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Slide 1
WW HMI SCADA-01Increased Operational Effectivenesswith Situational Awareness
John KrajewskiDirector HMI/Supervisory Product Management
© 2013 Invensys. All Rights Reserved. The names, logos, and taglines identifying the products and services of Invensys are proprietary marks of Invensys or its subsidiaries.All third party trademarks and service marks are the proprietary marks of their respective owners.
@InvensysOpsMgmt / #SoftwareRevolution
/Wonderware
/Wonderware HMI
/Groups –HMI/SCADA/AppServer
social.invensys.com
New Release!
2014
Slide 3 3
SituationalAwareness
Many Names – Same Intent
High Performance HMIAbnormal Situation Management (ASM)Operator/User Centered DesignSituation(al) AwarenessAdvanced Process GraphicsHuman Factors DesignMore…
Slide 4
High Performance HMIAbnormal Situation Management (ASM)Operator/User Centered DesignSituation(al) AwarenessAdvanced Process GraphicsHuman Factors DesignMore…
HMI Evolution/Current State
1970’s 1980’s 1990’s Present
Slide 5
1970’s 1980’s 1990’s Present
HMI/Supervisory Market SpectrumPlant Site Enterprise
• Ease of Use• Process Visualization• Basic Alarming• Short Term History• Device Connectivity
Key
Nee
ds/A
spec
ts
• Larger Tag/GraphicCounts
• Graphic Standards• Extensible Vis
(Client Controls)• Basic Reporting• Basic Alarm
Management
• Server Consolidation• Standard Equipment
Model• Thin Client• Centralized Historian• Fault Tolerance• Situational
Awareness
• Multi-PlantHMI/CommonControl Room
• Advanced AlarmManagement
• Large EngineeringTeams
• Common Standards
• Monitoring• Operational Centers• PIMS (Information
Management)
Scale of Solution
ProcessMachine
Segm
ents
Slide 6
Key
Nee
ds/A
spec
ts
• Larger Tag/GraphicCounts
• Graphic Standards• Extensible Vis
(Client Controls)• Basic Reporting• Basic Alarm
Management
• Server Consolidation• Standard Equipment
Model• Thin Client• Centralized Historian• Fault Tolerance• Situational
Awareness
• Multi-PlantHMI/CommonControl Room
• Advanced AlarmManagement
• Large EngineeringTeams
• Common Standards
Cumulative
SA R
elev
ance
Medium Medium High Very High Very High
Impact of Human Error
Abnormal SituationA disturbance or series of disturbances in a process that cause plantoperations to deviate from their normal operating state.
Slide 7
The average percentages shown had the following:•People and work Context Factors: 35% - 58%•Equipment Factors: 30% - 45%•Process Factors: 3% - 35%
Source: ASM Consortium
Contributing Factors to Human Error
Trend Operator ImpactPlants are larger, more complex • Increased Monitoring Load
• Lack of UnderstandingIncreased Levels ofInstrumentation
• More Data to Manage• Lost in the Details• Inability to Act Quickly
HMIs are not new so why is this an issue now?
Slide 8
• More Data to Manage• Lost in the Details• Inability to Act Quickly
Increased Levels of Automation • Operators Become Disengaged• Role Is Reduced To Dealing With Upsets
Centralized Operations • Loss of direct awarenessStaffing Issues • Operators Lack Experience
© Invensys 10/23/2013 Invensys proprietary & confidential
Situational Awareness
The perception of environmental elementswith respect to time and/or space, thecomprehension of their meaning, and theprojection of their status.
Slide 9
Creating the Business Case
Slide 10
Safe and Reliable ControlPoorly performing alarm systems AND HMIs
are contributing factors to major accidentsand poor operating performance.
Proper Alarm System Management and AlarmSystem Performance is essential tomaximum-efficiency operations.
There are multiple contributing factors:
Slide 11
Poorly performing alarm systems AND HMIsare contributing factors to major accidentsand poor operating performance.
Proper Alarm System Management and AlarmSystem Performance is essential tomaximum-efficiency operations.
There are multiple contributing factors:
AlarmManagement
HumanMachineInterface
ControlLoop
Performance
Measurable Costs/Value
Raw Materials Process Products/Services
EnergyEnergy
$
$
$
Slide 12
Raw MaterialsRaw Materials ProcessProcess Products/ServicesProducts/Services
Waste
Waste
$
$
$
Business Value = Products(Availability) – Energy – Raw - Waste
New Paradigm in HMI Design
Slide 13
• Goal Oriented Design
• Hierarchical Information Organization
• Proper Color Usage
• Actionable Alarm Awareness
• Effective Design Elements
Aspects of Good HMI Design Philosophy
Slide 14
• Goal Oriented Design
• Hierarchical Information Organization
• Proper Color Usage
• Actionable Alarm Awareness
• Effective Design Elements
Common Mistake – The System is the Goal.
Goal Oriented Design
Goal DirectedTask Analysis
Slide 15
Goal DirectedTask Analysis
Common Mistake: Organize by P&ID
Information Organization
Sheet 1 Sheet 2 Sheet 3 … Sheet N
Slide 16
Sheet 1 Sheet 2 Sheet 3 … Sheet N
Level 1 – Area-wide overviews– KPIs, summary status information
Level 2 – Facility-wide overviews– key operating screens, specialty pages
Level 3 – Detailed operating information– similar to most current screens
Level 4 – Auxiliary information– help screens, trend pages, etc. Description of the tag
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Alarm 2 Descriptor
Alarm 3 Descriptor
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F3073.HCO
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EFFICIENCYEF.F4483
PCT
DUTYQ.F44NET40.4
MBTU/HR
83% FBX 025.4PCT
STOPPEDSP= 5.4
B
OVHDF
NAPF
BTMSF
IRF
TYPE 2
TYPE 3
TYPE 4
630
720
CSO
LGO
HGO
TRAY 29
XHGO
TRAY 4
60 40 20 0
60 40 20 0
60 40 20 0
605
700
635
720
60 40 20 0
60 40 20 0
Offspec
Diesel
IBP
60 40 20 0
FGF
NGF
650#F
175#F
CIF
DWF
83%
5.1:1
MATERIAL BALANCE
IN VENT
H2 QUALITYRY
VENTMU
Nap Prod
88%
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DU-5
FG
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Solutions Outside The Box, Inc.
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INFO
Cascadedto:
P221 T53 L3
ALARM
Alarm 1 Descriptor
Alarm 2 Descriptor
Alarm 3 Descriptor
CLEAR INH ENB PO INTDETAIL
TREND
60 50 40 30 20 10 0
S PP VOP
T RK
500
20060 MINUTES
RANGE
LO 200DEFAULT
1000200
500HI
Feed
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FRACTIONATOR OVERVIEW
83%
E-XXXX
T-XXXT-XXX
F3065
OVHDF
NAPF
BT MSF
IRF
Hydrogen
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Fractionator2 3 1
Overview
Start-up
Special
LP Sep
Recycle
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Shut Down Schematic Schematic Schematic AlarmSummary
E-XXXX
T -XXXT-XXX
E-XXXX
T-XXXT-XXX
CV 255
G5
OVHDF
NAPF
BT MSF
IRF
60 50 40 30 20 10
G3
TV 68 A
HV-125
Y9B
Y9A
PV 124
PV 125
Y9C
PV 126
F-570
F-120
PV 123
F-75
NAPHTHA
60 50 40 30 20 1090%
F-66HV 23
G2
F-67
F-68
CV 255
TV 68 B
45%
M
LP Sep
R. Absorber
S.O .C.
Back End
Recycle
EX PHTR
Histo ryH isto ry
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INFO
Cascadedto:
P221 T53 L3
ALARM
Alarm 1 Descripto r
Alarm 2 Descripto r
Alarm 3 Descripto r
CLEAR INH ENB POINTDETAIL
TREND
60 50 40 30 20 10 0
SPPVOP
TRK
500
20060 M IN UTES
RANGE
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Feed
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Schematic Schematic Level 4 Schematic Schematic
Level 4 Alarm Summary
ACK TIME IN TIME LST MODE TAGNAME STATUS VALUE CURLN 11:33:20 16:15:33 SCADA01 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA02 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA03 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA04 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA05 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA06 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA07 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA08 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA09 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA10 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA11 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA12 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA13 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA14 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA15 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA16 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA17 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA18 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA19 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA20 ALAREA-P LO 5.00 LO
File View Alarm General Help
Filter: ON Sort: TIME Columns Delete: ALL
Description of the tag
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INFO
Cascadedto:
P221 T53 L3
ALARM
Alarm 1 Descriptor
Alarm 2 Descriptor
Alarm 3 Descriptor
CLEAR INH ENB POINTDETAIL
TREND
60 50 40 30 20 10 0
SPPVO PTRK
500
20060 M IN UT ES
RANGE
LO 200DEFA ULT
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TREND
60 50 40 30 20 10 0
SPPVO P
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500
200
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LO 200
DEFA ULT1000
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500H I
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60 50 40 30 20 10 0
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Type 4 Schematic
Level 1
Level 2
Display structure
Slide 17
Level 1 – Area-wide overviews– KPIs, summary status information
Level 2 – Facility-wide overviews– key operating screens, specialty pages
Level 3 – Detailed operating information– similar to most current screens
Level 4 – Auxiliary information– help screens, trend pages, etc. Description of the tag
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INFO
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P221 T53 L3
ALARM
Alarm 1 Descriptor
Alarm 2 Descriptor
Alarm 3 Descriptor
CLEAR INH ENB POINTDETAIL
TREND
60 50 40 30 20 10 0
SPPVOPTRK
500
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RANGE
LO 200DEFA ULT
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STOPPEDSP= 5.4
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NAPF
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TYPE 2
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TYPE 4
630
720
CSO
LGO
HGO
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XHGO
TRAY 4
60 40 20 0
60 40 20 0
60 40 20 0
605
700
635
720
60 40 20 0
60 40 20 0
Offspec
Diesel
IBP
60 40 20 0
FGF
NGF
650#F
175#F
CIF
DWF
83%
5.1:1
MATERIAL BALANCE
IN VENT
H2 QUALITYRY
VENTMU
Nap Prod
88%
1st STG
DU-5
FG
MU
Solutions Outside The Box, Inc.
Frac
Frac
R.A.
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RRRRRRR
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LOGDate: Jan 1/2003, 11pmValve stem continues to st ick...calledmaint.tracking number: 454632--------------Date: Dec 23/2002, 10amValve stuck today...watch over next fewdays
INFO
Cascadedto:
P221 T53 L3
ALARM
Alarm 1 Descriptor
Alarm 2 Descriptor
Alarm 3 Descriptor
CLEAR INH ENB PO INTDETAIL
TREND
60 50 40 30 20 10 0
S PP VOP
T RK
500
20060 MINUTES
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FRACTIONATOR OVERVIEW
83%
E-XXXX
T-XXXT-XXX
F3065
OVHDF
NAPF
BT MSF
IRF
Hydrogen
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Fractionator2 3 1
Overview
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E-XXXX
T -XXXT-XXX
E-XXXX
T-XXXT-XXX
CV 255
G5
OVHDF
NAPF
BT MSF
IRF
60 50 40 30 20 10
G3
TV 68 A
HV-125
Y9B
Y9A
PV 124
PV 125
Y9C
PV 126
F-570
F-120
PV 123
F-75
NAPHTHA
60 50 40 30 20 1090%
F-66HV 23
G2
F-67
F-68
CV 255
TV 68 B
45%
M
LP Sep
R. Absorber
S.O .C.
Back End
Recycle
EX PHTR
Histo ryH isto ry
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LOGDate: Jan 1/2003, 11pmValve stem continues to stick...calledmaint.tracking number: 454632--------------Date: Dec 23/2002, 10amValve stuck today...watch over next fewdays
INFO
Cascadedto:
P221 T53 L3
ALARM
Alarm 1 Descripto r
Alarm 2 Descripto r
Alarm 3 Descripto r
CLEAR INH ENB POINTDETAIL
TREND
60 50 40 30 20 10 0
SPPVOP
TRK
500
20060 M IN UTES
RANGE
LO 200DEFA ULT
1000200
500H I
Feed
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Level 4 Alarm Summary
ACK TIME IN TIME LST MODE TAGNAME STATUS VALUE CURLN 11:33:20 16:15:33 SCADA01 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA02 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA03 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA04 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA05 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA06 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA07 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA08 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA09 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA10 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA11 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA12 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA13 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA14 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA15 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA16 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA17 ALAREA-P LO 5.00 LO
11:33:20 16:15:33 SCADA18 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA19 ALAREA-P LO 5.00 LO11:33:20 16:15:33 SCADA20 ALAREA-P LO 5.00 LO
File View Alarm General Help
Filter: ON Sort: TIME Columns Delete: ALL
Description of the tag
12345678PV
SP
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UNITS
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12345678 UNITS
TAGNAME Description of the Tag
OP
COMP
MAN
AUTO
CAS
CascadeComputer
Set toDefault
RRRRRRR
TRK
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LOGDate : Jan 1/2003, 11pmValve stem continues to stick...calledmaint.tracking number: 454632--------------Date : Dec 23/2002, 10amValve stuck today...watch over next fewdays
INFO
Cascadedto:
P221 T53 L3
ALARM
Alarm 1 Descriptor
Alarm 2 Descriptor
Alarm 3 Descriptor
CLEAR INH ENB POINTDETAIL
TREND
60 50 40 30 20 10 0
SPPVO PTRK
500
20060 M IN UT ES
RANGE
LO 200DEFA ULT
1000200
500HI
Feed
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TREND
60 50 40 30 20 10 0
SPPVO P
TRK
500
200
60 MIN UT ES
RANGE
LO 200
DEFA ULT1000
200
500H I
TREND
60 50 40 30 20 10 0
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TRK
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LO 200
DEFA ULT1000
200
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200
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60 50 40 30 20 10 0
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500
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LO 200
DEFA ULT1000200
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LO 200
DEFA ULT1000200
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60 50 40 30 20 10 0
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500
200
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LO 200
DEFA ULT1000200
500H I
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60 50 40 30 20 10 0
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500
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LO 200
DEFA ULT1000200
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TREND
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LO 200
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Type 4 Schematic
Level 3
Level 4
Reduced Navigation
Start-up/Shut Down Info
NO MASTER FUEL TRIPPURGE COMPLETEFUEL GAS ONABC RESETABC MODE MANUALIGNITOR HEADER PERMISSIVES SATISFIEDGAS HEADER PERMISSIVES SATISFIED
Navigation Zone
STM F BFW F
DL
BP
FD (P)
% O2
STMT
Air F
IGNB2
IGMN
BURNER STARTREGISTER OPENMODE AUTOIGNITOR ONIMPELLER OUTOIL BURNER ONSAB ON
N W COO2
BTU/C
900#
TN-BN
TS-BS
TS-BN TN-BS
BFW
Boiler Metal Temperatures
FG
202 Boiler Start-up
% MCR100
0
BM %100
0
LB %50
0
202
-50
Pre
ssur
e(P
SIG
)
Time (min)10 20 30 SAT Steam
0
100
200
300
400
500
600
700
800
900
1000
Sat Steam ROC(oC/hr)
Last hr: 0.00Current: 0.00
SH Steam ROC(oC/hr)
Target: 0.00Current: 2.00
To 100oC DrumBottom Temp (oC)
Target: 0.00Current: 2.00Last hr: 0.01
Drum Press ROC(psig/min)
Last hr: 0.20Current: 0.00
Task Orientated Level Two Displays- To startup operator had to visit 12 screens.- Operational level 1 screen to start up a Boiler
Start-up/Shut Down Info
NO MASTER FUEL TRIPPURGE COMPLETEFUEL GAS ONABC RESETABC MODE MANUALIGNITOR HEADER PERMISSIVES SATISFIEDGAS HEADER PERMISSIVES SATISFIED
Navigation Zone
STM F BFW F
DL
BP
FD (P)
% O2
STMT
Air F
IGNB2
IGMN
BURNER STARTREGISTER OPENMODE AUTOIGNITOR ONIMPELLER OUTOIL BURNER ONSAB ON
N W COO2
BTU/C
900#
TN-BN
TS-BS
TS-BN TN-BS
BFW
Boiler Metal Temperatures
FG
202 Boiler Start-up
% MCR100
0
BM %100
0
LB %50
0
202
-50
Pre
ssur
e(P
SIG
)
Time (min)10 20 30 SAT Steam
0
100
200
300
400
500
600
700
800
900
1000
Sat Steam ROC(oC/hr)
Last hr: 0.00Current: 0.00
SH Steam ROC(oC/hr)
Target: 0.00Current: 2.00
To 100oC DrumBottom Temp (oC)
Target: 0.00Current: 2.00Last hr: 0.01
Drum Press ROC(psig/min)
Last hr: 0.20Current: 0.00
Slide 18
Start-up/Shut Down Info
NO MASTER FUEL TRIPPURGE COMPLETEFUEL GAS ONABC RESETABC MODE MANUALIGNITOR HEADER PERMISSIVES SATISFIEDGAS HEADER PERMISSIVES SATISFIED
Navigation Zone
STM F BFW F
DL
BP
FD (P)
% O2
STMT
Air F
IGNB2
IGMN
BURNER STARTREGISTER OPENMODE AUTOIGNITOR ONIMPELLER OUTOIL BURNER ONSAB ON
N W COO2
BTU/C
900#
TN-BN
TS-BS
TS-BN TN-BS
BFW
Boiler Metal Temperatures
FG
202 Boiler Start-up
% MCR100
0
BM %100
0
LB %50
0
202
-50
Pre
ssur
e(P
SIG
)
Time (min)10 20 30 SAT Steam
0
100
200
300
400
500
600
700
800
900
1000
Sat Steam ROC(oC/hr)
Last hr: 0.00Current: 0.00
SH Steam ROC(oC/hr)
Target: 0.00Current: 2.00
To 100oC DrumBottom Temp (oC)
Target: 0.00Current: 2.00Last hr: 0.01
Drum Press ROC(psig/min)
Last hr: 0.20Current: 0.00
Start-up/Shut Down Info
NO MASTER FUEL TRIPPURGE COMPLETEFUEL GAS ONABC RESETABC MODE MANUALIGNITOR HEADER PERMISSIVES SATISFIEDGAS HEADER PERMISSIVES SATISFIED
Navigation Zone
STM F BFW F
DL
BP
FD (P)
% O2
STMT
Air F
IGNB2
IGMN
BURNER STARTREGISTER OPENMODE AUTOIGNITOR ONIMPELLER OUTOIL BURNER ONSAB ON
N W COO2
BTU/C
900#
TN-BN
TS-BS
TS-BN TN-BS
BFW
Boiler Metal Temperatures
FG
202 Boiler Start-up
% MCR100
0
BM %100
0
LB %50
0
202
-50
Pre
ssur
e(P
SIG
)
Time (min)10 20 30 SAT Steam
0
100
200
300
400
500
600
700
800
900
1000
Sat Steam ROC(oC/hr)
Last hr: 0.00Current: 0.00
SH Steam ROC(oC/hr)
Target: 0.00Current: 2.00
To 100oC DrumBottom Temp (oC)
Target: 0.00Current: 2.00Last hr: 0.01
Drum Press ROC(psig/min)
Last hr: 0.20Current: 0.00
Common Mistakes:
Proper Color Usage
Slide 19
Color and Attention
Color is a powerful way to guide attention– Your eye is automatically drawn to colored objects
• This is called the “pop out” effect
– Now try this one…
Color is a powerful way to guide attention– Your eye is automatically drawn to colored objects
• This is called the “pop out” effect
– Find the the “L”s and “I”sin this picture…
Slide 20
Source: NASA Ames Research Center Color Usage Labhttp://colorusage.arc.nasa.gov/popout.php
Color is a powerful way to guide attention– Your eye is automatically drawn to colored objects
• This is called the “pop out” effect
– Now try this one…
Color is a powerful way to guide attention– Your eye is automatically drawn to colored objects
• This is called the “pop out” effect
– Find the the “L”s and “I”sin this picture…
Color and Attention
APGs take advantage of the “pop out” effect to guide operators’attention to values that are in alarm
Click andwatch for thealarm…
Slide 21
Click andwatch for thealarm…
Color and Attention
BUT – if you use too much color, the “pop out” effect doesn’t workanymore
Click and then try to
find the “I”s in the picture…
Slide 22
BUT – if you use too much color, the “pop out” effect doesn’t workanymore
Click and then try to
find the “I”s in the picture…
Different tastes…Reactor 1
ThioniteMid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
IN OUTBalance
Menus
MainMenu
FeedSys
AuxSys
Reactor1
L2
TrendControl
Comp A Comp B
72.0
80.0
2 HR
Cool CPC CRM
Rate
Reactor 2
CRM-114Mid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
Balance
Comp A Comp B
60.0
68.0
2 HR
Cool CPC CRM
Rate
IN OUT
Hydrog A
BedA1
BedA2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp A
470
500
FLOW
2 HR
Hydrog B
BedB1
BedB2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp B
470
500
FLOW
2 HR
Alarms:ACKUNACK
ToggleList /Summary
P100
P210
P321
P441
Reactor2
HydrogA
HydrogB
L3 L4
70
80
%
12 HR
Key Performance Indicators
Conversion Efficiency
0.5
1.0
12 HR
Emissions Limit Ratio
Feed A Feed B Feed C SynG
Feed System Aux Systems
Atv 1 Atv 2 Pres %IP
Clr T-In T-Out Visc
CWT CWP S10
PWR VentP VentT
C57D Null-A Jup2
S200
MGA
Grok2
2
071608 08:55:07 RX2 LOW CRM –QUALITY EXC
LVL
LVL
Reactor 1
ThioniteMid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
IN OUTBalance
Menus
MainMenu
FeedSys
AuxSys
Reactor1
L2
TrendControl
Comp A Comp B
72.0
80.0
2 HR
Cool CPC CRM
Rate
Reactor 2
CRM-114Mid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
Balance
Comp A Comp B
60.0
68.0
2 HR
Cool CPC CRM
Rate
IN OUT
Hydrog A
BedA1
BedA2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp A
470
500
FLOW
2 HR
Hydrog B
BedB1
BedB2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp B
470
500
FLOW
2 HR
Alarms:ACKUNACK
ToggleList /Summary
P100
P210
P321
P441
Reactor2
HydrogA
HydrogB
L3 L4
70
80
%
12 HR
Key Performance Indicators
Conversion Efficiency
0.5
1.0
12 HR
Emissions Limit Ratio
Feed A Feed B Feed C SynG
Feed System Aux Systems
Atv 1 Atv 2 Pres %IP
Clr T-In T-Out Visc
CWT CWP S10
PWR VentP VentT
C57D Null-A Jup2
S200
MGA
Grok2
2
071608 08:55:07 RX2 LOW CRM –QUALITY EXC
LVL
LVL
Slide 23
Reactor 1
ThioniteMid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
IN OUTBalance
Menus
MainMenu
FeedSys
AuxSys
Reactor1
L2
TrendControl
Comp A Comp B
72.0
80.0
2 HR
Cool CPC CRM
Rate
Reactor 2
CRM-114Mid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
Balance
Comp A Comp B
60.0
68.0
2 HR
Cool CPC CRM
Rate
IN OUT
Hydrog A
BedA1
BedA2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp A
470
500
FLOW
2 HR
Hydrog B
BedB1
BedB2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp B
470
500
FLOW
2 HR
Alarms:ACKUNACK
ToggleList /Summary
P100
P210
P321
P441
Reactor2
HydrogA
HydrogB
L3 L4
70
80
%
12 HR
Key Performance Indicators
Conversion Efficiency
0.5
1.0
12 HR
Emissions Limit Ratio
Feed A Feed B Feed C SynG
Feed System Aux Systems
Atv 1 Atv 2 Pres %IP
Clr T-In T-Out Visc
CWT CWP S10
PWR VentP VentT
C57D Null-A Jup2
S200
MGA
Grok2
2
071608 08:55:07 RX2 LOW CRM –QUALITY EXC
LVL
LVL
Reactor 1
ThioniteMid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
IN OUTBalance
Menus
MainMenu
FeedSys
AuxSys
Reactor1
L2
TrendControl
Comp A Comp B
72.0
80.0
2 HR
Cool CPC CRM
Rate
Reactor 2
CRM-114Mid-RunONCLEAR
Prod:State:Agit:Locks:
Run Plan:Actual:
Balance
Comp A Comp B
60.0
68.0
2 HR
Cool CPC CRM
Rate
IN OUT
Hydrog A
BedA1
BedA2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp A
470
500
FLOW
2 HR
Hydrog B
BedB1
BedB2
Suct Dsch
OKOKOKCLEAR
VIB:BRG:OIL:Locks:
CycleComp B
470
500
FLOW
2 HR
Alarms:ACKUNACK
ToggleList /Summary
P100
P210
P321
P441
Reactor2
HydrogA
HydrogB
L3 L4
70
80
%
12 HR
Key Performance Indicators
Conversion Efficiency
0.5
1.0
12 HR
Emissions Limit Ratio
Feed A Feed B Feed C SynG
Feed System Aux Systems
Atv 1 Atv 2 Pres %IP
Clr T-In T-Out Visc
CWT CWP S10
PWR VentP VentT
C57D Null-A Jup2
S200
MGA
Grok2
2
071608 08:55:07 RX2 LOW CRM –QUALITY EXC
LVL
LVL
Is there only one palette choice that isright?
Slide 24
Common Mistakes:
Actionable Alarm Awareness
Slide 25
Best Practices: Alarm signaling in theHMI displays
Severity 1 response time < 5min
2
3
Severity 2 response time < 30min
Severity 3 response time < 60min
1
Slide 26
4 Severity 4 response time < 120min
Navigation Badges
Reactor 31Reactor 311 2 1 3
Reactor 32Reactor 323
Reactor 33Reactor 332
OverviewOverview1 4 1 6
Slide 27
Reactor 31 Reactor 32 Reactor 33
Common Mistakes
Effective Design Elements
Slide 28
Wonderware Situational AwarenessLibrary
Wonderware will provide with InTouch and Wonderware System Platform:
• New types of animations (points, style, sweep angle, trends)
• And a SAL library of ArchestrA Graphics (2014) and objects (2015) to support the dvt ofHighly Efficient Graphics at lowest cost
• This new version will also provide a Symbol wizard and themes management
WW HMI SCADA-04 Discover the new SituationalAwareness Library in InTouch 2014
Slide 29
Objects
PUMP
G5
Slide 30
PUMP
G5
Running Standby
Level 3 Display
Slide 31
Task With TraditionalHMI
With HighPerformanceHMI
Result
DetectingAbnormalSituations beforealarms occur
10% of the time 48% of the time A 5X increase
Benefits…
Slide 32
DetectingAbnormalSituations beforealarms occurSuccess rate inhandling abnormalSituation
70% 96% 37% over basecase
Time to completeabnormal situationtasks
18.1 min 10.6 min 41% reduction
Reference Material
Slide 33
High Performance HMI HandbookASM Consortium Guidelines to Effective Operator Display DesignDesigning for Situational AwarenessInformation Dashboard DesignShow Me the Numbers
Take aways
• Invensys will provide a library of pre-defined objects (OOB)with next release to simplify the implementations of highperformance HMIs
• Invensys will provide tools to simplify the engineering ofgraphics (themes, symbol wizard)
• Invensys will provide a new infrastructure for the alarmmanagement based on Historian with embedded graphicalrepresentation
• Invensys and its Ecosystem will provide services to guide ourcustomers in the implementation of high performance HMIs
• We are just getting started and there is much more to come…
Slide 34
• Invensys will provide a library of pre-defined objects (OOB)with next release to simplify the implementations of highperformance HMIs
• Invensys will provide tools to simplify the engineering ofgraphics (themes, symbol wizard)
• Invensys will provide a new infrastructure for the alarmmanagement based on Historian with embedded graphicalrepresentation
• Invensys and its Ecosystem will provide services to guide ourcustomers in the implementation of high performance HMIs
• We are just getting started and there is much more to come…
34
Slide 35