Advanced Process Control for ARC

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1 Advanced Process Control Presented by Anil K. Choudhari

Transcript of Advanced Process Control for ARC

Page 1: Advanced Process Control for ARC

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Advanced

Process ControlPresented by

Anil K. Choudhari

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What is APC?

• APC = Advanced Process Control

• A traditional control system controls processes to fixed set points

determined by operators. Uses generic control algorithms and instructions

such as a PID controller.

• The purpose of an APC system is to automatically account for an

expected (modeled, predicted…) process response and calculate

“optimal” control actions to minimize process variation.

• APC systems utilize controllers and technologies such as

– Model based control

– Fuzzy logic and control

– Multivariable control

– Adaptive control

– Inferential control

– Process modeling and simulation

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Steam

PIC

Pressure SP

Typical Process Control

Flow

Density

FIC

Product

Inlet

Density

DI

Flow SP

Concentrate

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Advanced

Process

Controller

MV1

MV2

CV1

CV2

FV1

Steam

PIC

Advanced Process Control

FIC

Product

Inlet

Density

DIConcentrate

Flow

Density

Density SP

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The Business Challenges

Increased customer demands

Better quality

Greater quantities

Tighter specifications

Higher operating costs

Fuels

Energy

Personnel

Transportation

Increased competition

Internal capital

Other suppliersHow Can Your Business Flourish in this

Environment?

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Solutions for the Business Challenges

Economic benefits from APC

Throughput increase 4 - 10%

Yield increase 0.1 – 10%

Energy savings 3 - 10%

Variation reduction 20 – 90%

Reduce variation of key process and quality parameters

Increase plant capacity via tighter and smarter controls

React correctly and quickly to changing conditions

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Achieving Dairy

Manufacturing Excellence

using the APC

Milk Powder Solution Overview

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Issues & Trends

In the times when price of energy is increasing day by day & dairy plant is high energy consuming plant we should look into them first. One of the area can be the milk powder plant which is based on spray drying technology which is very costly way of reducing moisture from the milk.

Now a days many technologies are available to make the plant efficient but very few look into realizing process potential and achieve performance excellence with the help of automation available for industry.

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Benefits of APC

Advanced automation strategies help to ensure steady

performance of plants. Site analyses of Powder plant

indicate that the various parameters to be maintained are

not always steady.

Moreover the variations of a basic parameter have not always

been accompanied by corresponding proportionate

variations of other related parameters.

This has added to the instability in batch cycle time,

productivity and product consistency of Powder Plant.

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Commercial Benefits

By using advance automation, some of the tangible benefits derived can be :

– Increased Production of Valuable Products`

– Reduced Energy Consumption

– Predictable Process Performance

– Fewer Unscheduled Shutdowns, Improved Stability and Longer Equipment Life

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Pavilion8

Dryer Controller

Process (Manipulated Variables)

Uncontrolled Influences(Disturbance Variables)

Process Results(Controlled Variables)

Abs humidityFeed solids

Dryer Exhaust RH

Solids throughput

Product Moisture

Air flows

Setpoints(Manipulated Variables)

Uncontrolled Influences(Disturbance Variables)

Process Results(Controlled Variables)

Dryer Exhaust Temp

Dryer Inlet Air Temp

SFB Inlet Air Temp

Fluid Bed Inlet Temp

Abs humidityFeed solids

Dryer Exhaust RH

Solids throughput

Product Moisture

Air flows

Dryer Controller

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Spray Dryer application drying Cheese Whey

• Feed : 8000 Kg/Hr. processing with 9% final moisture

• 3760 Kg/Hr. solids

• Change in operational setpoints with use of Advance

automation

• Revised Final Moisture: 10%

• 1% increase in moisture due to better multivariable control

• 1% increase translates to 46 Kg/Hr. additional product (as

water)

• Assume dryer operation at 288 days/year, 24 hours/day

• ~6900 hours/year

• Total increase in production: 317 Tons/year

• Value of Increase: 250 – 317 Tons/year

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Commercial Benefits

• Key is price of product: $1.20 - $1.50/Kg…..or higher!!

• NFDM

• Cheese Whey

• Lactose

• WPC Powder

• Automation Sell Price: $300 - $400K

• Moisture Analyzers

• Software and associated APIs

• Design/Engineering

• Remote Support (optional)

• Payback: 9 - 15 months

This can be an eye opener if you really crave for energy in your country.

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Where the Technology stands today & how it works

More than 30 similar advanced control projects

have either been put in place or are in the

process of being installed in milk powder,

casein and cheese plants.

The technology permits operators to accurately

control factors that alter milk's quality and

consistency during the evaporating and drying

cycles.

Using models obtained from process data

allows to predict the future performance of the

plant, enabling correction before external

factors come through and affect the operation.

Process

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Additional benefits to the dairy which cannot be quantified

• Improvement in powder Quality by precisely controlling

moisture & bulk density of milk powder.

• Reduction in stack loss & improvement in environment.

• Reducing energy consumption by adaptive controls ( 3 to

10% savings)

• Quicker, more effective start - up.

• Reduces wastages & reworking by stopping choke-ups &

plant shutdowns.

• Improves thermal efficiency.

• Improves safety of plant

• Reduces fouling will reduce frequent requirement of CIP

• MIS, ERP & Energy management

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Cheese Cooker

Temperature

and

Moisture Control

Advanced Process Control (APC) Case Study

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Upstream Cheese

Supply

Controlled Variable

Manipulated Variable

Measured (known) Variable

KEY:

Temperature

Water Content

Water

Steam Pressure

Weight

Moisture

Recipe

Valve Position

Temperature

To Downstream

Processing

Additives

Weight

Moisture

Water Quantity

Generic Cheese Cooker Diagram

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Control Objectives

Control temperature in batch cookers

Achieve consistent product temperature profiles and batch times

Achieve consistent steam condensation in cookers

Achieve consistent, closer to target, final product temperature

Control product moisture

Achieve tighter and consistent control of downstream line moisture

Make model based adjustments between moisture lab samples

Consistent water addition adjustments per downstream line feedback

Temperature and moisture

Enable maximum possible line throughput

Enable maximum possible moisture content

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Business Objectives

OBJECTIVES ACTUAL RESULTS

Line throughput increase 7.6%

Yield increase 0.15% (based on moisture content only **)

Steam usage reduction 7.7% (less energy used)

Batch time reduction 13.5% (less time per batch)

Temperature variation reduction 40%

Operational benefits consistent control adjustments

consistent cheese quality

** Additional yield increase possible due to scrap/rework reduction

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Key Features of Temperature Control

Modeling

Dynamic heat/mass cooker model was developed and used to design, test

and evaluate control algorithms

Batch cycle temperature control

Constraint control (control final temperature to a minimum)

Control to multiple set points during different phases of cooker batch

Timing (follow batch logic to quickly satisfy conditions for next steps)

Expert (use expert set starting values for optimal initial conditions)

PID (instruction used for fast feedback corrections)

Steam valve manipulation (manipulated variable, actuator)

Controller tunable per recipe

Controller integrated in CLX/PLC, reusable code

Bumpless controller switching ON/OFF

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Key Features of Moisture Control

Modeling

Based on upstream sampling per cooker load

Mathematical model used for real time calculations

Controls

Model based compensation for upstream variation

Operator adjustments available (if needed)

Downstream line adjustments

Operator input: Set point (target) for product moisture

Output: water addition correction

Tunable magnitude of adjustments

Controller integrated in CLX/PLC, reusable code

Bumpless switching ON/OFF

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Final Product Temperature Before-After

Reduction of average final temperature and reduction of final temperature variation contribute to

downstream faster processing.

BEFORE AFTER IMPROVEMENT

AVERAGE minus MINIMUM 2 deg F 1.4 deg F 30%

STANDARD DEVIATION 1.4 deg F 0.7 deg F 50%

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Steam Consumption Before-After

Average Steam Consumption Reduction: 7.7%

Equivalent of: 68 PSIhours/day

DEC 04 = BASELINE

PS

Imin

Cooker #1: BLUE

Cooker #2: RED

Average: YELLOW

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Batch Time Before-After

Batch time improvements, RECIPE 1:

Batch time BEFORE: 255 seconds

Cooker #1 AFTER: 217 seconds

Cooker #2 AFTER: 228 seconds

Batch time improvements, RECIPE 2:

Batch time BEFORE: 200 seconds

Cooker #1 AFTER: 188 seconds

Cooker #2 AFTER: 188 seconds

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Moisture Control Before-After

Before After

Tests

Approximately 10-15% variation reduction, improved controllability.

Enabled moving the target to economically more favorable setting.

Target

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Industry Solutions

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Achieving Biofuel

Manufacturing Excellence

Using APC

Biofuel Solution Overview

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Ethanol Production

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Slurry Solids/Water Balance Control Application

Capabilities

– 50% reduction in slurry solids/pH variability

– Continuous management of fermentation gap increasing capacity and stabilizing plant to milling target

– Stabilize mineral/backset conditions to fermentation

– Manage process water toward global requirements/make-up

Benefits

– Increase ethanol yield (~2% gal/bu)

– Increase fermentation capacity (MMGPY)

– Increase enzyme effect (enzyme/gal)

8 8

Methanator

Slurry Tank

Process Water

Liquefaction

Backset

Beer Feed

Milling

88 88

MethanatorMethanator

Slurry Tank

Process Water

Liquefaction

Backset

Beer Feed

Milling

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Fermentation Control Application

Capabilities

– 50% reduction in batch EtOH and dextrose/residual sugars variability

– Continuously manage enzymes to maximize throughput and ethanol yields

– Optimal target on temperature and pH for fermentation

– Manage fermentations to match production targets

Benefits

– Increase in batch drop ethanol yield (MMGPY) by 0.5-1.0%

– Increase in fermentation capacity by 5-12% (MMGPY)

– Increase in batch yields (gal/bu) by 2-5%

– Reduce enzymes/gal ($$ enzymes/gal) by 5-10% 8

Slurry Tank

Liquefaction

Backset

Beer Feed

FermenterYeast Propagation

Enzymes

88

Slurry Tank

Liquefaction

Backset

Beer Feed

FermenterYeast Propagation

Enzymes

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Beer Feed

Evap. Steam

Steam Flow

Sieve Back

Pressure

Rectifier Reflux Sieve Feed

Vaporizer Temperature

Beer Feed

Evap. Steam

Steam Flow

Sieve Back

Pressure

Rectifier Reflux Sieve Feed

Vaporizer Temperature

Distillation / Molecular Sieve Application

Capabilities

– Integrate non-linear models, multivariable control and advanced optimization in one algorithm

– Control distillation to optimum moisture

– Control end-product moisture to the desired specifications

Benefits

– Increase Ethanol production capacity 3-10%

– Increase ethanol yield by .1-.2%

– Reduce energy use/gallon by 1-2%

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Dryer Control Application

Capabilities

– Direct targeted control of Syrup Solids and DDGS moisture

– Continuous management of dryer capacity (centrifuge feed) against dryer operating limits (moisture, temperature, gas)

– Balance dehydration energy between evaporation and drying

– Reduce Overdrying, stabilize dryer and reduce energy consumption/ton

– Stabilize plant steam and thermal oxidizer thermal destruction temperature against operating limits

Benefits

– Increase average DDG yield of 1-1.5%

– Reduce energy costs per gallon of ethanol produced by 2-4%

– Reduce product moisture variability by more than 50%

Steam Flow

Centrifuge Feed

Whole Stillage

Thin Stillage

Syrup Tank

Wet Cake

Pad

Steam Flow

Centrifuge Feed

Whole Stillage

Thin Stillage

Syrup Tank

Wet Cake

Pad

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Benefits of APC Are Substantial for Ethanol Manufacturers

Revenue

3 – 6%2.5 – 5% 1 – 2%5 – 8%

Reduce energy costs (BTU/gal)Improved ethanol yields (gal/bu)Improved DDGS yields Reduce enzyme usage (gal/Kgal)

Operating Cost

2 – 10% Increase production volume (MMGPY)

% IMPACTESTIMATED BENEFITS

Typical Project Payback < 6 mo.Typical Project ROI > 200%Project Duration 4-12 months

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APC Project Flow

Enhance Profitability

– Increase Production

• Unlock capacity

• Maximize throughput

– Reduce Manufacturing Costs

• Use less energy per unit of output

• Maximize alternative fuels use

– Improve Product Quality

• Minimize variability

• Reduce deviation from

specifications

– Reduce Environmental Risk

• Achieve active emissions

compliance

• Support emissions trading

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For more details

Contact : Anil K. Choudhari

[email protected]