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PepsiCo - Palakkad
                  Water Conservation
                  Water Conservation


  CII National Award for Excellence in Water Management
                                                    Hy derabad
                        With in the Fence     December 16, 2008




Plant Overview

• Plant located in Industrial Development Area, Kanjikode
  in Kerala.
• Three filling lines
   – Glass line for CSD

   – PET line for CSD

   – Aqua Fina line

• Plot Area - 50.48 Acres

• Employment - 250




                                                                  1
Manufacturing Process
                                   Sugar Purification                                               CO2 Purification
                                                                                                                                        SILICA
                                                                                                                                       ALUMINA
     Sugar                                                                     CO                                                      CARBON
                                                                                                                                        MICRON
                                                                                 2
                          SUG R
                             A       CA B
                                        R ON     PA C LE
                                                    RTI      T MA
                                                             HER L                                       VAPORIZATION                 MULTI- MEDIA
                      DISSOLU N
                             TIO   PUR C A N
                                      IFI TIO   FI TR
                                                 L ATIO N   T TMEN
                                                            REA   T                                                                   FIL TRA ION
                                                                                                                                             T



                                                        Tre ate d                                                     Tre ate d
                                                     Liquid S ugar                                                      CO2


                                                                                                            Filling
                                                        Blendi ng
               Concentrate




• Tech nol og y-in tensiv e                                                             Tre ate d Water
• High precisi on                                                              Water Purification
  equi pme nt
                                                               COAGULATI N
                                                                        O
                                                                                  OZONE        SAND                        ULTRA
                                                             REVERS OSM
                                                                    E   OSIS
• Stringe nt proce ss                                          ION-E
                                                                   XCHANGE
                                                                                 CHLORINE     CARBON                       V
                                                                                                                           IOLET


  con trols to e nsure                     Water
  adhere nce to q uality                                        PRI A
                                                                   M RY            PR R
                                                                                     IMA Y    PAR LE
                                                                                                  TIC       M O
                                                                                                             ICR N          FINAL
                                                              PUR A N
                                                                 IFIC TIO      DISINF TIO
                                                                                     EC N    FILTR TIO
                                                                                                  A N      FILT TIO
                                                                                                              RA N     D FECTIO
                                                                                                                        ISIN      N
  stan dards.




    PepsiCo’s Vision

Positive water balance — going beyond zero
               Water Recharge a t
                   Plant lev el
                         +
               Water I nitiativ es at
                Com munity lev el
                         +
                                                                                     >                   Water used in
                                                                                                         manufacturi ng plants
                Promoting w ater
             Conserv ation measures
                 in agriculture


                CREDITS                                                              >                     DEBITS
        As a result of this focus, water was revalued




                                                                                                                                                     2
What we’ve accomplished on “debit” side of the
    equation

    SCO RECARD 2008                                4.5
                                                      4
    •    60% water u sage reduction in             3.5
         2008 over 2004 (4.41 to 1.77                 3
         L/L)                                      2.5
                                                      2
    •    77% reduction in effluent over
                                                   1.5
         2001(3.41 to 0.77 L/L)                       1
    •    The journey continues…                    0.5
                                                      0
                                                          2 004-      2 005-   2006-   2007-
                                                            05          06      07      08




        2008 vs. 2004: > 250 Million L saved
    2008: We could save another 16 Million liters

                Now…
                Now…what about the credits?




We continue to achieve water “credits” through
recharge of water resources

                              Surface water desilting chambers
•   Roof water harve sting                                              Water balance
    at our facilities                                                   •   Total Cons:153
•   Surface water                                                            – million L/ yr
    st ructure--pilots                                                  •   Total recharge:
        – Palakkad plant                                                     – 108 million
                                                                               L/yr
                                                                        •   The results:
                                                                               – 71%
                                                                                 recharge of
                                                                                 the aquifer at
                                                                                 Palakkad
                              Rain water su rface infiltration pond



    These results reinforced that our goal of positive water
                     balance is possible!




                                                                                                  3
Palakkad Water Strategy


                                                           In         4R
                                                        Process



  RWH
           Conse rve
            Source
          (Rechar ge)

                                 Water Strategy
                                                                 At
                                                              Discharge




                                                                    ZERO
                    In T he
                 Co mm un ity



                                CSR




Rain Water Harvesting




De silting chamber for pond
                   for pond


                                      Surf ace Water Harv esting – Palakkad Plant




                                                                                    4
Roof Water Harv esting – Palakkad Plant




                                          5
Global Best in Class WUR in Beverages
                  from Benchmarking Survey


             7
                                                             6.1
             6
                                                                           5.2
             5                                                                           4.7
Water Use Ratio




             4             0.8 L/L Better

             3                  2.5
                     2
             2                                 1.6                                                   1.7


             1
                                                         Palakkad
             0
                    CSD       CSD w/      Spring Water   Beer - Small Beer - Medium Beer - Large    Dairy
                             Refillable                   Brewery       Brewery      Brewery
                            Containers                                             Source: WBCSD R eport




       Zero based targeting


Roadmap for reduction
• Define specifications of water to be used at each step
  in the process
• Determine quantity and quality of discharge at each
  stage
• Identify opportunities for recycling, treatment and
  technology to be deployed
• Discard as effluent after establishing that it is unfit for
           recycling




                                                                                                            6
Water



                 Water use                            Water
                                                  sustainability
                optimization




Consu mption ETP lo ad                              Rain water
                         Recycle   Recover          harvesting
 Redu ction Redu ction




                 Imp act on
                   Energ y                   4R   Ground W ater
                                                      Table




          “When the well is dry, we learn
          the worth of water.”
                               --Benjamin Franklin




                                                                   7
Approach                          TPM WAY


•    Assess current situation
•    Estimate Losses
•    Take Loss Reduction Target
•    Identify Losses                                         PLAN
•    Identify Projects
•    Formation of Task force / Teams
•    Deploy 4R Tool                                                         DO
•    Implement Solutions             ACT
•    Check Results
•    Plan further actions

                                                             CHECK




    Estimate Losses


    • Best in Pepsi                           1.6 lits/lit
    • Palakkad plant @ 4.4 lits/lit (25 lit/8oz case) in 2004
    • Potential for reduction = 2.8 lits/lit ( 15.9 lit/8oz case)
       – This translate s to 350 kL of water sa ving potential per day.

    • Zero based calculation
       – 8 oz case content s         = 5.664 lits
       – Evaporation losse s         = 1.0 lits
       – This equals to 1.2 lits/lit of water consumed – this is the ab solute
          minimum if the effluent discharge from ETP is to be ZERO




                                                                                 8
Case Study

         Target                                                                                                                  Present
                                                                                                                                   1.69
                                                                                                                                  Ltr/Ltr

                                                              Av g for
          4.9                                                 2004-05
                                                              4.4 lit / li t
          4.4

          3.9
          3.4                                                                                                                                        G
                                                                                                                                                     O
          2.9
                                                                                                                                                     O
          2.4                                                                                                                                        D
          1.9
          1.4
                     2004            2005             2006           2007               2008         2009

                                                              Target lit/lit                 Achieved




         Reduction in Chemical Usage Over 2006
                                                          Chemical consumption Trend

         45000
         40000
         35000
         30000
         25000
In Kgs




         20000
         15000
         10000
         5000
            0
                         06




                                                                               07




                                                                                                                              8
                                                                     07




                                                                                                                     08
                                          06




                                                                                                      07




                                                                                                                                            08
                                                                                        07




                                                                                                                                      08
                                                          06




                                                                                                                                                       8
                06




                                 06




                                                  06




                                                                                                              07
                                                                                                     07




                                                                                                                             0




                                                                                                                                                    .0
                                                                 n




                                                                                                   p.
                     ar




                                                                                                                                           ly
                                                                                    ay




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               n




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                                 y




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                                                                Ja




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                              Ma




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                                               Se
                                      Ju




                                                                                             Ju
                     M




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                                                                                                                          M
                                                                                    M




                                                                                                                                  M




                                                                                                                                                 S




                                                                                         Month
                                                               Caustic                  Salt         HCL




                                                                                                                                                           9
Solid waste Management – ETP Sludge

                                           Sludge Generation Avg/Month

                     3500
                                3000
                     3000

                     2500
Solid waste in Kgs




                     2000

                     1500
                                                                                              Tar get
                     1000
                                                          588
                      500
                                                                             197
                                                                                          0
                        0
                               2006 - 07                2007 - 08          2008 - 09   2009 - 10
                                                                    year
                                           ETP Sludge




                                                             B ACKW ASH W ATER
                     RECOVER
                                                            STE AM CONDENS ATE

                                                             BOTTLE W ASHER

                                                            CIP WATER
                     REUSE
                                                            TRE ATED EFFLUENT


                                                             AF-RO REJ ECT
                     RECYCLE
                                                             PET RINSE W ATER

                                                                SF AIR SCORING
                     REDUCE
                                                                FLOOR CLE ANING




                                                                                                        10
Case Study


          Water Conservation

         REDUCTION OF WATER USE BY
           COMPLETE USAGE OF ETP
             TREATED EFFLUENT




AFRO Reject – Opportunity to Improve

  Opportunity: Currently AFRO reject being used in ETP
  Tertiary Treatment & permeate used for Utilities & TDS
  balancing.

  ETP Treated Effluent is having all the required parameters
  to treat through ETP UF RO, but due to AFRO reject
  availability Plant is using effluent for own land discharge to
  develop green field.

  Effective use of Treated Effluent through ETP UF RO could
  save another 17KL/Hr.




                                                                   11
PDCA
                                                               PI
                                                           Guidelines
                                                           for Usage


                Compile & Dis cus s
                                      PLAN
                    Findings
                 M odificat ions &           Reus e Pot ent ial
                    Addit ions



                 A CT                                     DO
                                                                        Why-Why
                    Pay Back                  Es timat e Cost           Analysis
                  Effect ivenes s             Rais e C APEX              done
                  Sus t ainabilit y           Define U s age
                                  CHEC K




Analysis for Reuse Potential

•   AFRO Reject is having more or less same Qualities of Raw Water

    due to permeate re-circulation.

•   Additional Generation of permeate through new CSD RO could save

    another 12 KL/Hr out of 17KL which is now being pumped to ETP

    UF RO.

•   Proposed CSD RO can be able to treat this Reject.

•   This phenomenon prompted team to work on e stimated reduction of

    TDS through New RO.




                                                                                   12
Estimated Savings

• AFRO Run Hours/Day: 20
• Total Reject Generation @ 17KL= 17*20 = 340 KL
• Permeate Generation through proposed CSD RO @
  12KL/Hr for 20 Hrs = 12*20 = 240 KL
• Balance 100KL will be pumped to ETP UF RO.
• There will be direct reduction of 240KL/Day in Gross
  Water Usage of Plant.



              Approximate 7 0 Mill ion L ann uali ze d Water Sav ings




TASK PLANNING – 5W-1H
What          Where          When         Who           Why             How?


Reduce    ETP UFRO           Daily        QC            This             Reuse
Usage of  f eed                           Exec/ETP      activ ity       AFRO
AFRO                                      associate     propmts         Reject in
Reject in                                               complete        the process
ETP UFRO                                                recy cle of     only .
                                                        Tre ated
                                                        Eff luent.
Reuse of      WTP &                                                     Propose f or
AFRO          Production     During       QC            To optimi ze    New RO in
Reject f or   processes      AFRO         Exec/WTP      the water       CSD WTP
process                      Run          associate     consumptio      to recycle
                                                        n of the        AFRO
                                                        Plant           reject.




                                                                                       13
PROPOSED CSD RO SCHEMATIC
WITH TDS BALANCING
                                                                              Bore Well Water
                                        BoreWel l Water              ST-
               UG Sump                  BoreWel l Water
                450 KL
                                                                     22 KL @ 550TDS                       < 10 T ,4 KL
                                                                                                                DS

                                                          Rej ect
                                                                     AQUA     26KL @500 TDS             Permeate @<10 TDS

                                                                     SUMP                         AF RO

                    PSF                           RAW
                               ACF                    Permeate
                                                 W R
                                                  ATE
                      2         3
                                                    RO                                          Reject @ 800 TDS            For Aqu n Producti on
                                                                                                                                   afi a
                                       11KL @ 15 ppm TDS

         ST-




                                                                                       1 KL Mi scell aneous *

                                                                                       8 KL for G *
                                                                                                 RB
            SR.COAG 620TDS        INTERME        <400TDS     PSF    ACF      ACF
  38 KL @ 800 Tds                 DIATE                       1      1        2        18 KL for PET*



                                                                                                                Propose d Reuse
* Maximum LimitsMen tioned For FLO W
* Mi n mu L mits Mentioned For TDS
      i m i




                          New CSD RO
                                                                            Suppli er: GE Water
                                                                            Capacity : 12KL/Hr
                                                                            Project Cost: 40 Lac
                                                                            Time                    : 6 Weeks




                                                                                                                            AF Reject
                                                                                                                         Collection Tank




                                                                                                                                                    14
Consumption Target – Total Plant



                      2
                  1.95             1.94
                   1.9
                  1.85
              %




                   1.8
                                             1.77
                  1.75
                   1.7
                  1.65
                           2007           2008

                                                        KL/Day
     REDUCTION OF 0.17 L/L TRANSL A TES TO REDUCTION OF 120 KL/DAY




 Actions towards Water reduction

Sr              Actions                              Benefits                   Cost      Date
                                                                               Rs’000
1     Wor kout TD S esti mati ons         Proper usag e i denti fication for            Wk – 1
      pre & exi t R O and                 Reject Str eam & D esign
      proposed us e.                      consider ation
2     Esti mate N et Benefit to           Esti mati ng Pay Bac k &                      Wk – 2
      the Plant and esti mated            Res ourc e Sustai nabilit y
      water us age r ati o.

3     Provi de 50KL Storag e              Storag e AFRO rej ect in c ase        450     Wk – 3
      tanks for both feed &               any s toppag es i n the new C SD
      per meate.                          RO.

4     Re-dir ect Rej ect line to          Enable AFR O storag e                 100     Wk – 4
      CSD R O F eed T ank.

5     Connect CSD R O                     Per meate us age opti miz ati on      100     Wk – 5
      per meate to Stor age               based on the r equirement
      Tank.




                                                                                                 15
Result of New CSD RO Project

                 300
                                                                                                    70% of
 Savings in KL


                                                                                               Targeted Overall
                                                                                       240    240 240
                                                                                                   Savings
                                                         200     220     220    220
                 200                     180       180
                               160
                          140
                                                                                                                  G
                                                                                                                  O
                 100
                                                                                                                  O
                                                                                                                  D


                   0
                                                                  Y




                                                                                 Y
                                               B




                                                                          E




                                                                                              PT
                                                                                        G
                          EC


                                     N
                     V




                                                    AR


                                                            R

                                                                 A


                                                                         N
                                          FE




                                                                                 L

                                                                                      AU
                    O




                                JA




                                                          AP




                                                                               JU
                                                                       JU




                                                                                             SE
                                                   M




                                                                M
                         D
                   N




                                                                Month




 Imple mentation

• 2 Major Projects Implemented in 2007-08 resulting in
        Annualized Water Savings of 70,000 KL (CSD RO & AF
        Rinse Water Recovery)
• Redesign, Rethink initiatives Identified & implemented,
        resulting in a saving of 15,000 KL in the year 2008.
• 18 Core consumption points metered on daily basis.
• Abnormalities paid higher attention by top to bottom.




                                                                                                                      16
Results


       4.9
       4.4
       3.9
                                                         Backwash
       3.4
                                                         Recover y            G
       2.9                                                                    O
       2.4                                                                    O
                                                                              D
       1.9
       1.4
              2004        2005   2006     2007       2008      2009

                                   Target lit/l it    Actual l it/ lit

              B/W                                                         NEW
          Dacausticizer
            Recovery
                                                                         CSD RO




Overall Results


•   Total Savings of 240 Million Ltrs over 2004.
•   No.2 on YTD Basi s acro ss 43 Pepsi Plants in India with 1.69 Lit/Lit
    Water Con sumption.

•   Zero Di scharge from the plant
•   Controlled Effluent Generation. (0.69 KL/KL of Bev)




                                                                                  17
Way Forward

  •Identifying further opportunities to save water through proce ss
  effectiveness.

  •Rede sign & Rethink Strategy added to 4R (No other stream
  available to deploy 4R)

  •Reduction of Effluent by adopting latest technologies. (Electro
  Chlorinator)

  •Optimizing total recovery from the existing water recovery
  sy stem s.

  •Con sulting Experts to generate ideas on water con servation.




“The significant problems we face cannot be solved at the same level
of thinking we were at when we created them.”

                                                  --Albert Einstein




                                                                       18
THANK YOU!




             19

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PepsiCo, Palakaad

  • 1. PepsiCo - Palakkad Water Conservation Water Conservation CII National Award for Excellence in Water Management Hy derabad With in the Fence December 16, 2008 Plant Overview • Plant located in Industrial Development Area, Kanjikode in Kerala. • Three filling lines – Glass line for CSD – PET line for CSD – Aqua Fina line • Plot Area - 50.48 Acres • Employment - 250 1
  • 2. Manufacturing Process Sugar Purification CO2 Purification SILICA ALUMINA Sugar CO CARBON MICRON 2 SUG R A CA B R ON PA C LE RTI T MA HER L VAPORIZATION MULTI- MEDIA DISSOLU N TIO PUR C A N IFI TIO FI TR L ATIO N T TMEN REA T FIL TRA ION T Tre ate d Tre ate d Liquid S ugar CO2 Filling Blendi ng Concentrate • Tech nol og y-in tensiv e Tre ate d Water • High precisi on Water Purification equi pme nt COAGULATI N O OZONE SAND ULTRA REVERS OSM E OSIS • Stringe nt proce ss ION-E XCHANGE CHLORINE CARBON V IOLET con trols to e nsure Water adhere nce to q uality PRI A M RY PR R IMA Y PAR LE TIC M O ICR N FINAL PUR A N IFIC TIO DISINF TIO EC N FILTR TIO A N FILT TIO RA N D FECTIO ISIN N stan dards. PepsiCo’s Vision Positive water balance — going beyond zero Water Recharge a t Plant lev el + Water I nitiativ es at Com munity lev el + > Water used in manufacturi ng plants Promoting w ater Conserv ation measures in agriculture CREDITS > DEBITS As a result of this focus, water was revalued 2
  • 3. What we’ve accomplished on “debit” side of the equation SCO RECARD 2008 4.5 4 • 60% water u sage reduction in 3.5 2008 over 2004 (4.41 to 1.77 3 L/L) 2.5 2 • 77% reduction in effluent over 1.5 2001(3.41 to 0.77 L/L) 1 • The journey continues… 0.5 0 2 004- 2 005- 2006- 2007- 05 06 07 08 2008 vs. 2004: > 250 Million L saved 2008: We could save another 16 Million liters Now… Now…what about the credits? We continue to achieve water “credits” through recharge of water resources Surface water desilting chambers • Roof water harve sting Water balance at our facilities • Total Cons:153 • Surface water – million L/ yr st ructure--pilots • Total recharge: – Palakkad plant – 108 million L/yr • The results: – 71% recharge of the aquifer at Palakkad Rain water su rface infiltration pond These results reinforced that our goal of positive water balance is possible! 3
  • 4. Palakkad Water Strategy In 4R Process RWH Conse rve Source (Rechar ge) Water Strategy At Discharge ZERO In T he Co mm un ity CSR Rain Water Harvesting De silting chamber for pond for pond Surf ace Water Harv esting – Palakkad Plant 4
  • 5. Roof Water Harv esting – Palakkad Plant 5
  • 6. Global Best in Class WUR in Beverages from Benchmarking Survey 7 6.1 6 5.2 5 4.7 Water Use Ratio 4 0.8 L/L Better 3 2.5 2 2 1.6 1.7 1 Palakkad 0 CSD CSD w/ Spring Water Beer - Small Beer - Medium Beer - Large Dairy Refillable Brewery Brewery Brewery Containers Source: WBCSD R eport Zero based targeting Roadmap for reduction • Define specifications of water to be used at each step in the process • Determine quantity and quality of discharge at each stage • Identify opportunities for recycling, treatment and technology to be deployed • Discard as effluent after establishing that it is unfit for recycling 6
  • 7. Water Water use Water sustainability optimization Consu mption ETP lo ad Rain water Recycle Recover harvesting Redu ction Redu ction Imp act on Energ y 4R Ground W ater Table “When the well is dry, we learn the worth of water.” --Benjamin Franklin 7
  • 8. Approach TPM WAY • Assess current situation • Estimate Losses • Take Loss Reduction Target • Identify Losses PLAN • Identify Projects • Formation of Task force / Teams • Deploy 4R Tool DO • Implement Solutions ACT • Check Results • Plan further actions CHECK Estimate Losses • Best in Pepsi 1.6 lits/lit • Palakkad plant @ 4.4 lits/lit (25 lit/8oz case) in 2004 • Potential for reduction = 2.8 lits/lit ( 15.9 lit/8oz case) – This translate s to 350 kL of water sa ving potential per day. • Zero based calculation – 8 oz case content s = 5.664 lits – Evaporation losse s = 1.0 lits – This equals to 1.2 lits/lit of water consumed – this is the ab solute minimum if the effluent discharge from ETP is to be ZERO 8
  • 9. Case Study Target Present 1.69 Ltr/Ltr Av g for 4.9 2004-05 4.4 lit / li t 4.4 3.9 3.4 G O 2.9 O 2.4 D 1.9 1.4 2004 2005 2006 2007 2008 2009 Target lit/lit Achieved Reduction in Chemical Usage Over 2006 Chemical consumption Trend 45000 40000 35000 30000 25000 In Kgs 20000 15000 10000 5000 0 06 07 8 07 08 06 07 08 07 08 06 8 06 06 06 07 07 0 .0 n p. ar ly ay ar n ly ar ly n ay v ep y p v Ja Ja No Ja No Ma Ju Se Se Ju Ju M M M M M S Month Caustic Salt HCL 9
  • 10. Solid waste Management – ETP Sludge Sludge Generation Avg/Month 3500 3000 3000 2500 Solid waste in Kgs 2000 1500 Tar get 1000 588 500 197 0 0 2006 - 07 2007 - 08 2008 - 09 2009 - 10 year ETP Sludge B ACKW ASH W ATER RECOVER STE AM CONDENS ATE BOTTLE W ASHER CIP WATER REUSE TRE ATED EFFLUENT AF-RO REJ ECT RECYCLE PET RINSE W ATER SF AIR SCORING REDUCE FLOOR CLE ANING 10
  • 11. Case Study Water Conservation REDUCTION OF WATER USE BY COMPLETE USAGE OF ETP TREATED EFFLUENT AFRO Reject – Opportunity to Improve Opportunity: Currently AFRO reject being used in ETP Tertiary Treatment & permeate used for Utilities & TDS balancing. ETP Treated Effluent is having all the required parameters to treat through ETP UF RO, but due to AFRO reject availability Plant is using effluent for own land discharge to develop green field. Effective use of Treated Effluent through ETP UF RO could save another 17KL/Hr. 11
  • 12. PDCA PI Guidelines for Usage Compile & Dis cus s PLAN Findings M odificat ions & Reus e Pot ent ial Addit ions A CT DO Why-Why Pay Back Es timat e Cost Analysis Effect ivenes s Rais e C APEX done Sus t ainabilit y Define U s age CHEC K Analysis for Reuse Potential • AFRO Reject is having more or less same Qualities of Raw Water due to permeate re-circulation. • Additional Generation of permeate through new CSD RO could save another 12 KL/Hr out of 17KL which is now being pumped to ETP UF RO. • Proposed CSD RO can be able to treat this Reject. • This phenomenon prompted team to work on e stimated reduction of TDS through New RO. 12
  • 13. Estimated Savings • AFRO Run Hours/Day: 20 • Total Reject Generation @ 17KL= 17*20 = 340 KL • Permeate Generation through proposed CSD RO @ 12KL/Hr for 20 Hrs = 12*20 = 240 KL • Balance 100KL will be pumped to ETP UF RO. • There will be direct reduction of 240KL/Day in Gross Water Usage of Plant. Approximate 7 0 Mill ion L ann uali ze d Water Sav ings TASK PLANNING – 5W-1H What Where When Who Why How? Reduce ETP UFRO Daily QC This Reuse Usage of f eed Exec/ETP activ ity AFRO AFRO associate propmts Reject in Reject in complete the process ETP UFRO recy cle of only . Tre ated Eff luent. Reuse of WTP & Propose f or AFRO Production During QC To optimi ze New RO in Reject f or processes AFRO Exec/WTP the water CSD WTP process Run associate consumptio to recycle n of the AFRO Plant reject. 13
  • 14. PROPOSED CSD RO SCHEMATIC WITH TDS BALANCING Bore Well Water BoreWel l Water ST- UG Sump BoreWel l Water 450 KL 22 KL @ 550TDS < 10 T ,4 KL DS Rej ect AQUA 26KL @500 TDS Permeate @<10 TDS SUMP AF RO PSF RAW ACF Permeate W R ATE 2 3 RO Reject @ 800 TDS For Aqu n Producti on afi a 11KL @ 15 ppm TDS ST- 1 KL Mi scell aneous * 8 KL for G * RB SR.COAG 620TDS INTERME <400TDS PSF ACF ACF 38 KL @ 800 Tds DIATE 1 1 2 18 KL for PET* Propose d Reuse * Maximum LimitsMen tioned For FLO W * Mi n mu L mits Mentioned For TDS i m i New CSD RO Suppli er: GE Water Capacity : 12KL/Hr Project Cost: 40 Lac Time : 6 Weeks AF Reject Collection Tank 14
  • 15. Consumption Target – Total Plant 2 1.95 1.94 1.9 1.85 % 1.8 1.77 1.75 1.7 1.65 2007 2008 KL/Day REDUCTION OF 0.17 L/L TRANSL A TES TO REDUCTION OF 120 KL/DAY Actions towards Water reduction Sr Actions Benefits Cost Date Rs’000 1 Wor kout TD S esti mati ons Proper usag e i denti fication for Wk – 1 pre & exi t R O and Reject Str eam & D esign proposed us e. consider ation 2 Esti mate N et Benefit to Esti mati ng Pay Bac k & Wk – 2 the Plant and esti mated Res ourc e Sustai nabilit y water us age r ati o. 3 Provi de 50KL Storag e Storag e AFRO rej ect in c ase 450 Wk – 3 tanks for both feed & any s toppag es i n the new C SD per meate. RO. 4 Re-dir ect Rej ect line to Enable AFR O storag e 100 Wk – 4 CSD R O F eed T ank. 5 Connect CSD R O Per meate us age opti miz ati on 100 Wk – 5 per meate to Stor age based on the r equirement Tank. 15
  • 16. Result of New CSD RO Project 300 70% of Savings in KL Targeted Overall 240 240 240 Savings 200 220 220 220 200 180 180 160 140 G O 100 O D 0 Y Y B E PT G EC N V AR R A N FE L AU O JA AP JU JU SE M M D N Month Imple mentation • 2 Major Projects Implemented in 2007-08 resulting in Annualized Water Savings of 70,000 KL (CSD RO & AF Rinse Water Recovery) • Redesign, Rethink initiatives Identified & implemented, resulting in a saving of 15,000 KL in the year 2008. • 18 Core consumption points metered on daily basis. • Abnormalities paid higher attention by top to bottom. 16
  • 17. Results 4.9 4.4 3.9 Backwash 3.4 Recover y G 2.9 O 2.4 O D 1.9 1.4 2004 2005 2006 2007 2008 2009 Target lit/l it Actual l it/ lit B/W NEW Dacausticizer Recovery CSD RO Overall Results • Total Savings of 240 Million Ltrs over 2004. • No.2 on YTD Basi s acro ss 43 Pepsi Plants in India with 1.69 Lit/Lit Water Con sumption. • Zero Di scharge from the plant • Controlled Effluent Generation. (0.69 KL/KL of Bev) 17
  • 18. Way Forward •Identifying further opportunities to save water through proce ss effectiveness. •Rede sign & Rethink Strategy added to 4R (No other stream available to deploy 4R) •Reduction of Effluent by adopting latest technologies. (Electro Chlorinator) •Optimizing total recovery from the existing water recovery sy stem s. •Con sulting Experts to generate ideas on water con servation. “The significant problems we face cannot be solved at the same level of thinking we were at when we created them.” --Albert Einstein 18