TSE SCADA Design presentation new
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Transcript of TSE SCADA Design presentation new
Pre and Post Contract Professional Consultancy Services for
TSE SCADA Automation
PRESENTATION:
Charles Chandler his role in Hyder for this project is to:
• Review the technical content • Assist with delivering the project to you.
WHAT DOES THIS PRESENTATION COVER?
• Introduction
• Operations analysis
• Valves, flow meters & leak detection
• RTU and services
• Central SCADA
• Future expansion
• Summary
Introduction
• This presentation concentrates on the Preliminary Design Report
• I will speak about the Operations analysis
• Mohamed ElSirsy will follow on and speak about the valves, flowmeters & leak detection
• Nasir will follow on and speak about the RTU and services
• I will finish by speaking about the Central SCADA and summarize the benefits
• Questions please hold if possible for each speaker at the end of his talk
Operations analysis
TSE1 & TSE2. TSE3 comes on line in the future.Existing sources are sufficient currently, BUT supply can be interrupted by fault or process failure at source. Operations response will be more effective with a strategy of:• Early detection and indication of location.• Detection of service failure (low pressure) remote from the fault• Means of rationing supply.SCADA will help by:• Monitor flow and pressure to detect major leaks and detect areas where
pressure is low (below 30mWG). • Remote control of valves so that areas can be isolated and returned back
into service easily.
Operations analysis
RECOMMENDATIONS ARE:• 12 zones, each of which can be isolated by valves which will be motorised
with facility to operate from the SCADA HMI• Flow meters on key pipelines providing good indication of demand pattern
and for identifying exceptional conditions• Pressure transmitters associated with the flow meters to provide service
pressure indication• Pressure transmitters associated with key transmission lines, with
particular functionality of identifying major leaks.• Automate in-line valves• Slow operation of valves for surge suppression• Semi-automatic exercise of automated valvesAll the above work will be undertaken at 135 sites, each of which includes an existing valve chamber.
Operations analysis
Operations analysis
CATEGORY OF THE LOCATION OF IN-LINE VALVES
INDICATORS OF USEFULNESS
Washouts Major consumers
Congested area remote from the operations centre
See note *
Area where leak/fault could cause serious disruption or damage
See note *
Main transmission pipelines
Frequency of occurrence
Infrequent Infrequent Occasional Occasional Occasional
Risk of leak/fault causing serious disruption or damage
Low LowNo linkage with this category
High High
Reliability of information for remote control
Good Good Medium, relies upon local observation.
Medium, relies upon local observation.
Good, for key sections where leak detection is proposed
Time of response at the site by staff
Long, generally
No linkage with this category
Long, especially when traffic flow is high, areas such as Corniche
No linkage with this category
Medium, generally
CONCLUSIONS
Low priority, subject to comments below
Low priority, subject to comments below
Priority 3
Priority 1Priority 2if both categories apply, for example Corniche & Diplomatic areas
Valve Statistics & feasibility of retrofit
Methodology of Condition Survey:• Asses the condition of the valves, fittings, pipes and valve chamber.• Determine the services available at each valve chamber• Take digital coloured photos of the valve chamber to provide evidence of
the current condition of the valve chamber.• Recording of Northern and Eastern coordinates based on QNG data.• Develop a condition assessment grade of the valve chambers.• The Results of the Condition survey:
Total Number of Proposed valves to be Actuated 241Total Number of Actuators to be supplied (Retrofit) 144
Total Number of complete valves with Actuators to be supplied 96
Total Number of Recommended manual valves to be replaced 52
Valve Statistics & feasibility of retrofit (cont’d)
100mm 150mm 200 mm 300mm 350mm 400mm 500mm 600mm 700mm 800mm 900mm 1000mm0
10
20
30
40
50
60
0 0 0
49
2
49
8
23
6 5
1 1
Number of Actuators To be Supplied
Valve Statistics & feasibility of retrofit (cont’d)
100
150
200 m
m
300m
m
350m
m
400m
m
500m
m
600m
m
700m
m
800m
m
900m
m
1000
mm05
101520253035404550
0 0
22
43
3 511 11
1 0 0 0
Number of Complete Actuated Valve Set (Valve & Actuator) to be Supplied
Valve Statistics & feasibility of retrofit (cont’d)
100m
m
150m
m
200 m
m
300m
m
350m
m
400m
m
500m
m
600m
m
700m
m
800m
m
900m
m
1000
mm0
5
10
15
20
25
30
35
62
5
29
31 0
5
0 0 0 0
Number of RecommendedNew Manual Valves
Valve Statistics & feasibility of retrofit (cont’d)
• Feasibility of Retrofit:• Proceeding through finalizing detail design drawing of the valve
chamber, till now it was found that there is no need for mounting the actuators outside the valve chamber (this will be confirmed after finalizing and settling on number of the valves to be actuated).
• Examples of finalized valve chambers :
Valve Statistics & feasibility of retrofit (cont’d)
Valve Statistics & feasibility of retrofit (Cont’d)
Valve Statistics & feasibility of retrofit (cont’d)
Flow Meter Scheme
• Current Situation: During our investigation survey phase and referring to the
Engineering reports related to this project especially (C 685, C 682, C747 & C682), we have noticed the following:
• Regarding flow meters in the TSE network itself (i.e. excluding the pump stations TSE1 &TSE2), no proper reading were taken for TSE metering along the network.
• The operators presently take potable meter and measure pressure from chambers that have pressure gauges (tapping).
• The presently status of measuring devices is as follows:• Valve chamber No.68 (VC0068) – Pressure gauge connection • Valve Chamber No.77 (VC0077) - Pressure gauge connection
Flow Meter Scheme(cont’d)
• Valve chamber No.G01 & G02 (VC0G01 & VC0G02) - Pressure gauge connection
• Valve chamber No.106 (VC0106) - Pressure gauge connection• Port Roundabout – Meter installed (C685, Rationalization o TSE –
Engineering Report) • Criteria:• For monitoring consumption and system metering, it is desirable to
install permanent flow meters on the flows from:
sources Direct Feed Areas
Pumping Stations Flows to zones
Reservoirs
Flow Meter Scheme (cont’d)
In general, flow meter locations should facilitate day to day system monitoring.
We have suggested 22 flow meter mainly; on the main transmission lines where the flow will split feeding different areas and zones
The number and locations shall be finalized after discussion and agreement with the operation department, encountering all their concerning to achieve proper monitoring and ease of measurement.
Flow Meter Scheme (cont’d)
Flow Meter Scheme (cont’d)
• The following points should be considered:• It isn’t possible to predict the exact quantities of future demands within the
greater Doha TSE network, because the final demands are not known in advance by the project developers of the various irrigation and district cooling projects.
• There are some future projects, which are predicted to use TSE which may be cancelled, or conversely, where the scope of TSE usage may greatly increased. There will also be future projects which are not presently identified and have been not allowed for in the demand assessments under this project
• It isn’t possible to state precisely when future TSE demands will actually occur because the actual finish date of all projects utilising TSE cannot be accurately predicted.
• The zoning of the network will need to be modified over time as new demands in the network and the need to match the output of TSE from TSE 1, TSE 2, and TSE 3 necessitate a change in the source of TSE.
Flow Meter Scheme (cont’d)
Leak Detection Scheme
Proposed Leak Detection Methods Using SCADA• Mass or Volume Balance• Real Time Transient Modeling (RTTM)• Single Pressure Point Analysis
Mass Balance: The Mass balance method of leak detection, also known as line
balance, compensated volume balance, or volume balance, is based on measuring the discrepancy between the incoming (receipt) and outgoing (delivery) product volumes of a particular pipeline segment. During a unit time interval, the volume of product that enters a pipe may not be equal to the measured volume exiting the pipe. The difference is accounted for by uncertainties in line pack and flow measurement
Leak Detection Scheme (cont’d)
• Compared to other leak detection methods, Mass balance is particularly useful in identifying small leaks. However, leaks are generally detected more slowly and flow metering at each end of the line or pipeline segment will not identify the location of the leak.
Real Time Transient Method: The most sensitive, but also the most complex and costly leak
detection method in use is real time transient modeling (RTTM). RTTM involves the computer simulation of pipeline conditions using advanced fluid mechanics and hydraulic modeling. Conservation of momentum calculations, conservation of energy calculations, and numerous flow equations are typically used by the RTTM system.
Leak Detection Scheme (cont’d)
• First, the pressure-flow profile of the pipeline is calculated based on measurements at the pipeline or segment inlet.
• Next, the pressure-flow profile is calculated based on measurements at the outlet.
• Third, the two profiles are overlapped and the location of the leak is identified as the point where these two profiles intersect. If the measured characteristics deviate from the computer prediction, the RTTM system sends an alarm to the pipeline controller.
• The more instruments that are accurately transmitting data into the model, the higher the accuracy of and confidence in the model.
Leak Detection Scheme (cont’d)
• The distinct disadvantages of this method are the costs associated with implementing RTTM and the complexity of the system, which requires numerous instruments and extensive controller training and system maintenance.
• Single Pressure Point Analysis:• The most widely method used to detect the depressurization that
accompanies a leak. The most common implementations of this are detecting pressures that become abnormally low, and detecting rate of pressure change that become too low (pressure falling too rapidly). These systems implemented as software or hardware solutions, and may be remote from the transducers.
Leak Detection Scheme (cont’d)
The implementation of a single point pressure is a fairly straightforward matter; as the pressure measurements are obtained they are placed in a circular buffer where the most recent and all numbers of date point’s values are kept.
Each pressure measurement used in the procedure is treated individually, and as many measurements as desired or available may be analyzed. For each measurement the data is partitioned into new and old sets.
The advantage in doing so is to try to maximize both detection speed and sensitivity. By using shorter time periods for the new data partition, which corresponds to putting more data in the old partition, the leak affects the mean of the new data more rapidly. This leads to the reduction of false alarms.
The primary strength of this system is its simplicity. This translates into minimal instrumentation and computer resource requirements and therefore lower overall costs.
Leak Detection Scheme (cont’d)
Criteria Mass Balance Real Time Transit Modelling
Single Pressure Point Analysis
Water Table No Effect Sensitive No Effect
Condition of Pipe Line Leak Present at installation will not be detected
No effect Leak Present at installation will not be detected
Ease of Operation Easy Complex Straightforward
Time Monitoring Continuous Continuous Continuous
Spatial Resolution Low Excellent Good
Equipment used Two flow meters (on the inlet & outlet)
Flow meters, pressure transducers, sensors and cables
One pressure transducer for each section
Cost Expensive (flow meter on inlet and outlet)
Highly expensive Low Cost (compared with the other 2 methods)
RTU & services
TOPICS:• Electricity Supply• General RTU arrangement• Communication Servise• TSE 1 & TSE 2 RTU
Electricity Supply
Power Supply Sources1- KAHRAMAA Network
Main supply source for all valve chambers2- Solar System
Solar Power System will be considered for the location where KHARAMAA supply can not provided
3- Street Lighting Feeder pillars Street lighting feeder pillar was considered as the main power supply
source. According to the Road department street lighting feeder pillars will not be allowed to be utilized
Power Supply Sources Comparison
KAHRAMAA Solar Power Reliability Good Medium
Effects of climate No effects Some Effects
Maintenance Not Required Required
Installation cost Medium Medium
Ease of installation Easy Complex
Additional Future Load Could be without additional equipments
Additional equipments will be required
Power supply loads
• Typical Actuators power rating
Valve Size - mm
Valve Type Actuator Power Pn (KW)
300 Gate Valve 0.75
400 Gate Valve 1.5
500 Gate Valve 1.5
600 Gate Valve 3.0
700 Gate Valve 0.3
800 Butterfly Valve 0.75
900 Butterfly Valve 0.75
1000 Butterfly Valve 0.75
Electrical Load summary
• Typical Maximum Demand Load of a Valve Chamber• vvvv Item Maximum Demand
load - kWActuator 5 *Cabinet Lamp 0.1230V Power Socket 0.5Instrumentation power supply/battery unit
0.1
RTU 0.1Anti- Condensation heater 0.2
Total 6
* Short time demand load at closing end
RTU Main Features
• Support for DNP-3 and modbus as minimum. • Data acquisition from field equipment (digital and analogue
inputs). • Data recording and time stamping (time and date). • Sequence of events recording. • Alarm management (priorities) including report by exception. • Handling data received from control centers. • Initiating commands (digital and/or analogue outputs) and
software routines (pump • Self diagnostics • Communications control including route selection.
RTU Inputs/ Outputs (I/O)
• The Following is a typical signal that will be available at the RTU and will be transferred and displayed on SCADA
Digital Input DescriptionValve Fully Open Valve is in the fully open position
Valve Fully Closed Valve is in the fully closed position
Valve Actuator collective fault signal
Faulty signal from actuator control circuit ( torque fault, motor overheated. Loss of phase ..etc)
Actuator Selector Switch Remote/ Manual
Position of the actuator selector switches at valve chamber
Main Power Supply Available
Healthy main power supply is available
Flowmeter Faulty Faulty signal from flowmeter transmitter
RTU Inputs/ Outputs (cont’d)
High water level in the Chamber
Water is detected in the valve chamber
Battery charger Operating or not
Battery voltage Normal or low
Flowmeter instantaneous flow
Instantaneous reading of the flowmeter
Flowmeter totalized flow Totalized flow indicated in flowmeter transmitter
Pressure transmitter reading
Reading of the pressure transmitter
RTU Communication
• RTU will be communicated with the SCADA centre using • 1- Public Service Network (PSTN)• For Valves chamber outside roundabouts or road islands• 2- Global System Mobile (GSM)• For all valve chamber inside roundabouts
Valve Chamber Location
Number of Valve Chambers
RTU Communication
Road Side 42 PSTN, ISDN
Road Island 29 GSM
Roundabout 61 GSM
RTU Cubicle & site wiring - Option 1
RTU Cubicle & site wiring - Option 2
RTU local controls
ACTUATOR CONTROL:• Surge control 300 seconds• Surge control, and limit power supply, one only to move at any time• Manual control, is on actuator; OK or manual controls in RTU pillar?
Central SCADA
DIAGRAM option 1
Central SCADA
DIAGRAM option 1
Central SCADA
DIAGRAM option 2
Central SCADA
STRATEGIC SUPPLIER CHOICES
• SCADA standard software package/licences
• RTU manufacturer/programming licences & spares
Suggest that this is considered for prequalification of Contractors
Future expansion
TOPICS:New pumping station TSE 3, see Hyder Consulting report “C682 - Doha North Sewerage, Treatment and Associated Works, Volume 4, TSE3 and Rising Mains” of 24 September 2009. Uncertainties include several items where the proposed TSE SCADA project can provide benefits, such as:• The area of network zoning will change over time and might be seasonal. Central
control of the key valves will provide an efficient means of responding promptly to the circumstances.
• The profile of pressure/flow that has to be delivered by stations TSE1, TSE2 and TSE3 depends on monitoring the pressure in the most sensitive parts of the network. The RTU at these sites will provide relevant data and also transmit alarms should abnormal pressure or flow occur.
SCADA system should be capable of accommodating at least 500 sites within the current provision, and expandable thereafter.
Future expansion
Summary
• TSE operations can be made faster and more efficient as a result of the proposed centralized SCADA system. Valves may be operated remotely in response to the circumstances and a full record kept of all states and operator actions.
• The records will enable exceptional events to be analyzed and long term trends to be assessed.
• The historical database can be connected to other asset management and analytical systems that are being developed as an integrated business IT infrastructure for Ashghal and thereby contribute a valuable corporate data archive resource.
• The central SCADA installation will accommodate substantial increases in the number of sites that can be monitored in the future.