AMINE GAS TREATMENT CASE PROACTIVELY PREDICT COLLAPSE OF AN AMINE PROCESSING CONTACTOR
AMINE GAS CASE PREDICT COLLAPSE OF PROCESSING CONTACTOR Save $200M USD per year Foaming / Flooding events: 2 to 4 events per contactor per year Costing $250,000 per event 200 contactors worldwide Impact: Lost revenue High unplanned maintenance costs Poor amine utilization 2
AMINE GAS CASE SAS DAY AT TEXAS A&M: PREDICT COLLAPSE OF PROCESSING CONTACTOR Project Objectives Data Overview Agenda Analytical Approach Summary of Analytical Findings Lessons Learned Requirements for Big Data Predictive Analytics
AMINE GAS CASE AMINE GAS TREATMENT CASE OBJECTIVES Business Challenge Reduce collapse of Amine processing contactor due to foaming and flooding Business Impact Proactively predict foaming and flooding events Predict and monitor processing liquid levels Optimize Amine utilization Value Driver Improve up-time and processing efficiency
AMINE GAS CASE GOAL: PROACTIVELY PREDICT PROCESSING FAULTS Lean Amine to Contactor Foaming/Flooding Event Excess Amine Pickup Low Amine Gas Pickup
AMINE GAS CASE PROCESSING CONTACTOR SYSTEM OVERVIEW Contactor C101 CO 2 treated C-101 C-102 CO 2 feed gas Storage Tanks 41, 42 & 43
AMINE GAS CASE ANALYTICAL APPROACH SAMPLE EXPLORE MODIFY MODEL ASSESS Consolidate multiple data sources Quality Check Cleanse Visualize sensor and fault data Collaborate with subject matter experts Identify candidate anomalies Transform variables Filter outliers Cluster similar acting groups Variable selection Identify early fault indicators Root cause analysis Generate predictive models Decision trees Logistic regression Neural networks Review results with subject matter experts Score new data Automate ongoing assessment of prediction accuracy Flag model needing tuning Alert when operation becomes unstable
AMINE GAS CASE DATA OVERVIEW Source: PI System Systems: Contactor C-101: 22 sensor variables & 18 calculated variables Contactor C-201: 22 sensor variables & 18 calculated variables Contactor Feed Flow: 1 sensor variable Storage tanks: 3 sensor variables (1 per tank) Time range: January 1, 2010 to April 12, 2014
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ANALYTICAL APPROACH www.sas.com
AMINE GAS CASE ANALYTICAL WORKFLOW Identify Time periods to investigate Events to investigate Explore See potential trends/areas to investigate Leading cause of failures Identify potential explanatory variables Analyze Perform root cause analysis Statistical signatures for events Stability modeling and monitoring
AMINE GAS CASE EXPLORE SENSOR DATA AND FAILURE TIMES February 10, 2013 to April 12, 2014
AMINE GAS CASE ANALYTICAL METHODS EMPLOYED Pareto Analysis Correlation Analysis Variable Cluster Analysis Principal Component Analysis Association Analysis Root Cause Analysis Decision Trees Logistic Regression Stability Monitoring
AMINE GAS CASE CORRELATION ANALYSIS Purpose: Measures strength of a linear relationship between numerical variables Benefits: Improves accuracy and performance of predictive models
AMINE GAS CASE VARIABLE CLUSTER ANALYSIS AND PRINCIPAL COMPONENT ANALYSIS Cluster Analysis Principal Component Analysis Purpose: Identifies similar acting variables or groups Variable reduction technique Benefits: Identifies most meaningful sensor data and events to further analyze
AMINE GAS CASE MULTIPLE LINEAR REGRESSION Purpose: Predicts contactor processing liquid levels Explains variables or combination of variables affecting contactor processing liquid levels Benefits: Analyzes more information generating greater predictive power Generates better understanding of relationships between variables Dependent Var: Gas Treating Area Pickup Ratio Explanatory Var: Flash Drum Level Feed Filter Separator Level CO 2 in treated gas Tray 21 Level Dependent Var: Contactor Level Feed Gas Pressure DSG Stripper Explanatory Temp Var: DSG Stripper Temp D101 NGL Train Separator Feed Gas Temp Feed gas - Lean DGA temp Feed gas Lean DGA temp Contactor Level D201 NGL Train Separator Lean DGA % Strength Dependent D101 Var: NGL Feed Train Gas Separator Flow NGL Train Separator Level Lean DGA % Strength Explanatory Var: Lean DGA % Strength Feed Gas Temp Feed Filter Separator Level DGA Antifoam Tank Level Tray 21 Level Contactor Level Flash Drum Level Flash Drum Level Lower Tray #5 Temp NGL Train Separator Level
AMINE GAS CASE CONTACTOR FOAMING/FLOODING DECISION TREE Purpose: Illustrates all possible outcomes and highlights typical path Benefits: Visually identifies variables considered relevant to target event occurrence or non-occurrence
AMINE GAS CASE ROOT CAUSE ANALYSIS & ASSOCIATION ANALYSIS Period: Jan 1/2013 to Dec 31/2013 Foaming/Flooding Event Analytical rule Lift PDI205_v_gt95p & PDI022_v_gt95p ==> TARGET_EVENT 17.86 PDI205_v_gt95p & PDI006_v_gt95p ==> TARGET_EVENT 16.76 TI028_v_gt95p & PDI205_v_gt95p ==> TARGET_EVENT 15.94 TI028_v_gt95p & FIC004_v_gt95p ==> TARGET_EVENT 15.59 PDI022_v_gt95p & FIC004_v_gt95p ==> TARGET_EVENT 15.52 TI026_v_gt95p & FIC004_v_gt95p ==> TARGET_EVENT 15.45 TI026_v_gt95p & PDI022_v_gt95p ==> TARGET_EVENT 15.12 Purpose: Helps understand why processing fault occurred Identifies variables potentially contributing to fault/failure event Benefits: Identifies association rules to predict occurrence of future faults/failures
AMINE GAS CASE ALERT FOAMING/FLOODING ROOT CAUSE PATTERN RECOGNITION WARNING
AMINE GAS CASE CONTACTOR LEVEL STABILITY MONITORING MODELS ARIMA REGRESSION Purpose: Provides predictive capability to show current state and alert of potential problems Benefits: Automatically alerts when operation becomes unstable Provides better forecasting accuracy Detects and accounts for daily and seasonal operational differences Provides better explanatory power Traditional approach used by engineers
AMINE GAS CASE SCORE NEW DATA AGAINST PREDICTION MODELS
AMINE GAS CASE ALERT UNSTABLE OPERATION TO PREVENT FUTURE FOAMING/FLOODING EVENTS
AMINE GAS CASE SUMMARY OF ANALYTICAL FINDINGS Proactively predict foaming and flooding events Discovered foaming/flooding fault signatures Predict and monitor processing liquid levels Developed prediction models and stability monitoring forecast models Optimize Amine utilization Developed stability model to feed optimization model
AMINE GAS CASE LESSONS LEARNED Sensor and fault data can easily be analyzed Wide variety of analytical methods available Tremendous business value discovering root cause of faults and failure initiating variables
AMINE GAS CASE REQUIREMENTS FOR BIG DATA PREDICTIVE ANALYTICS Data: High-Performance Architecture: Scalable Performance Data Server Analysis:
AMINE GAS CASE PREDICT COLLAPSE OF PROCESSING CONTACTOR Save $200M USD per year Foaming / Flooding events: 2 to 4 events per contactor per year Costing $250,000 per event 200 contactors worldwide Impact: Lost revenue High unplanned maintenance costs Poor amine utilization 32