-e,*

    0-rir>Qpr > utoa i < c 3< J tSs- MpcMiuEurm. 11Adel Mourtada

  • IAC Systems

    * 5

    AC options / combinations:

    Da* Air Conditioning (for comfort / machine)

    Split air conditioners

    Fan coil units in a larger system

    Air handling units in a larger system

    TTiJ9I0

    fflrp1

    Adel Mourtada 12

  • Refrigeration systems* 5

    Small capacity modular units of directexpansion type (50 Tons of Refrigeration)

    * Centralized chilled water plants withchilled water as a secondary coolant (>50TTiJ9I TR)

    0V

    l 'L

    Adel Mourtada 13

  • IRefrigeration at large CommercialBuildings* Bank of units off-site with common

    Chilled water pumps

    Condenser water pumps

    Cooling towers

    * More levels of refrigeration/AC, e.g.

    5

    Da

    * Comfort air conditioning (20-25 C)

    Chilled water system (5-10 C)0

    II(HIAdel Mourtada 14

  • - Refrigeration cycle-AC/Refrigeration Systems andComponents

    Qjype of refrigeration- Assessment of refrigeration and AC-Energy Efficiency Measures

    -Energy Audit of HVAC System inCommercial Building Utilities

    *p i

    ji]:r?t>-- S

    15Adel Mourtada

  • Type of refrigerationf

    t

    ia2S!Qrr Refrigeration systemsLr

    * Vapour CompressionRefrigeration (VCR): usesmechanical energy

    * Vapour Absorption Refrigeration(VAR): uses thermal energy

    A

    Adel Mourtada 16

  • 1Type of refrigeration

    Vapour Compression RefrigerationChoice of compressor, design ofcondenser and evaporator determined

    *

    M if- I,

    S ,

    by: Refrigerant

    Required cooling

    LoadItTl (/s * Ease of maintenance Physical space requirements

    Availability of utilities (water, power)ftr*

    s.

    * PR

    Adel Mourtada 17

  • What's Solar Cooling?

    The core idea is to use the solar energy directly toproduce chilled water.

    The high temperature required by absorptionchillers is provided by solar troughs.

    The system doesn't require "High Technology"materials (like in PV systems] and has peakproduction in the moment of peak demand.

    I

    '5T HeatTransfer Fluidwater L:If fcr> Xl 'I

    Wfr JiiftiS

    18Adel Mourtada

  • tJSystem combined to sub-floor exchanger

    - r;.

    VJ ? i A SFloor system1.IJ Controllers I li1> I'L. \

    11 11Cooling towerU Storage tank

  • Type of refrigeration

    Evaporative Cooling* Air in contact with water to cool it close to wet

    bulb temperature

    * Advantage: efficient cooling at low cost

    Disadvantage: air is rich in moisture

    f

    IQrr

    SprinklingWater

    fL

    ColdHot Air * r " Air1 V, I

    s i tN.

    -F- 1i# Adel Mourtada 20

  • I-'L Type of refrigerationMain Features of Cooling Towers/f*

    $/GiMlAnatomy of a Cooling Tower

    rV I i aerosc

    \ w!..

    air handling unrt

    /i- L 4 - Cr: !b_V

    itanJ* 4 dritt cccd air tobuilding

    j

    _ eliminator:; A* f mmmmtmsmi heatedrefrigerantA .;.y- -

    Su VJX * T 4, t > 4 * >:'.irflowl VlterPiVs) * f'

    viater ii CDC1 jilc S.w%

    - F

    Adel Mourtada 21

  • I Type of refrigerationComponents of a cooling tower

    * Frame and casing: support exteriorenclosures

    Fill: facilitate heat transfer bymaximizing water / air contactSplash fill

    * Film fill

    * Cold water basin: receives water atbottom of tower

    imm

    fL

    I

    - k.H

    Adel Mourtada 22

  • L Type of refrigerationComponents of a cooling tower Drift eliminators: capture droplets in

    air stream

    Air inlet: entry point of air

    * Louvers: equalize air flow into the filland retain water within tower

    Nozzles: spray water to wet the fill

    * Fans: deliver air flow in the tower

    1t

    SMMBIJ- *5

    sl +

    j " T

    CNsL - j

    m Adel Mourtada 23

  • Type of refrigeration

    Mechanical Draft Cooling Towers

    * Large fans to force air throughcirculated water

    /\ )j

    f

    I

    *MF'111; - * Water falls over fill surfaces:

    maximum heat transferJ a*5 Cooling rates depend on many

    parameters

    * Large range of capacities

    Can be grouped, e.g. 8-cell toweri

    1%.

    Pfr

    - ...Adel Mourtada 24

  • Type of refrigerationf

    I! * T Forced Draft Cooling Towers

    Air blown through towerby centrifugal fan at airinlet

    Advantages: suited forhigh air resistance & fansare relatively quiet

    Disadvantages:recirculation due to highair-entry and low air-exitvelocities

    \\\\u~jwfmmmmmmh Hot waterm m * mm m n\ rT\ A

    Fill

    Centrllugaltan

    r *r \ Cold wateri ' L- :v

    L:: Adel Mourtada 25

  • - Refrigeration cycle-AC/Refrigeration Systems andComponents

    -Type of refrigeration

    -Assessment of refrigeration and A

    -Energy Efficiency Measures

    - Energy Audit of HVAC System inCommercial Building Utilities

    *p i

    ji]:

    -- S26Adel Mourtada

  • HT! Assessment of Refrigeration

    * Cooling effect: Tons of Refrigeration*

    1 TR = 3024 kCal/hr heat rejected

    TR is assessed as:TR = Q x-Cp x- (Ti- To) / 3024Q = mass flow rate of coolant in kg/hrCp- is coolant specific heat in kCal /kg deg CTi - inlet, temperature of coolant to evaporator (chiller) in 0CTo - outlet temperature of coolant from evaporator (chiller) in 0C

    kI

    Adel Mourtada 27

  • Assessment of RefrigerationSpecific Power Consumption (kW/TR)

    * Indicator of refrigeration systemsperformance

    * kW/TR of centralized chilled watersystem is sum of* Compressor kW/TR

    Chilled water pump kW/TRCondenser water pump kW/TRCooling tower fan kW/TR

    p f5

    I* rJsSc__

    I T

    Adel Mourtada 28

  • \/

    Assessment of RefrigerationCoefficient of Performance (COPCarnot) Standard measure of refrigeration efficiency

    Depends on evaporator temperature Te andcondensing temperature Tc:

    i

    IUS COP Te / (Tc - Te)CarnotI

    COP calculated for type of compressor:

    Coolingeffect (kW)... COP =Power input to compressor (kW)....i

    i# Adel Mourtada 29

  • IAssessment of Air Conditioning

    Measure5

    Airflow Q (m3/s) at Fan Coif Units (FCU) or AirHandling Units (AHU): anemometer

    Air density p (kg/m3)

    Dry bulb and wet bulb temperature: psychrometer

    Enthalpy (kCal/kg) of inlet air (hjn) and outlet air(Hout): psychrometric charts

    ])a

    0 Calculate TR Qx p X (K ~Kut)TR =J 'L--p 3024Adel Mourtada 30

  • s /I1'ta.

    LL r Assessment of Air ConditioningIndicative TR load profile

    * Small office cabins: 0.1 TR/m2

    Medium size office (10 - 30 peopleoccupancy) with central A/C: 0.06TR/m2

    * Large multistoried office complexeswith central A/C: 0.04 TR/m2

    9 m

    ys

    ph

    Hdel Mourtada 31

  • Considerations for AssessmentFFrffiHS''SML1 * Accuracy of measurements

    Inlet/outlet temp of chilled and condenserwater

    Flow of chilled and condenser water

    * Integrated Part Load Value (IPLV)kW/TR for 100% load but most equipment

    operate between 50-75% of full load

    IPLV calculates kW/TR with partial loads

    Four points in cycle: 100%, 75%, 50%, 25%

    5T___I T

    t

    Adel Mourtada 32

  • Assessment of Cooling TowersMeasured Parameters

    Ita.

    Wet bulb temperature of air

    Dry bulb temperature of air

    Cooling tower inlet water temperature

    Cooling tower outlet water temperature

    Exhaust air temperature

    Electrical readings of pump and fanmotors

    Water flow rate

    Air flow rate

    __ 5

    r -i **fV

    1 M

    - t*

    Adel Mourtada 33

  • Central Plant metrics

    I Chiller efficiency - kW/tonWJi Cooling tower efficiency - kW/ton

    Condenser water pump efficiency - kW/tonJ

    Chilled water pump efficiency - kW/ton.

    * (.

    f*-

    34Adel Mourtada

  • - Refrigeration cycle-AC/Refrigeration Systems andComponents

    -Type of refrigeration

    -Assessment of refrigeration and AC

    Efficiency Measures- Energy Audit of HVAC System inCommercial Building Utilities

    *p i

    a0

    35Adel Mourtada

  • mIn Energy Efficiency Measures1. Optimize process heat exchange

    2. Maintain heat exchanger surfaces3. Multi-staging systems

    4. Matching capacity to system load

    5. Capacity control of compressors

    6. Multi-level refrigeration for plant needs

    7. Chilled water storage

    8. System design features9. Optimize cooling tower

    t/

    ? ...ir B

    1

    . r>N

    f

    a:?''

    UF!

    Adel Mourtada 36

  • i Energy Efficiency Measurest1. Optimize Process Heat Exchange

    High compressor safety margins:energy loss

    1. Proper sizing heat transfer areas ofheat exchangers and evaporators

    Heat transfer coefficient on refrigerant side:1400 - 2800 Watt/m2K

    Heat transfer area refrigerant side: >0.5 m2/TR

    2. Optimum driving force (difference Te andTc): 1C raise in Te = 3% power savings

    if*2**!tysE***

    'M ;I TLP 1

    i

    F!Adel Mourtada 37

  • Energy Efficiency Measures1. Optimize Process Heat Exchange//rai!irVI B Evaporator

    Temperature (C)Refrigeration

    Capacity(tons)Specific Power

    Consumption (kW/TR)Increase

    kW/TR (%)5.0 67.58 0.81

    0.0 56.07 0.94 16.0-5.0 45.98 1.08 33.0

    -10-0 37-20 1-25 54-0

    -20-0 23-12 1-67 106-0

    Condenser temperature 40 Cwm; r\

    'Q1 CondensingTemperature (C) RefrigerationCapacity (tons) Specific PowerConsumption (kW/TR) increasekW/TR (%)/V) 26.7 31.5 1.1735.0 21.4 1.27 8.540-0 20-0 1-41 20-5Kb

    compressor using R-22 refrigerant. Evaporator temperature.-10 C

    Adel Mourtada 38

  • f11 f Energy Efficiency Measurest1. Optimize Process Heat Exchange

    Selection of condensershx **

    * Options: Air cooled condensers Air-cooled with water spray condensers* Shell & tube condensers with water-cooling

    * Water-cooled shell & tube condenser Lower discharge pressure* Higher TR Lower power consumption

    iftr* NI 'L v

    O'

    :I9-- raAdel Mourtada 39

  • ; Energy Efficiency Measures

    2. Maintain Heat Exchanger Surfaces

    * Poor maintenance = increased powerconsumption

    Maintain condensers and evaporators* Separation of lubricating oil and refrigerant Timely defrosting of coils

    * Increased velocity of secondary coolant

    * Maintain cooling towers* 0.55 C reduction in returning water from cooling

    tower = 3.0 % reduced power

    aI

    ST I

    K \I T1

    Adel Mourtada 40

  • I Energy Efficiency Measures/rai; 2. Maintain Heat Exchanger Surfaces

    Effect of poor maintenance oncompressor power consumption

    ir | rf

    SpecificPower

    Consumption(kW/TR)

    IncreasekW/TRTe Tc Refrigeration

    Capacity (TR)Condition (C)

  • Energy Efficiency Measures

    3. Multi-Staging Systems* iSuited for

    * Low temp applications with high compression

    * Wide temperature range

    Two types for all compressor types

    * Compound

    * CascadeKLA0V

    :v

    TgtUiAdel Mourtada 42

  • Energy Efficiency Measures3. Multi-Stage Systemsa. Compound

    i rr1

    i

    Two low compression ratios = 1 high First stage compressor meets cooling load

    Second stage compressor meets loadevaporator and flash gas

    Single refrigerant

    b. Cascade

    J

    : r?

    rf?MQ * Preferred for -46 oC to -101oCL

    * Two systems with different refrigerantst >-

    Adel Mourtada 43

  • Energy Efficiency Measures

    4. Matching Capacity to Load System* Most applications have varying loads

    * Consequence of part-load operationCOP increasesbut lower efficiency

    * Match refrigeration capacity to loadrequires knowledge of Compressor performanceVariations in ambient conditions Cooling ioad

    irtri

    HE*

    c

    r>

    >

    __IJ

    Adel Mourtada 44

  • Energy Efficiency Measures5. Capacity Control of Compressors

    /.

    % r._

    * Cylinder unloading, vanes, valves* Reciprocating compressors: Step-by-Step through

    cylinder unloading:

    * Centrifugal compressors: continuous modulationthrough vane control

    Screw compressors: sliding valves

    * Speed control Reciprocating compressors: ensure

    lubrication system is not affectedCentrifugal compressors: >50% of capacity

    1

    fKT*

    t 9

    Adel Mourtada 45

  • Energy Efficiency Measures

    5. Capacity Control of Compressorsrf rz

    Temperature monitoringReciprocating compressors: return water (if

    varying loads), water leaving chiller(constant loads)

    Centrifugal compressors: outgoing watertemperature

    Screw compressors: outgoing watertemperature

    Part load applications: screwcompressors more efficient

    iKT*

    t 9

    Adel Mourtada 46

  • Energy Efficiency Measures

    6. Multi-Level RefrigerationBank of compressors at central plant Monitor cooling and chiller load: 1chiller full

    loadmore efficient than 2 chillers atpart-load

    Distribution system: individual chillers feed allbranch lines; Isolation valves; Valves to isolatesections

    Load individual compressors to full capacitybefore operating second compressor

    Provide smaller capacity chiller to meet peakdemands

    mMT -- KV

    l

    !W I1

    HAdel Mourtada 47

  • Energy Efficiency Measures rr1

    6. Multi-Level Refrigerationi

    Packaged units (instead of central plant)Diverse applications with wide temp rangeand long distance

    * Benefits: economical, flexible and reliable

    * Disadvantage: central plants use less power

    Flow control

    J

    35 v Reduced flow'

    Operation at normal flow with shut-off periods5t t-

    Adel Mourtada 48

  • Energy Efficiency Measures

    7. Chilled Water Storage

    * Chilled water storage facility withinsulation

    * Suited only if temp variations areacceptable

    Economical because Chillers operate during low peak demand

    hours: reduced peak demand charges Chillers operate at nighttime: reduced tariffs

    and improved COP

    n; r>SP

    L

    u '

    [F

    Adel Mourtada 49

  • r Energy Efficiency Measures8. System Design Features

    f/

    FRP impellers, film fills, PVC drift eliminators

    Softened water for condensers

    Economic insulation thickness

    Roof coatings and false ceilings

    Energy efficient heat recovery devices

    Variable air volume systems

    Sun film application for heat reflection

    Optimizing lighting loads

    *

    0ssm H .

    Adel Mourtada_i-r m 50H -

  • Energy Efficiency Measures

    9. System Design FeaturesVI

    - Selecting a cooling tower-Fills

    - Pumps and water distribution- Fans and motorsi

    Ni *

    lJ

    Adel Mourtada 51c 1

  • Energy Efficiency Measures

    r ft? r Selecting a cooling tower

    Capacity

    * Heat dissipation (kCal/hour)

    * Circulated flow rate (m3/hr)

    Other factors

    *' "m

    iPCT' \

    Adel Mourtada 52

  • Energy Efficiency Measures

    Selecting a cooling tower>Range

    Range determined by process, not by system

    Approach* Closer to the wet bulb temperature

    * Bigger size cooling tower

    More expensive

    0

    fell Adel Mourtada 53

  • Energy Efficiency Measuresft! f

    >"1 Selecting a cooling tower

    Heat Load

    * Determined by process

    Required cooling is controlled by thedesired operating temperature

    * High heat load = large size and costof cooling tower

    LMIC14

    .

    rs kUi

    *

    *

    1

    i-

    Adel Mourtada 54

  • V 1

    Energy Efficiency Measurest!* n * Selecting a cooling tower

    Wet bulb temperature - considerations:Bfif

    Water is cooled to temp higher than wet bulbtemp

    Conditions at tower site

    Not to exceed 5% of design wet bulb temp Is wet bulb temp specified as ambient (preferred)

    or inlet

    Can tower deal with increased wet bulb temp

    Cold water to exchange heat

    1

    n rs__

    f /

    ! v ;p

    S7

    K'it-'

    Adel Mourtada 55

  • L Energy Efficiency Measures// Selecting a cooling towerRelationship range, flow and heat loadRange increases with increased

    Amount circulated water (flow)

    Heat load

    Causes of range increase

    Inlet water temperature increases

    Exit water temperature decreases

    Consequence = larger tower

    rin% B

    1

    iTs . r>M If

    mx3]XT':

    Adel Mourtada 56

  • Energy Efficiency MeasuresSelecting a cooling tower

    1

    5 Relationship Approach and Wet bulbtemperature

    If approach stays the same (e.g. 4.45 oC)

    Higher wet bulb temperature (26.67 oC)

    = more heat picked up (15.5 kCal/kg air)= smaller tower needed

    Lower wet bulb temperature (21.11 oC)

    = less heat picked up (12.1 kCal/kg air)= larger tower needed

    s

    it 9

    E Adel Mourtada 57

  • Energy Efficiency Measures

    1 iff H* Fill media* y s

    * Hot water distributed over fill mediaand cools down through evaporation

    * Fill media impacts electricity use* Efficiently designed fill media reduces pumpingcosts

    * Fill media influences heat exchange: surfacearea, duration of contact, turbulence

    r. r>ST

    F!Adel Mourtada 58

  • f Energy Efficiency MeasurestPumps and water distribution* Pumps: see pumps session

    * Optimize cooling water treatmentIncrease cycles of concentration (COC) bycooling water treatment helps reduce makeup water

    Indirect electricity savings

    * Install drift eliminators

    PP!ir ii IT

    ift* N Reduce drift loss from 0.02% to only 0.003 -

    0.001%I 'L v

    O'

    :I9-- raAdel Mourtada 59

  • Energy Efficiency MeasuresCooling Tower Fans

    Fans must overcome systemresistance, pressure loss: impactselectricity use

    * Fan efficiency depends on bladeprofileReplace metallic fans with FBR blades (20-

    30% savings)

    Use blades with aerodynamic profile (85-92%fan efficiency)

    EMOflM5

    !

    W I1

    t 9

    Adel Mourtada 60

  • il Benefits of Variable Flow1 1JF/

    fI

    X* Lowest Energy consumption Low Differential Pressure Easier Operation Reduced & Timely Maintenance Greatest Diversity Fewer or smaller chillers possible

    n yDrm

    V--*,

    61Adel Mourtada

  • Why Variable Flow?

    1 Power varies with Cube of New FlowRatio.- New Energy = New Flow / Old Flow (!4), Cubed

    = 1/8- Most reliable operation.

    1

    Therefore, Energy Savings = 7/8 of theoriginal energy (less any losses fromnew equipment)!

    E)I

    pr >X-*.L '4

    62Adel Mourtada

  • V 1

    Energy Efficiency Measurest!* n * Fill media

    Comparing 3 fill media: film fill moreefficient

    wo* 5

    1SplashFill FilmFill Low Clog

    FilmFill

    Possible UG Ratio 1.1 -1.5 1.5 -2.0 1.4- 1.8

    Lt? 150 m2/m3 85- 100m2/m3Effective Heat ExchangeArea

    30-45m2/m3

    Fill Height Required 5-10 m 1.2 -1.5 m 1.5- 1.8 m' s Pumping Head

    Requirement9-12m 5- 8 m 6-9 m

    S7

    Quantity of Air Required High Much Low Lowia-'Adel Mourtada 63

  • VPF system configurationsManifolded pumps

    .

    fr - Redundancy- Reduced energy- VFD on aii pumps- Allows "overpumping"

    for "Low ATSyndrome"

    I

    J -

    &\ r,i ITr:ft1E* -P * JJ IL J

    1 Adel Mourtada 64

  • Keep it Simple1F\

    pranau Well designed control system ismandatory.

    Minimize manual operation.Develop clearly written operating

    procedure and backupfailure mode.

    Continual training ofthe operators.

    1

    i

    1

    oir,r*

    N

    -r

    65Adel Mourtada

  • - Refrigeration cycle-AC/Refrigeration Systems andComponents

    -Type of refrigeration

    -Assessment of refrigeration and AC

    -Energy Efficiency Measures

    -Energy Audit of HVAC SysternirP-Commercial Building Utilities

    *p i

    ji]:

    -- S66Adel Mourtada

  • Typical Cooling Load Profile

    i Tl&

    illI!

    I BLQ3

    asSe

    K

    :

    JL 6167Adel Mourtada

  • Energy Saving,Possibilitiesiilfp.

    Jkedteeabiftg: LoadmmmmmL _'........................W7: . .

    PPS

    /m -/< ' NiflewlVr Shift Cooling Demand To '

    Off Peak hours;, :: . i-xf v yJ-"'H|| , _ JJF

    3-i-

    S&K: Redore Required chiHer- : ;

    Capacity for meeting :

    te lhtKlk i)ia.I _

    E- 7 s

    ' Reduce Maximum '.Generate Hof Watexjo to :

    :/: : ;$QT through:; i :.....waste neat recovery : - :sj"! " ':,I from Chiller V '

    litb

    5323233T

    fsm*I/

    n 6868Adel Mourtada

  • I Interior Window FilmsFn

    t

    If acceptable bybuildingmanagement,window films may bea useful option.Choose film tailoredfor climate.

    $

    iijT,

    11Mtih

    1

    Imw i TlIii. i i** i!

    fK

    i] : Lift L: -

    Pay Back Period 2 yearsT .

    6969Adel Mourtada

  • I Programmable Thermostats or BMSFf

    Thu

    t n'ifuu ILI They work whenyou use them.A~)nFVi 1|J ' IU rHMI

    A 1

    Jl j:nm

    HMwjL

    P2jp WhfteTRockjersLi 1 Q

    l>

    70Adel Mourtada

  • VAV Fans Control1i(

    Static Pressure Reset on VAV Systems.

    Provides significant fan energy savingssince system is often at part load

    Reduces fan noise"Variable air volume (VAV ) terminal units

    shall be programmed to operate at theminimum airflow when the zonetemperature is within the setdeadband."

    Ita.i*i

    5K

    I

    s.

    t

    H71Adel Mourtada

  • Heat recovery from Chiller

    -* c Air-conditione

    d Space

    5 -AChiller Mode MS y

    700 kW (200TR) coolingload

    140 kWElectricalInput

    1T

    ,r>- -Ph +>+ 840 kW heat

    RejectedthroughCT/aircooledcondenser

    H ' T *rt--*- + +.-S

    0 About 8-12% of heat can be recovered in Chiller mode (Le, 65-100 kWheat) through desuperheater (Free of Cost )"0.1Carbon credit per hour" 720 Carbon Credits/ Year (24hrs K 30 Q Days}

    JF72*f 72Adel Mourtada

  • Partial Heat Recovery1Jf

    IQrr

    I 1 Recovery1 Aircooled orwater cooledcondenser

    50C 55CAdditionalrefrigerantfluid tank.

    g * *

    LDesuperheater

    DesuperheatedLiquid I GasGas

    IExpansionvalvei Compressorsrr I Partial heat recovery(Desuperheater) does not requireany additional electrical input. Itrecovers (8-12%) of waste heatfree of cost.

    Evaporator

  • B Hot Water Economics1/'W r ESTIMATES OF ANNUAL SAVINGS:

    V Pu

    X Hot water capacity : 10000 Lts/dayDiesel cost : 0.70$ per liter ;Diesel NCV :10100 Kcai/Liter;Boiler efficiency : 85%Saving by Heat Recovery system over diesel fired boiler7000 US$/year

    pFr., *r.L; w

    BL

    7474Adel Mourtada

  • Thermal Energy Storage System.frffini,p riri M iii- inn -J i r r.r.ri -i in- i-nn -innr ririr i ii. , i- n -i r, r r r iP! i.1 i . i -i ., -i i r r riri -i - ..i- i-.i-i.-i ri n ri-r nr. i-ii.....-.........................- -...............H..................------ pi -I

    IfHHMHfl H-IfKMMIU irMMWMtlIfKKNNWWlfKHM* HIf IfMHHMW IfKHMNUIfH'HWHH'HlfHHN'MI! WHHMSHflu\jirfitHMWHKSHtMSriM!H H ! MMMri S KHHHHH MMMHHM StSfiHMSIK MMMHHSiri SCMNHSiSfclfMKKMMMKSiHWMHMWKK ririMH :! !: HHHSfrKSLX : K : : : : x : : :: :::: : H X : : : : x : : -, ;.; : . , y xxx : , : -VJIKKKintSKK--; ...... ..... riri " - v v - " - v v . v K'KKKK'KriririKKJrtfKKKH

    JIHlIXitKIlirXIClXllMiCKXKXIEXKKllIiKOSXX XXXllDiXICKKKXXKlCKKlitKiCtKSXICXKXlliCXXliXXKKKllitltKKXlIXitXXX/::: :-! :-=MS:>: MMMK x x MMM:ri=i x MM x xlc>::-:ri riKKMXitri x KMWriri:-:KMMriri x x SCSririri riMUMriri ri x MM:: ririMMM::! x x MMWririHMMMK* x : \ri : x :>:>: x x : xx>:x x x : : : x : r-: x : :: : x x : ; c:: x x : x : : :: x - : x x : x : : v x x : ex x[SK--: : 1 v v 1 1 K 1 1 " 1 -'KKirwKKBKK'''WKKK'K'H'KKSS'KK'BKK'K'K'fKBKS''KKBKKKriririKKWf KEKSVlfiCi

    CKJb lUriA JI L phase change thermal energy storageTHS-W K WW-KKU'W ){JfKK WWKK'a;WKKS-W ririKKiS-W riririKK*!SKKKNUnifK'rCM-X K-riKH*1*KrKXKit K ifpSK K riK WKKMU'S J5CJ-

    ipffriipidpisolutionciSiM;th& followingi.:yy: ...:: x . : : : x : .. : : : :: :.: x x ; : .. : : : x :: . . . . * x .: x : : .. c: : . : : :: x : M! . .. . : : :K x=M|r; wsKKK SSKKHIKKKKKWKKKKK SSCWKS ;-= ;-= ;-H : =; x=|r:|r; wKKPW KKKKBKKKKKKBHWtfvvwvtrwvvwuirtfuwuvu-vwwirvww'uu-ww-uwwvwwww w v Kii"?ilKiSKK r riri-' -'i i'nitKKKH'KISKKllIKKKSMXiSK

    ,n n r .........- in.-i i n r- r r.r.pi .- ,n,-i -i n , r r......-.riHt-.................-i -.r - - ----1 .1.i 1.1 i - - r -MHMH H H-H'S-I-I!lI! H H II H HPHhlbl -III11- (a(d *|-H H H-l-

    FZTT. x::;-:-rr x x K?:::::K X KXXRX X X r-:x x ex x TT?:::::-: x x :-cxxx x x ?r:r :r:x x xxxxx x x?:r:r: :x* rx x x :-c::>:>: !

  • Some Possibilities with STLDtaiosgc

    =.5 I'joao 72 *O. 7

    It11v1.1 fituktfciiCbqt

    ? I'.L9 Cf?d2l 23!Hours JtHiMK

    TraditionalSolution.!

    Peak shaving withchiller switchedoff during highiafrriTpefiod ax 1.2m-L.LHU-HM-t 4T: jiii-s ?*> JJVaPeak shaving - KIII

    uiaiiyVW-i \/ i nAr [*TJ-TN _y

    1 2 r 5 4 : a in 1 1 12DfcdajpiJll1Pl L-dLhtn.M

    OlUff

    IULU-S ftl-

    t -iii')-> ZWr

    UL;[ luaiV L

    I.'T" Lf Ml& ammiu ,1 m It- 4mH I: 1 :f J iv(.;n iu 11 iZnvms mit i* 19 arzi iitfjv

    H*una-H

    I 2 3 -I i * 7 rf H In 1 1 I jm-l Ij Id 1 Ji 2 1 23Eli'ii11 /iiuuy

    Total storage during offpeak hours

    Chiller switched off during high pay ggperiod 4 yearstariff period

  • ALMEE

    r\MID-ENIC

    ALMEE TW rM * -wI

    ::: SjDescription of the project_Zgharta - North Lebanon _200 m ALT, 95 Km from Beirut1Building7 stories Hospital 1000 m3 floor110 beds , surgery X Ray. etc.Built in 1996.operating since 1997

    [ -IImil \Iw_

    p-

    w*

    9 ngtz OEC0FVS

  • ALMEE

    No Description KW /0 0 Save % of Investment PaybacYearsSaved Total total EurosAmount

    Euros BillKWh1 Roof thermal

    insulation2 Changing conventional

    fluorescent ballast toelectronic ballast andinstalling harmonic filter

    20,500 1.2 % 3.-200 C 1.3% 16,000 5

    9.1% 13,750 9.5% 25,000 1.3120,000

    3 Installation of BMS/DSM 160,000 N/A 23,125 C 11,7% 13,800 0.6retrofit system to ( of fuel)manage KW demandallowing operation on

    one 500 KVA Generator

    Total 300,500 45,075 C 22,5% 54,800 1.22

  • 9/f

    rfi*ur.il%

    Thank you for your attentionp

    )PtN

    ;'l 79Adel Mourtada

  • Annex

    - Instruments Required

    - Cost Effectives Measures

    BOAdel Mourtada

  • L Instruments Required/ Power Analyzer: Used for measuring electricalparameters of motors such as kW, kVA, pf, V, Aand Hz

    Temperature Indicator & Probe Pressure Gauge: To measure operating

    pressure and pressure drop in the system Stroboscope: To measure the speed of the

    driven equipment and motor Ultra sonic flow meter or online flow meter Sling hygrometer or digital hygrometer Anemometer In addition to the above calibrated online

    instruments can be used PH meter

    * * -i I *'

    iKl/= SJ ilh/*>

    0mmr \i u, PS

    siS

    & 81Adel Mourtada

  • Measurements & ObservationEnergy consumption pattern of pumps and coolingtower fansMotor electrical parameters (kw, kVA, Pf, A, V, Hz,THD) for pumps and cooling tower fans

    Pressure drop in the system (between dischargeand user point)

    > Pressure drop and temperatures across the users(heat exchangers, condensers, etc)

    > Cooling water flow rate to users - Pump /Motorspeed

    > Actualpressure at the user end> User area pressure of operation and requirement

    1

    LJ 0fcr> N1 1

    i-.

    82Adel Mourtada

  • Exploration of Energy Conservation Possibilities*> Water pumping and cooling towerImprovement of systems and drivesUse of energy efficient pumpsCorrecting inaccuracies of the Pump sizing / Trimming of

    impellersUse of high efficiency motorsIntegration of variable speed drives into pumps: The

    integration of adjustable speed drives (VFD) into compressorscould lead to energy efficiency improvements, depending onload characteristics

    High Performance Lubricants: The low temperature fluidityand high temperature stability of high performance lubricantscan increase energy efficiency by reducing frictional lossesImprovements in condenser performanceImprovement in cooling tower performanceApplication potential for energy efficient fans for cooling towerfansMeasuring and tracking system performance

    1 tffTjt!

    Liab':

    fcr> X

    83Adel Mourtada

  • Exploration of Energy Conservation Possibilities

    q Measuring water use and energy consumption isessential in determining whether changes inmaintenance practices or investment inequipment could be cost effective

    In this case it is advised to monitor the waterflow rate and condenser parameters, coolingtower parameters periodically i.e. at least oncein a three months and energy consumption ondaily basis. This will help in identifying the -- Deviations in water flow rates- Heat duty of condenser and cooling towers- Measures to up keep the performance

    *

    PCT' \

    84Adel Mourtada

  • h Exploration of Energy Conservation PossibilitiesSystem Effect Factors

    Equipment cannot perform at its optimum capacity iffans, pumps, and blowers have poor inlet and outletconditions

    Correction of system effect factors (SEFs) can havea significant effect on performance and energysavings

    Elimination of cavitation: Flow, pressure, andefficiency are reduced in pumps operating undercavitation. Performance can be restored tomanufacturers specifications through modifications.This usually invo ves inlet alterations and mayinvolve elevation of a supply tank

    mji

    .- J

    ML:

    i,i. 85Adel Mourtada

  • Exploration of Energy Conservation Possibilities

    Internal Running Clearances: The internal runningclearances between rotating and non-rotatingelements strongly influence the turbo machinesability to meet rated performance. Proper set-upreduces the amount of leakage (re-circulation) fromthe discharge to the suction side of the impeller

    Reducing work load of pumping: Reducing ofobstructions in the suction / delivery pipes therebyreduction in frictional losses. This includes removal ofunnecessary valves of the system due to changes.Even system and layout changes may help in thisincluding increased pipe diameter. Replacement ofcomponents deteriorated due to wear and tear duringoperation, modifications in piping system

    *

    r-LJ 0fcr> X1 1

    i-.

    86Adel Mourtada

  • Sources:

    a - Energy Equipments UNEP/SIDA/Gerlap,- HVAC System Design, Mark Hydeman, P.E., FASHRAETaylor Engineering, LLC.

    - Building Automatic System Bradley Chapman, DWEYER

    - Solar Cooling, Eco buildings, SARA.- Ventilation for buildings Energy performance of buildings Guidelines forinspection of air-conditioning systems- EN 15240, Intelligence Energy.- Energy Efficiency Guidelines, Brahm Segal, Power Correction System.

    - Results of HVAC system monitoring of tertiary buildings in Italy, M. Masoero,C. Silvi, J. Toniolo ,Politecnico di Torino, HarmonAC- Saving Energy Municipal Buildings and More, Ben J. Sliwinski BuildingResearch Council School of Architecture, University of Illinois at Urbana-Champaign. Kreider Curtis Rabl, Mac gGaw Hill.- Cleanrooms Energy Benchmarking, Lawrence Berkley laboratory.

    I

    ffCT* XI T

    87Adel Mourtada

    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