Using computer models to save energy: An early …npcw17.imm.dtu.dk/Proceedings/Session 3 Control...

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Krones GB-GM SPBT We do more.1 Using computer models to save energy: An early warning model for tunnel pasteurizer energy consumption Falko Jens Wagner 17th Nordic Process Control Workshop Technical University of Denmark

Transcript of Using computer models to save energy: An early …npcw17.imm.dtu.dk/Proceedings/Session 3 Control...

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Using computer models to save energy: An early warning model for tunnel pasteurizer energy consumption

Falko Jens Wagner 17th Nordic Process Control Workshop Technical University of Denmark

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Agenda

How does a pasteuriser work? The PU Control system Possible faults

Introducing the Virtual Pasteuriser Diagnosing possible faults Real-life example

Conclusion and Outlook

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Krones SHIELD Pasteuriser

Pasteurisation is heating and cooling of products - Inlet temperature 3-5°C - Typical pasteurisation temperature 62°C - Killing Point 60°C - Discharge temperature 25-30°C - Heating and cooling in steps (zones)

Tunnel Pasteuriser - Pasteurises filled cans or bottles - Typically beer and softdrinks - Heat transfer by spraying products with

water in individual zones

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Water circulation and temperature corrections

Water is pumped from the bottom chanel to the spray system The spray water flows across the products on 1, 2 or 3 decks, and via a catch-plate the water

is fed back to the bottom chanel Temperature change is achieved by adding

hot or cold water before the pump

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Tunnel pasteuriser energy regeneration

Energy is reused by cross-pumping water between heating and cooling zones

Temperature set points are calculated so temperature change of spray water is equal in heating and cooling zones

During normal operation, energy is only added to the hot zones

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Energy flow in tunnel pasteurisation process

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added Heat is added removed. … …

Heat loss to environment

Heat loss between zones

Energy balance through regeneration

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Temperature model and Pasteurisation Units (PU)

Product temperature (inside can/bottle) is obtained through heat transfer equations - Heat transfer coefficients are based on

measurements in a controlled environment

Empirical formula accepted as standard

- 1 PU = 1 minute @ 60°C - Based on product (content) temperature - Exponential formula (Z = 6.94, X = 60°C)

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60/10dt

dPU ZXTproduct

=

( )

( )productwallspraywall

productwallproduct

T,T,Tdt

dT

T,Tdt

dT

Func

Func

=

=

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The PU Control

Optimization: Achieve minimum PUs, reduce maximum as much as possible - By heating (with steam) and cooling (with freshwater) => Here is where the money

goes! Temperature model is used to predict achieved PUs Prediction is used to control temperature set points in pasteurisation zones

- Too many PUs -> Lower temperature set points - Too few PUs -> Higher temperature set points

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PU pick-up Predicted PU

PID-Controller

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PU Control - Steady State Operation

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PU Control – Interrupted production (Stop)

To ensure, that the critical (worst) product in each pasteurisation zone achieves a minimum of PUs, some products will reach a higher degree of pasteurisation.

Highest PU in same zone as worst product

Critical (worst) product in zone has to achieve the desired PUs

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Possible Machine Faults

Leaking valves Water mixing due to incorect water level in buffer tanks (open system, water level measured

by pressure sensors) Wear on pump impellers giving incorrect flow, causing water imbalance and thus overflow Wrong assembly of pumps and orifices after maintenance Faulty temperature sensors Structural integrity of buffers (rust, corrosion)

The PU Control optimizes the pasturisation process with the only concern being the PUs To optimize the PUs, enormous amounts of energy and water can be used

- Especially, when the machine is not working as it should due to faults. The challenge is to raise awareness and give the operator a possibility to detect, whether a

machine uses more energy and water than it should - By analysing the pasteurisation process and determining the theoretical (optimal) amount

of energy used.

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The Challenge

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What is a Virtual Pasteurizer?

vs

Computer model

Actual machine

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Purpose To monitor the behavior of a running pasteurizer

- Early warning model To obtain better process knowledge To serve as a development tool for improvements

Calculates the theoretical utility consumption of - Water - Steam

Compares the actual consumption with the theoretical values - Actual consumption

• How much energy is the machine actually using? • Based on flow and temperature measurements

- Theoretical consumption • Based on temperature model

Analyses the difference, displays warning messages and gives the operator a hint to where the problem could be.

What does it do?

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Theoretical consumption – product energy

pasteurized Products are heated cooled. … …

)( _ OLDcontentcontentPPP TTCmQ −= ∑=MaxAUZ

PTOTP nQQ ,

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Theoretical consumption – energy losses

Energy loss to environment

Energy loss between zones

)( envZZL TTkAQ −=

)()( 11 +− −+−= ZZNNZZNNN TTAkTTAkQ

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Measurements

Filler speed signal

PU Control³

Siemens IO-Rack

PT100 Environment Temperature

IR Sensor

PLC Serial / Ethernet

Ethernet IO

24 / 120 V

Choice

PLC Comm.

24 V

Flow meter Flow meter

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System compares

Process / theoretical

Heat going into products Heat taken out of products Heat loss to environment Water mixing between zones

Machine / actual

Heating valves opening and flow Cooling valves opening and flow Zone vs. environment temperature Difference between zone temperatures

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Measurement data – fluctuations in utility consumption

Virtual Pasteuriser

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Measured actual consumptionCalculated theoretical consumption

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Comparison between discrete actual cooling and theoretical consumption

Actual Consumption Theoretical Consumption

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Measurement data – 1 hour moving average

Virtual Pasteuriser

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kW

Measured actual consumption (1h avg)

Calculated theoreticall consumption (1h avg)

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Detailed description of possible faults detected by VP

Leaking valves Water mixing Integrity of buffer tanks

Zone 1 Zone 2 Zone 3 Zone 4 Zone 5 Zone 6 Zone 7 Zone 8 Zone 9 Zone 10

Actual

Theoretical

Consumption:

Normal operation

Main energy consumption in hot zones

Energy balance in regenerative zones = 0 consumption

Total

Total energy consumption CHESS heat exchanger

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Leaking cooling valve – pasteurization zones

A leaking cooling valve is not detected by the standard control system. It results in an unwanted cooling water flow into the zone, which is counteracted by an

additional heating water flow to keep zone temperature set point.

Zone 1 Zone 2 Zone 3 Zone 4 Zone 5 Zone 6 Zone 7 Zone 8 Zone 9 Zone 10

Actual

Theoretical

Consumption:

Actual energy consumption is higher than theoretical

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Water mixing between zones – regenerative zones

Water mixing between zones is not detected by the standard control system. It results in unwanted hot and cold water additions to the zones involved to keep the zones at

their respective set points. This combination predicts possible water mixing between to adjacent zones.

Zone 1 Zone 2 Zone 3 Zone 4 Zone 5 Zone 6 Zone 7 Zone 8 Zone 9 Zone 10

Actual

Theoretical

Consumption:

Actual energy consumption is lower than theoretical. Cooling is added to counteract.

Actual energy consumption is higher than theoretical

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1 Screen - Theoretical and actual values

Each bar compares actual

and theoretical consumptions - Alarm is displayed

if deviation is larger than allowed

Additional information - Current fill factor - Current infeed temperature - Time between filler and pasteuriser

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Example from running plant

Notice how last hot zone is using more energy than it should? .....

This gives rise to the operator to look and investigate in this Particular zone ......

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... and here is the reason!

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Water flowing from colder, neighbouring zone into hot zone, causing control system to counteract by opening heating valve to keep constant temperature

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Conclusion

By using the Virtual Pasteuriser it is possible to detect faults on the equipment immediately. - Matter of hours

Without, the increased energy and water consumptions was possibly detected after a long observation period - Typically months

Savings are eminent and the system is currently being extended to other utilities - Electricity - Compressed Air

Side-effect and additional benefit - Analysis with the Virtual Pasteuriser has shown a time-lag between the actual energy

consumption and the theoretical consumptions due to transport delays in the system. - Work is going on to use this knowledge to make a faster PU-Control system.

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