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PIPELINE OPERATIONS
           THROUGH SCADA


                                       K Kumar
                                    DGM(T&I), PL . HO


PIPELINE OPERATIONS THROUGH SCADA
SCADA

     Objectives of SCADA system

     •   To provide effective & efficient monitoring and control of
         entire pipeline network.
     •   Remote control of important station equipment, process set
         points & block valves from SCC / MCC.
     •   Emergency shutdown of entire pipeline from MCC.
     •   Acquisition & display of pipeline parameters, alarms from
         attended stations, scraper stations, C.P. Stations & block
         valves at MCC.




PIPELINE OPERATIONS THROUGH SCADA
TYPICAL ORIGINATING PUMP STN LINE DIAGRAM
                                                      STRAINER   FLOW    MASTER
                              BOOSTER SECTION
                                                       SECTION   METER   METER



          TANKS




                                                                                           DENSITY
                                                                                            METER




                                  MAINLINE
                               PUMPING SECTION




                                                                                        SUMP
                                                                                       PUMP &
                                                                                        TANK




              MOV              PRESSURE/TEMPERATURE
                                    INSTRUMENTS                            SCRAPPER
                                                                          LAUNCHING
              NRV
                                                                          BARRELTION

              HOV
PIPELINE OPERATIONS THROUGH SCADA
TANK AND MANIFOLD INTERLOCKS LOGIC
         LS,
         LT
                                    TANK LINEUP CONDITIONS:

                                    1.   Sufficient ullage in the tank ensured by LT.
                                    2.   Tank Valve will be opened when there is no
                                         Low Alarm
                                    3.   System will allow only one tank valve at a time.
                    TO BOOSTERS     4.   During changeover 25% valve opening gives
                                    5.   command for the closure of other tank valve.
                                    6.   Manifold valve operation is also similar.
                                    7.   Failure of above operation, sequence incomplete
                 MANIFOLD
                                         condition will ensure shutdown of equipments.




PIPELINE OPERATIONS THROUGH SCADA
BOOSTERS LINE UP LOGIC
                BOOSTERS

                                    1.   Any one of the tank and manifold valve
                                         should be inn open condition.
                                    2.   Discharge valve of the booster should be
                                         closed.
                                    3.   No faults in the booster alarms should exist.
                                    4.   Maximum only 2 Nos. of boosters can start.
                                    5.   Start command opens cution valve, then to
                                         pump. Once pump runs discharge valve is
                                         opened.
                                    6.   Suction Pressure alarm comes online after a
                                         time delay.
                                    7.   Any alarm initiation trips the boosters.




PIPELINE OPERATIONS THROUGH SCADA
MAINLINE PUMP LINE UP LOGIC
        1. Mainline Pumps are either Engine Driven or Motor Driven.
        2. In case of Engine Driven Pump, a self contained control panel
           ensures the healthy status of all engine/pump parameters.
        3. In case of Motor Driven Pump, the health of the equipment is
           monitored directly by the SCC.
        4. Precondition to start : Discharge valve should be closed, No fault
           condition exist confirms the availability of the equipment.
        5. Start command opens suction valve, then to pump. Once pump runs
           opens discharge valve.
        6. Any failure in the sequence will not allow the pump to start.
        7. While pump running, any alarm of the pump/station like high discharge, ESD,
           Sump Tank Level Hi-Hi etc. will trip the system and isolates the system by
           closing the valves.
        8. All important alarms are derived from Primary instruments as well as
           secondary instruments to ensure fail safe operation.




PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
DISCHARGE MOV
                  FAILED TO CLOSE
                WITH IN PRESET TIME?
                      (120 SEC)




PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
AUTOMATIC CONTROL OPERATION
          PT
                            PT
                                              MAINLINE PUMPING UNITS
               BP                                                                                 PI        PS   PT
TANK                                TM


                                         PI         PS   PI   PI        PS         PI   PI   PS
                                                                                                       PI
                                         PS              PS   PS                   PS   PS
                    BP                                                                             PS




  PID LOOP
                           SET POINT
                         CONTROLLERS
                           FP

                                              LOW
                                                                   GOVERNOR /
                           SP                 SIGNAL               VFD / CONTROL
                                                                   VALVE
                                              SELECTOR


                           DP


PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
TYPICAL CONTROL LOOP OF RECEIVING STATION
          PT       PS    PI                        PI
                                  SD


                                             SRB
         SD

         PCV
                    PT

                                                        BP    LOW
                              S
                                       DPI
                              T
                              R.
                                                              SIGNAL

                                                        FC
                                                              SELECT
                                                              OR
               T              T
               M                                        LS,
                              M                         LT



                   PS    PT

                                  DM




PIPELINE OPERATIONS THROUGH SCADA
PIPELINE OPERATIONS THROUGH SCADA
LOCAL CONTROL SYSTEM /
                 PROGRAMMABLE LOGIC CONTROL SYSTEM


     OBJECTIVES ARE -LOGIC CONTROL - PROCESS CONTROL
                 COMMUNICATION WITH SCC



                                       Digital I/Os
                                       Analog I/Os
                               CPU & Communication interface


                                         Field Instruments
PIPELINE OPERATIONS THROUGH SCADA   Independent Control System Irrespective of SCADA
CONTROL SYSTEM
                                During the scan, a PLC …



                                               Monitors Inputs




          Scan                                Executes Program




                                              Changes Outputs

                                                                 20
PIPELINE OPERATIONS THROUGH SCADA
TYPICAL SCADA ARRANGEMENT


                                          MCC



                                    COMMUNICATION
                                       SERVER
                                                           COMMUNICATION LINK



            SCC,                                 SCC,                             SCC,
         Originating          BV    BV      Intermediate       BV               Delivery
           Station           RTU    RTU        Station         RTU               Station




PIPELINE OPERATIONS THROUGH SCADA
APPLICATION SERVERS (32           DUAL REDUNDANT SCADA                    OPERATOR
   ENGG/PROGRAMMING           BIT)                     MCS cum SCC SERVERS (32            WORKSTATIONS (32BIT)                             SIC terminal (32 BIT)
    TERMINAL 15” Flat     15” Flat Mon.                          BIT)                         19” Fat Mon.             50”TFT                 15” Flat Mon.
          Mon.                                               15” Flat Mon.                                             Screen
                                                                                                                       Display




                                                                                                            DUAL REDUNDANT
                                                                                                         100 MBPS ETHERNET LAN



                                                                                                                                                    In owner’s OFC
                                                                                                                                                   based
                                                                                  Interface between                                                communication
        RTU / PLC                                                                Printers & Dual LAN
                                                                                                                                                   system provision
   CPU, Memory,      P   C   C    I                       P   C   C   I                                                                            shall be made for
   comm. Module, I/O S   P   O    O                       S   P   O   O
                                                                                                                                                   Ethernet Interface
   controller, power U   U   M    C                       U   U   M   C
   supply
                                                                                                          DOT MATRIX
                                                                                                                                                   point to point
                                                                                                           PRINTER                                 redundant
                                                                                                                                                   communication
                                                                                                                   Communication                   with each PLC of
                                                                                                                    Server / FES
                                                                                                                                                    SCCs
                                                                                                                                        Ethernet
                                                                                                        LASERJET
                                                                                                         PRINTER
                                                                                                                                                   Multi drop
                                                                      I/O MODULES
                                                                                                                                                   redundant
                                                                                                                                                   communication
                                                                                                                                                   with RTUs of
                                 MODBUS Interface                                                                                                  block valves
                                                                          FIELD DEVICES
                                 to third party                                                                                  V.28/Ethernet
                                  devices e.g. flow
                                 computers, RTG,
                                 VFD etc.



                                                                             TYPICAL MCS cum SCC CONFIGURATION


PIPELINE OPERATIONS THROUGH SCADA
SCADA
    Major functions of SCADA system –
       • Data acquisition / Communication

          • Alarm & Event processing

          • Control processing/commands

          • Trend generation

          • Shift / Daily /Maintenance Reports

          • Management Information Reports
                                                 23
PIPELINE OPERATIONS THROUGH SCADA
APPLICATION SOFTWARE
   • LEAK DETECTION & LOCATION MODULE
               Sensing Pipeline Leakage and Location
   • BATCH TRACKING/INTERFACE ANALYSIS
               Calculation of motion and position of batches
   • PIG TRACKING
               Tracks Movement of pig
   • LOOK AHEAD MODEL
               To predict future trends of pressures and flow with respect to pump changes
   • PIPELINE EFFICIENCY
               Recommends for cleaning of pipeline
   • PREDICTIVE MODEL
              Simulates the hydraulic dynamics of the pipeline (Offline)



PIPELINE OPERATIONS THROUGH SCADA
LEAK DETECTION SYSTEM
        Typical Leak detection system consists following software
        modules :
        WHEN LINE IN OPERATION
           Pressure & Flow Profile Module / Pressure Wave Module
                                       -To detect leak and location
         Volume balance method : To detect leak only
        UNDER SHUT IN CONDITION
            Pressure wave module : To detect leak and location
            Pressure Drop method : To detect leak only


PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
                       Dynamic flow balance method


           A simple LDS could be based upon detecting an
            imbalance between a measured inlet flow and a
            measured outlet flow (ie Net Volume Line
            Balance)




                   Qin                                        Qout

PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
                       Ideal Pressure Control Upstream

                  Pu
                                        Normal Pressure Profile

                  Pressure

                                Pressure Profile fully
                                developed due to leak
                                                                       PDCALC
                                                         Pipe Length

                                                                        UPD
           With ideal pressure control upstream                       PDMEAS
              UPD = PDCALC - PDMEAS
               UPD        is Unexpected Pressure Downstream
               PDCALC     is Calculated Pressure Downstream
               PDMEAS     is Measured Pressure Downstream
           UPD = 0 implies no leak


PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
               Ideal Pressure Control Upstream

           The pressure profile is capable of indicating leaks, but
              small leaks have minimal effect on pressure

              the leak cannot be located

              difficult to filter out normal pressure variations

           Profiling the flow using flow control downstream
            increases the model accuracy




PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
      Pressure Profiling (Upstream Pressure Control)

   Pu
                            Normal Pressure Profile
                                                Pressure Profile under
Pressure                                        development due to leak (dashed
                                                lines)
                    Pressure Profile fully
                    developed due to leak
   Pd
                                            Pipe Length




PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
               Ideal Flow Control Downstream
                               Flow Profile fully developed
                               due to leak
            QUMEAS
               UFU
            QUCALC        Normal Flow Profile
                   Flow


                                                         Pipe Length



            With ideal flow control downstream
               UFU = QUMEAS - QUCALC
                UFU        is Unexpected Flow Upstream
                QU  CALC
                           is Calculated Flow Upstream
                QU  MEAS
                           is Measured Flow Upstream
            UFU = 0 implies no leak



PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
           Flow Profiling (Downstream Flow Control)

                   Flow Profile fully
 QU                developed due to leak


 QD
           Normal Flow Profile
                                                          Flow Profile under development
  Flow                                                          due to leak (dashed lines)

                                            Pipe Length




PIPELINE OPERATIONS THROUGH SCADA
MODEL BASED LEAK
                   DETECTION




PIPELINE OPERATIONS THROUGH SCADA
LDS Functional Overview
                            Response Time Series




   response
                                      .                               threshold


                                                                      time
                                      t1            t2
                                                                      event periods
             leak           level 1       level 2   level 3   level 4 response levels
            occurs
                              detection time

PIPELINE OPERATIONS THROUGH SCADA
PRESSURE DROP METHOD- leak notified




PIPELINE OPERATIONS THROUGH SCADA
Typical leak sensitivity data on dynamic flow



        % leak                      Location   time

        2%                          + 10 km    20-30 mins

        5%                          + 5 km     15-20 mins

        10%                         + 2 km     5 mins



PIPELINE OPERATIONS THROUGH SCADA
APPLICATION SOFTWARE
   • LEAK DETECTION & LOCATION MODULE
               Sensing Pipeline Leakage and Location
   • BATCH TRACKING/INTERFACE ANALYSIS
               Calculation of motion and position of batches
   • PIG TRACKING
               Tracks Movement of pig
   • LOOK AHEAD MODEL
               To predict future trends of pressures and flow with respect to pump changes
   • PIPELINE EFFICIENCY
               Recommends for cleaning of pipeline
   • PREDICTIVE MODEL
              Simulates the hydraulic dynamics of the pipeline (Offline)



PIPELINE OPERATIONS THROUGH SCADA
SYSTEM RELIABILITY
1. MAJOR EQUIPMENT LIKE PLC, SCADA SERVER ARE AVAILABLE
   IN HOT STANDBY MODE. ONLY STANDBY IS NOT AVAILABLE
   FOR RTUs.

2. FAILURE OF COMMUNICATION WILL INHIBIT THE CONTROL
   COMMANDS. ALTERNATE HIREDCOMMUNICATION TO SCCs
   WILL HELP IN OPERATING FROM MCC WITHOUT APPLICATION
   SOFTWARE .

3. STATION LEAKAGES CANNOT BE DETECTED. CCTV WITH
   MOTION SENSOR – GENERATE ALARM

4. PROPER MAINTENANCE OF STATION WITH TO REGARD
   LEAKS/EQUIPMENT CAN ENSURE RELIABLE FUNCTIONING OF
   SCADA SYSTEM
38
PIPELINE OPERATIONS THROUGH SCADA
SYSTEM CAPABILITIES AND BENEFIT
     OPERATIONAL INFORMATION AND CONTROL

   Data is acquired from field sensors / instruments
   Data is processed for monitoring and control of
    Engines/Motors, Valves etc.
   Supports operator decisions; reports and isolates abnormal
    situations
   Operator settable alarms for station from centralized master
    station for pressure and flow
   Emergency shutdown of entire pipeline from MCC in a
    defined sequence starting from the terminal station so as to
    keep the line pressurized .
   Acquires and displays repeater data such as pressure,
    temperature, MOV status, intrusion alarms.
   The block valve under the respective station can be locally
    controlled by the station control centre in case master-
    station communication fails.
SYSTEM CAPABILITIES AND BENEFIT
    OPERATIONAL INFORMATION AND CONTROL
     Data is communicated over dedicated Communication channels
      to local and centrally located system at remote
     When the communication between master and local station/
      repeater fails, the system maintains the previous state of
      operationi.e. there shall not be operational shutdwn.
     Communication failure indication shall be messaged to the
      operator.
     While controlling the SCC from MCC by way of commands or
      change of set points, confirmation is sought from the address
      before execution of command/ change of set point takes place.
     Bump less transfer from local station control to Master station
      and Vice versa.
     Can remotely prove the flow meters and effect calibration
      factors.
SYSTEM CAPABILITIES AND BENEFIT
             MAINTENANCE BENEFITS
    Data is stored as history
    Archives data and alarms for future analysis
    Generates hourly and daily shift reports
    Generates equipment running hour report
    Acquires and displays parameters of CP system such
     as power availability, PSP etc.
    Remote and auto start of DG set in RCPs
    Event database will maintain all alarms, alarm
     acknowledgements, return to normal process,
     operator control actions.
    On-line data base can be modified from Master.
    Permits security level log-ins.

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Optimizing Pipeline Operations with SCADA Monitoring

  • 1. PIPELINE OPERATIONS THROUGH SCADA K Kumar DGM(T&I), PL . HO PIPELINE OPERATIONS THROUGH SCADA
  • 2. SCADA Objectives of SCADA system • To provide effective & efficient monitoring and control of entire pipeline network. • Remote control of important station equipment, process set points & block valves from SCC / MCC. • Emergency shutdown of entire pipeline from MCC. • Acquisition & display of pipeline parameters, alarms from attended stations, scraper stations, C.P. Stations & block valves at MCC. PIPELINE OPERATIONS THROUGH SCADA
  • 3. TYPICAL ORIGINATING PUMP STN LINE DIAGRAM STRAINER FLOW MASTER BOOSTER SECTION SECTION METER METER TANKS DENSITY METER MAINLINE PUMPING SECTION SUMP PUMP & TANK MOV PRESSURE/TEMPERATURE INSTRUMENTS SCRAPPER LAUNCHING NRV BARRELTION HOV PIPELINE OPERATIONS THROUGH SCADA
  • 4. TANK AND MANIFOLD INTERLOCKS LOGIC LS, LT TANK LINEUP CONDITIONS: 1. Sufficient ullage in the tank ensured by LT. 2. Tank Valve will be opened when there is no Low Alarm 3. System will allow only one tank valve at a time. TO BOOSTERS 4. During changeover 25% valve opening gives 5. command for the closure of other tank valve. 6. Manifold valve operation is also similar. 7. Failure of above operation, sequence incomplete MANIFOLD condition will ensure shutdown of equipments. PIPELINE OPERATIONS THROUGH SCADA
  • 5. BOOSTERS LINE UP LOGIC BOOSTERS 1. Any one of the tank and manifold valve should be inn open condition. 2. Discharge valve of the booster should be closed. 3. No faults in the booster alarms should exist. 4. Maximum only 2 Nos. of boosters can start. 5. Start command opens cution valve, then to pump. Once pump runs discharge valve is opened. 6. Suction Pressure alarm comes online after a time delay. 7. Any alarm initiation trips the boosters. PIPELINE OPERATIONS THROUGH SCADA
  • 6. MAINLINE PUMP LINE UP LOGIC 1. Mainline Pumps are either Engine Driven or Motor Driven. 2. In case of Engine Driven Pump, a self contained control panel ensures the healthy status of all engine/pump parameters. 3. In case of Motor Driven Pump, the health of the equipment is monitored directly by the SCC. 4. Precondition to start : Discharge valve should be closed, No fault condition exist confirms the availability of the equipment. 5. Start command opens suction valve, then to pump. Once pump runs opens discharge valve. 6. Any failure in the sequence will not allow the pump to start. 7. While pump running, any alarm of the pump/station like high discharge, ESD, Sump Tank Level Hi-Hi etc. will trip the system and isolates the system by closing the valves. 8. All important alarms are derived from Primary instruments as well as secondary instruments to ensure fail safe operation. PIPELINE OPERATIONS THROUGH SCADA
  • 9. DISCHARGE MOV FAILED TO CLOSE WITH IN PRESET TIME? (120 SEC) PIPELINE OPERATIONS THROUGH SCADA
  • 15. AUTOMATIC CONTROL OPERATION PT PT MAINLINE PUMPING UNITS BP PI PS PT TANK TM PI PS PI PI PS PI PI PS PI PS PS PS PS PS BP PS PID LOOP SET POINT CONTROLLERS FP LOW GOVERNOR / SP SIGNAL VFD / CONTROL VALVE SELECTOR DP PIPELINE OPERATIONS THROUGH SCADA
  • 17. TYPICAL CONTROL LOOP OF RECEIVING STATION PT PS PI PI SD SRB SD PCV PT BP LOW S DPI T R. SIGNAL FC SELECT OR T T M LS, M LT PS PT DM PIPELINE OPERATIONS THROUGH SCADA
  • 19. LOCAL CONTROL SYSTEM / PROGRAMMABLE LOGIC CONTROL SYSTEM OBJECTIVES ARE -LOGIC CONTROL - PROCESS CONTROL COMMUNICATION WITH SCC Digital I/Os Analog I/Os CPU & Communication interface Field Instruments PIPELINE OPERATIONS THROUGH SCADA Independent Control System Irrespective of SCADA
  • 20. CONTROL SYSTEM During the scan, a PLC … Monitors Inputs Scan Executes Program Changes Outputs 20 PIPELINE OPERATIONS THROUGH SCADA
  • 21. TYPICAL SCADA ARRANGEMENT MCC COMMUNICATION SERVER COMMUNICATION LINK SCC, SCC, SCC, Originating BV BV Intermediate BV Delivery Station RTU RTU Station RTU Station PIPELINE OPERATIONS THROUGH SCADA
  • 22. APPLICATION SERVERS (32 DUAL REDUNDANT SCADA OPERATOR ENGG/PROGRAMMING BIT) MCS cum SCC SERVERS (32 WORKSTATIONS (32BIT) SIC terminal (32 BIT) TERMINAL 15” Flat 15” Flat Mon. BIT) 19” Fat Mon. 50”TFT 15” Flat Mon. Mon. 15” Flat Mon. Screen Display DUAL REDUNDANT 100 MBPS ETHERNET LAN In owner’s OFC based Interface between communication RTU / PLC Printers & Dual LAN system provision CPU, Memory, P C C I P C C I shall be made for comm. Module, I/O S P O O S P O O Ethernet Interface controller, power U U M C U U M C supply DOT MATRIX point to point PRINTER redundant communication Communication with each PLC of Server / FES SCCs Ethernet LASERJET PRINTER Multi drop I/O MODULES redundant communication with RTUs of MODBUS Interface block valves FIELD DEVICES to third party V.28/Ethernet devices e.g. flow computers, RTG, VFD etc. TYPICAL MCS cum SCC CONFIGURATION PIPELINE OPERATIONS THROUGH SCADA
  • 23. SCADA Major functions of SCADA system – • Data acquisition / Communication • Alarm & Event processing • Control processing/commands • Trend generation • Shift / Daily /Maintenance Reports • Management Information Reports 23 PIPELINE OPERATIONS THROUGH SCADA
  • 24. APPLICATION SOFTWARE • LEAK DETECTION & LOCATION MODULE Sensing Pipeline Leakage and Location • BATCH TRACKING/INTERFACE ANALYSIS Calculation of motion and position of batches • PIG TRACKING Tracks Movement of pig • LOOK AHEAD MODEL To predict future trends of pressures and flow with respect to pump changes • PIPELINE EFFICIENCY Recommends for cleaning of pipeline • PREDICTIVE MODEL Simulates the hydraulic dynamics of the pipeline (Offline) PIPELINE OPERATIONS THROUGH SCADA
  • 25. LEAK DETECTION SYSTEM Typical Leak detection system consists following software modules : WHEN LINE IN OPERATION  Pressure & Flow Profile Module / Pressure Wave Module -To detect leak and location  Volume balance method : To detect leak only UNDER SHUT IN CONDITION Pressure wave module : To detect leak and location Pressure Drop method : To detect leak only PIPELINE OPERATIONS THROUGH SCADA
  • 26. LDS Functional Overview Dynamic flow balance method  A simple LDS could be based upon detecting an imbalance between a measured inlet flow and a measured outlet flow (ie Net Volume Line Balance) Qin Qout PIPELINE OPERATIONS THROUGH SCADA
  • 27. LDS Functional Overview Ideal Pressure Control Upstream Pu Normal Pressure Profile Pressure Pressure Profile fully developed due to leak PDCALC Pipe Length UPD  With ideal pressure control upstream PDMEAS  UPD = PDCALC - PDMEAS UPD is Unexpected Pressure Downstream PDCALC is Calculated Pressure Downstream PDMEAS is Measured Pressure Downstream  UPD = 0 implies no leak PIPELINE OPERATIONS THROUGH SCADA
  • 28. LDS Functional Overview Ideal Pressure Control Upstream  The pressure profile is capable of indicating leaks, but  small leaks have minimal effect on pressure  the leak cannot be located  difficult to filter out normal pressure variations  Profiling the flow using flow control downstream increases the model accuracy PIPELINE OPERATIONS THROUGH SCADA
  • 29. LDS Functional Overview Pressure Profiling (Upstream Pressure Control) Pu Normal Pressure Profile Pressure Profile under Pressure development due to leak (dashed lines) Pressure Profile fully developed due to leak Pd Pipe Length PIPELINE OPERATIONS THROUGH SCADA
  • 30. LDS Functional Overview Ideal Flow Control Downstream Flow Profile fully developed due to leak QUMEAS UFU QUCALC Normal Flow Profile Flow Pipe Length  With ideal flow control downstream  UFU = QUMEAS - QUCALC UFU is Unexpected Flow Upstream QU CALC is Calculated Flow Upstream QU MEAS is Measured Flow Upstream  UFU = 0 implies no leak PIPELINE OPERATIONS THROUGH SCADA
  • 31. LDS Functional Overview Flow Profiling (Downstream Flow Control) Flow Profile fully QU developed due to leak QD Normal Flow Profile Flow Profile under development Flow due to leak (dashed lines) Pipe Length PIPELINE OPERATIONS THROUGH SCADA
  • 32. MODEL BASED LEAK DETECTION PIPELINE OPERATIONS THROUGH SCADA
  • 33. LDS Functional Overview Response Time Series response . threshold time t1 t2 event periods leak level 1 level 2 level 3 level 4 response levels occurs detection time PIPELINE OPERATIONS THROUGH SCADA
  • 34. PRESSURE DROP METHOD- leak notified PIPELINE OPERATIONS THROUGH SCADA
  • 35. Typical leak sensitivity data on dynamic flow % leak Location time 2% + 10 km 20-30 mins 5% + 5 km 15-20 mins 10% + 2 km 5 mins PIPELINE OPERATIONS THROUGH SCADA
  • 36. APPLICATION SOFTWARE • LEAK DETECTION & LOCATION MODULE Sensing Pipeline Leakage and Location • BATCH TRACKING/INTERFACE ANALYSIS Calculation of motion and position of batches • PIG TRACKING Tracks Movement of pig • LOOK AHEAD MODEL To predict future trends of pressures and flow with respect to pump changes • PIPELINE EFFICIENCY Recommends for cleaning of pipeline • PREDICTIVE MODEL Simulates the hydraulic dynamics of the pipeline (Offline) PIPELINE OPERATIONS THROUGH SCADA
  • 37. SYSTEM RELIABILITY 1. MAJOR EQUIPMENT LIKE PLC, SCADA SERVER ARE AVAILABLE IN HOT STANDBY MODE. ONLY STANDBY IS NOT AVAILABLE FOR RTUs. 2. FAILURE OF COMMUNICATION WILL INHIBIT THE CONTROL COMMANDS. ALTERNATE HIREDCOMMUNICATION TO SCCs WILL HELP IN OPERATING FROM MCC WITHOUT APPLICATION SOFTWARE . 3. STATION LEAKAGES CANNOT BE DETECTED. CCTV WITH MOTION SENSOR – GENERATE ALARM 4. PROPER MAINTENANCE OF STATION WITH TO REGARD LEAKS/EQUIPMENT CAN ENSURE RELIABLE FUNCTIONING OF SCADA SYSTEM
  • 39. SYSTEM CAPABILITIES AND BENEFIT OPERATIONAL INFORMATION AND CONTROL  Data is acquired from field sensors / instruments  Data is processed for monitoring and control of Engines/Motors, Valves etc.  Supports operator decisions; reports and isolates abnormal situations  Operator settable alarms for station from centralized master station for pressure and flow  Emergency shutdown of entire pipeline from MCC in a defined sequence starting from the terminal station so as to keep the line pressurized .  Acquires and displays repeater data such as pressure, temperature, MOV status, intrusion alarms.  The block valve under the respective station can be locally controlled by the station control centre in case master- station communication fails.
  • 40. SYSTEM CAPABILITIES AND BENEFIT OPERATIONAL INFORMATION AND CONTROL  Data is communicated over dedicated Communication channels to local and centrally located system at remote  When the communication between master and local station/ repeater fails, the system maintains the previous state of operationi.e. there shall not be operational shutdwn.  Communication failure indication shall be messaged to the operator.  While controlling the SCC from MCC by way of commands or change of set points, confirmation is sought from the address before execution of command/ change of set point takes place.  Bump less transfer from local station control to Master station and Vice versa.  Can remotely prove the flow meters and effect calibration factors.
  • 41. SYSTEM CAPABILITIES AND BENEFIT MAINTENANCE BENEFITS  Data is stored as history  Archives data and alarms for future analysis  Generates hourly and daily shift reports  Generates equipment running hour report  Acquires and displays parameters of CP system such as power availability, PSP etc.  Remote and auto start of DG set in RCPs  Event database will maintain all alarms, alarm acknowledgements, return to normal process, operator control actions.  On-line data base can be modified from Master.  Permits security level log-ins.

Hinweis der Redaktion

  1. This slide has an animated product wave-front passing from inlet to outlet - explain how real systems are continually line packing and unpacking and thus introduce the idea of normal operational variations in measured values etc
  2. Introduce the idea of unexpected values forming the basis of alarms Simple principle determines downstream UP response UPd = 0 does imply no leak but that doesn't mean that UPd > 0 implies a leak filtering will also come into the equation later
  3. Now there is a need for more information - introduce the ideal of using flow readings
  4. ANIMATED SLIDE showing pipe with associated pressure/distance graph 1st click - normal profile, gas in pipe 2nd click - leak develops, pressure upstream is constant under assumed pressure control, downstream pressure drops 3rd click - new profile due to leak
  5. Much the same as before... An unexpected flow response will indicate the leak size (if its not coming out the other end then it must be going somewhere - but remember about line-packing etc) Once again it still requires clever filtering
  6. ANIMATED SLIDE showing pipe with associated flow/distance graph 1st click - normal profile, gas in pipe 2nd click - leak develops, flow downstream is constant under assumed flow control, upstream flow must increase 3rd click - new profile due to leak
  7. Each filter will generate response levels depending on how the leak response compares to its threshold A leak situation is generated for any response level > 1 otherwise it is a no leak situation t1 and t2 must be > than the filter averaging period + 1 scan time (15s)