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TRANSCRIPT
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Data Analytics Process Improvements & Event Detection
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Proficy CSense Solution
Optimize Process
Pro
ce
ss
KP
I
Optimal Performance
Current Performance
3. Control & Optimize Advanced process control (e.g., MPC)
Real-time set-point optimization
2. Monitor, Diagnose & Predict Reduce variation by real-time monitoring and diagnostics
Control loop performance monitoring
Predict lab measurements (soft sensors) for control purposes
Advanced regulatory control
1. Troubleshoot Identify & understand causes of variation
What If Scenario analysis & Benefit estimation
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Analyze, Troubleshoot , & Data mine
Develop & Simulate
Proficy CSense Solution
Deploy, Execute & Report
Monitor KPIs & Control Loops
Predict KPIs (Soft Sensors)
Advanced Process Control
De
velo
pe
r E
dit
ion
Troubleshooter Edition
Run-time Edition
For develop & test
For production use
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Industry examples Industries Problem Key Process / Asset
Brewery
Variation in Beer quality; Reduce chill haze in beer Improve product consistency and reduce waste Optimize Fermentation & Filtration Reduce energy consumption
Mash Tun Fermentation Filtration
Need to increase MER (Mean Effective Rate) Reduce scrap and downtime Determine V-profile (critical machine)
Packaging lines
Food High variation in Powder Moisture (Quality) Reduce energy consumption
Spray Dryer
Unstable exhaust temperatures Spray Dryer
High variation in Density (Quality) Need to increase throughput (or reducing batch cycle time) Need to reduce energy consumption
Evaporator
Water / Waste Water
Ensure Water Quality & Compliance (Drinking Water & Waste Water Effluent) Reduce Operating Cost (e.g. via reduced Energy & Chemicals)
Aeration tanks Settling tanks
Paper & Pulp Paper machine optimization; Moisture control; Brightness Control Paper machine
Coffee Improving yield and gel quality Processing (wet, dry or semi-dry process), Milling, Roasting
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Industrial
Data Intelligence
Food examples: Spray Dryers
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Spray Dryer Diagram
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Spray Drying Process
The drying time for a single droplet may be estimated by the following equation:
t = [r2dLÆHV ] x [mi-mf] / [3h(ÆT)] x [1+mi] , where: t= time (hr); r = radius of droplet; dL = density of liquid (lb/ft
3); ÆHV = latent heat of vaporization (Btu/lb); mi = initial moisture content (lb H2O/lb dry food); mf = final moisture content (lb H2O/lb dry food); h = film coefficient for heat transfer (Btu/ft2/hr/°F); ÆT = temperature difference between initial and final stages (°F).
Separation of Dry Particles; Charm (1971) has given an equation which relates the dimensions of a cyclone to the smallest particle (Dp) which can be separated:
Dp2 = (3.6 Ai D0 µ )/( ¹ZDV0ds ), where : Dp = diameter of particle; Ai = inlet cross sectional area of cyclone; D0 = diameter of outlet of cyclone; µ = viscosity of the fluid; Z = depth of the separator; D = diameter of the separator; V0 = velocity of air/powder mixture entering the cyclone; and ds = density of the particle.
Feed
Drying Air
Compressed Air
Drying Air
Cooling Air
Fluid bed
Dried product Outlet
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Spray Drying Process Average Spray Drying Conditions for Milk
Temperature of air (ambient) 25.0 C Temperature of feed: 60.0 C Temperature of inlet air: 150.0 C Temperature of outlet air: 82.0 C Temperature of drop surface (const. zone) 45.0 C Relative humidity (ambient air) 55.0 % Relative humidity (inlet air, psychrom.) 0.3 % Relative humidity (outlet air, psychrom.) 12.0 % Moisture content of milk: 87.0 % Moisture content of concentrate: 45.0 % Moisture content of powder: 4-5.0 % Moisture zone (constant rate): 9030.0 % Moisture zone (falling rate): 30 5.0 % Droplet size (initial), av. diameter: 40.0 µ Particle size (final) , av. diameter: 20.0 µ Density of milk 1.33 g/ccm Density of milk powder (bulk): .33 g/ccm Velocity of air: 61.0 meters/sec Velocity of droplet(initial): 17,000.0 cm/sec Velocity of droplet (free fall): Å 1.0 cm/sec Drying time (constant rate zone): .0023 sec Drying time (falling rate zone): .0014 sec Drying time (total): .0037 sec Travel distance for drying: 13.5 cm
Feed
Drying Air
Compressed Air
Drying Air
Cooling Air
Fluid bed
Dried product Outlet
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What is the problem? Product quality (Powder Moisture) too low after spray drying, resulting in inefficient utilization of power and hence high operating costs.
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Preparation Multiple trends
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Modeling Model results:
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Knowledge Extraction Enables us to visually see the IO relationship, causes as well as leverages.
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Knowledge Extraction Active rules automatically generated for each scenario.
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Knowledge Extraction Cause analysis.
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Benefit Estimation
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CSense Real-time Causal Analysis
The model provides the basis to built a Cause+ model that can be deployed in real-time.
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Example of Analytics Model
Historical used in
simulation
Process model
simulates reaction
of process
APC Controller
responds to process
reaction
Results written to
SCADA via OPC
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CSense Real-time Causal Analysis The rules are activated each time the set condition is violated and a message is displayed on the corrective action the Operator needs to take.
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Finger print PCA model – optimal vs non optimal
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Finger print PCA model – variables contributing to non optimal operation
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Decision Tree – classifying desirable/undesirable moisture levels
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Industrial
Data Intelligence
Water examples
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• Ensure Water Quality & Compliance
(Drinking Water & Waste Water
Effluent)
• Reduce Operating Cost (of which
Energy & Chemicals are important
components)
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… save up to 30% in Aeration energy consumption
DO Optimization – Wastewater Reduced variations in Dissolved Oxygen during the
aeration process through Advanced Analytics…
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Settled Solids Control – Wastewater Settled solids measurements are generally available after a few of days …
… predicted settled solids values can be used immediately to optimize the control of the plant
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Optimize Chemical Usage Optimize chemical addition while ensuring effluent compliance
Reduced quality deviation in effluent
Optimal amount of chemicals added only when required, resulting in average reduction in usage
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Optimize Energy Efficiency Identify areas and causes of high energy usage
HIGH Total Energy Usage
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Asset Monitoring: Slurry Pump
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Pump Monitoring Problem Definition
Centrifugal pump
Typical measurements
Process
• Inlet pressure (Pi)
• Head (H)
• Fluid flow rate (F)
• Power/Current draw (P/I)
• Variable speed (S)
Mechanical
• Drive end bearing temperature (TDE)
• Non-drive end bearing temperature (TNDE)
• Vibration (V)
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Advanced Troubleshooting & Optimization Capabilities
Cause Analysis – focus on causes for process deviation
Predicted KPI Output & Target trend
Process rule that fires at the current timestamp
What If Scenario Analysis
Input-Output Relationship Analysis
Input trends
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Pump Monitoring Solution
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Current increasing (blue), pressure (cyan) and flow (orange) constant. Indicating impeller wear
Fingerprint model picking up deviation from normal
Impeller replacement
detected 5 days in advance
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Introducing…
Facilities Watch Monitoring HVAC related equipment to ensure Performance & Efficiency
Identify Facilities risk
Proficy Advanced Alarming Reasoner Plug-in
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Example - Facility Analytic Reasoners Real Time Operational Information
Supply airflow is greater
than 10% away from set-point for longer than 0.5 hours
Calculated heat wheel
efficiency is significantly below design parameters
Fan VFD speed not resetting when discharge static pressure is greater than set-point
Outdoor air damper greater than 5% open for
at least 15 minutes during morning warm up
Discharge temperature
less than mixed temperature with cooling valve closed
Advanced Analytics
100+ Intelligent Checks
SMART Air Handler
Smart Air Handlers Operational Efficiency
Using Advanced Analysis
Down
Optimized for Energy Savings & Performance
Running - not Optimized
“An air handler chilled-water valve with a
faulty control code issue — the valve was
always 20 percent open, wasting thousands of dollars in energy. This issue was not easily visible before, but the analytics software was able to detect it
immediately!”
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Proficy Advanced Analytics
PID Watch DOG (Dynamic Operations Guide for Control Loop Performance Monitoring)
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Detailed Report for a Flow Rate Control Loop
BEFORE
AFTER
Process+: Weighted Weekly Out of Limits
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Weeks
Pe
rce
nta
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Weekly
Linear (Weekly)
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The Story of Lanxess Chemicals
BEFORE: 60% of loops in manual & rest out of control 20% of the time, resulting in sub-optimal process stability and performance
AFTER 6 months: 90% of loops in automatic and in control 90% of the time (and continuously improving) , resulting in significantly and continuously improving process stability and performance
100% ROI in less than 6 months