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Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station) Rob James (Product Manager, NeuCo) Eric Pahl (Production Manager, Dynegy-Independence Station)

Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

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Page 1: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Combined Cycle Plant

Duct Burner Optimization

Using ProcessLink

David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Rob James (Product Manager, NeuCo)

Eric Pahl (Production Manager, Dynegy-Independence Station)

Page 2: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Rationale

NeuCo has been optimizing processes in coal

plants for a long time

Conversations with friends and customers at

Combined Cycle (CC) plants suggested that it

could be useful in those as well

2NeuCo Proprietary

Page 3: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

The Project

Page 4: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Independence Station

Oswego, NY

1000 MW Total Capacity

2 x 2on1 CC

GE Units with STAG 207FA (165 MW) GTs

Vogt HRSGs and BOP controls

Duct Burners add 88 MW of capacity

Sell into the NYISO market

Started bidding into Regulation Market 4 years ago

4NeuCo Proprietary

Page 5: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Indentified Optimization Opportunities

Maximize plant capability for high Ramp-Rate (RR) Ancillary

Services

• Started development Jan 2013, deployed in closed-loop in Sept 2013.

results evaluated.

Optimize Dynamics of the Combined Cycle

Enhance Day Ahead Capability Prediction and Provide

Production Analytics

Detect Analyze and Diagnose Anomalies and Changes

GT Combustion Monitoring/Tuning

Power Augmentation Management

5NeuCo Proprietary

Page 6: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

The Tools

Page 7: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

The ProcessLink Platform

7

Plant I&C Systems Interfaces and Network (OPC, etc)

ProcessLink® Engine

Monitoring servicesOptimization services Modeling services

Model Predictive Control (MPC) Neural Networks

1st Principles Models AI Expert SystemsModel Predictive Control (MPC)

End-User InterfaceProcessLink Studio™

Product

Installation

and

Configuration

Tools

Application

Prototyping

Tools

Application

Deployment

and

Maintenance

Tools

Optimizer

Demystification

Views

Benchmarking

and Analysis

Views

Alert

Diagnosis

and

Management

7NeuCo Proprietary

Page 8: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

The ProcessLink Platform

8NeuCo Proprietary

Page 9: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Maximize Capability for High

Ramp-Rate Ancillary

Services

Page 10: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

The Challenge

For Independence, bidding into the Ancillary Services

Regulation Market is believed to have had a substantial

positive revenue impact

They bid 100 MW of ramp at 5MW/min (or 100MW over

20min) up to 1088 (all 1000 GTMW and 88 Duct Burner

MW) into the Day Ahead Ancillary Service Regulation

Capacity Market

They can add the Duct Burners to free up some GT

capacity in case they are asked to ramp at 5MW/minute

all the way to 1088 (or plant max)

But there is Heat Rate Penalty

10NeuCo Proprietary

Page 11: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Optimal Use of Duct Burners

for Regulation Support

Duct

burners

required

Actual NYISO

demand

Max capability

with GTs onlyMax Amount of DB

Energy Actually

Needed

11NeuCo Proprietary

Page 12: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Actual NYISO

demand

Potential NYISO

demand

Predicting Peak Output

Max capability

with GTs only

12NeuCo Proprietary

Page 13: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Duct Burner Management

Before Optimization

Duct

burners

required

Duct burners

operating

Duct burners were turned on when GT IGV angle > 74o

Annual fuel cost of excess use: $3 million

DB Energy Input,

scaled to fixed

expectation of

typical worst case

ramp

13NeuCo Proprietary

Page 14: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Duct Burner Management

After Optimization

Duct

burners

required

Duct burners

operating

Duct burners were turned on when

predicted 30 minute max demand > 980 MWs and GT IGV angle > 74o

DB Energy Input equal

to current risk of

needing it

14NeuCo Proprietary

Page 15: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

HR vs. Ramp Rate Readiness

15NeuCo Proprietary

Page 16: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

How The Optimizer Works

Predicts maximum likely demand over the next 30

minutes

Adds only enough Duct Burner fuel to offset shortfall in

case of maximum likely demand

Uses dynamic modeling to avoid over-shooting and

under-shooting

Predicts true combined cycle capability without duct

burners in 30 minutes given current state and history

Enables users to specify how certain they want to be

that they’ll meet demand

16NeuCo Proprietary

Page 17: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Application Evolution

Dmd Change30Min NN

Dmd30Min NN

MaxDmd Bound 30Min

PlantMaxCap30Min

PlantMaxCap NoDBs

Production

Closed-Loop Actuator

17NeuCo Proprietary

Page 18: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Max Thirty Minute Demand Predictor

(Model Ensemble)

18NeuCo Proprietary

Page 19: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Max Thirty Minute Demand Predictor

(Conservatively tuned)

19NeuCo Proprietary

Page 20: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Thirty Minute Max Demand Predictor

(Aggressively tuned)

20NeuCo Proprietary

Page 21: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Thirty Minute Max Demand Predictor

(Aggressively tuned + Expert Rules)

21NeuCo Proprietary

Page 22: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Thirty Minute Max Demand

Prediction Error

22NeuCo Proprietary

Page 23: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Application Evolution

GTMax NNGTMax NN

GTMax NNGTMax NN

STMax NNSTMax NN

Dmd Change30Min NN

Dmd30Min NN

MaxDmd Bound 30Min

PlantMaxCap30Min

PlantMaxCap

PlantMaxCap NoDBs

DB, PredDmd, IGV rules

Production

Closed-Loop Actuator

23NeuCo Proprietary

Page 24: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Neural Model Prediction of GT

Max Capability

24NeuCo Proprietary

Page 25: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Max 30 minute Demand and

Max Capability Predictions

25NeuCo Proprietary

Page 26: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Max 30 minute Demand and

Max Capability Predictions

26NeuCo Proprietary

Page 27: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

ISO Regulation Ancillary

Services “Performance Index”

27NeuCo Proprietary

Page 28: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

The Challenge

Total GT fuel

Total GT MW

Total DB fuel

Total ST MW

28NeuCo Proprietary

Page 29: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Evolution

GTMax NNGTMax NN

GTMax NNGTMax NN

STMax NNSTMax NN

Dmd Change30Min NN

Dmd30Min NN

MaxDmd Bound 30Min

PlantMaxCap30Min

PlantMaxCap

GTHeadroom

PlantMaxCap NoDBs

Dynamic Plant Model

GT Headroom Guide

DB, PredDmd, IGV rules

Production

MPC Optimizer

Closed-Loop Actuator

29NeuCo Proprietary

Page 30: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Closed-Loop MPC Duct Burner Optimizer

30NeuCo Proprietary

Page 31: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Closed-Loop Optimizer

Manipulated Variables

Optimizer uses a dynamic model to predict optimal Duct Burner (DB) fuel flow trajectory (GT fuel flow trajectory can also be predicted)

Then it biases the IGV angle start and stop thresholds in the DCS to inhibit or encourage burner activation

And biases the DCS fuel flow curve to control DB heat input more precisely, once a DB is running

31NeuCo Proprietary

Page 32: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Predicting 30 Minute Max Demand

Neural Net model of future demand and demand variance in 30

minutes

Inputs: Past demand/demand-variance (series of tap delays), time of

day, day of week, ambient temp, humidity, barometric pressure.

Combined in an ensemble, with a set of rules that leverage the

model’s prediction error, enforce limits to deal with special cases,

and allow for tuning of risk

To create a max limit for likely demand over the next 30 minutes32NeuCo Proprietary

Page 33: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Predicting 30 Minute Max Demand

Prediction of 30-minute max likely demand is compared

to 30 minute max plant capability

Any potential shortfall needs to be compensated for by

adding duct burner energy and running with more GT

capacity in reserve (aka more “GT headroom”)

33NeuCo Proprietary

Page 34: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Closed-Loop Optimizer Objectives

Dampen ST swings

Maintain sufficient spare GT capacity to meet possible future demand ramps

Minimize DB fuel

34NeuCo Proprietary

Page 35: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Evolution

GTMax NNGTMax NN

GTMax NNGTMax NN

STMax NNSTMax NN

Dmd Change30Min NN

Dmd30Min NN

MaxDmd Bound 30Min

PlantMaxCap30Min

PlantMaxCap

GTHeadroom

PlantMaxCap NoDBs

Dynamic Plant Model

GT Headroom Guide

DB, PredDmd, IGV rules

Production

MPC Optimizer

Closed-Loop Actuator

Plant HR NN

Benchmarking

35NeuCo Proprietary

Page 36: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Real-Time Analytics: Benchmarking

36NeuCo Proprietary

Page 37: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Real-time Analytics: Benefits Benchmarking

37NeuCo Proprietary

Page 38: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Benefits Benchmarking

Project Timeline:

• March 2013 Project kickoff

• September 2013 Initial closed-loop optimizer was tested.

• April 2014 New version of the optimizer was deployed using Model

Predictive Control (MPC) and a neural-first principles hybrid model

to predict max plant capability

38NeuCo Proprietary

Page 39: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Benefits Benchmarking (8/30/14)

NN 2 Test

NN 1 Test

NN 2 Train

NN 1 Train

39NeuCo Proprietary

Page 40: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Benefits Update (12/16/2014)

NN 2 Test

NN 1 Test

40NeuCo Proprietary

Page 41: Combined Cycle Plant Duct Burner Optimization Using ... · Combined Cycle Plant Duct Burner Optimization Using ProcessLink David Hinshaw ( Plant Engineer, Dynegy-Independence Station)

Benefits Update (12/22/2014)

NN 2 Test

NN 1 Test

41NeuCo Proprietary