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Business Accent
Adding value through the process dashboard
Process
control is an effective way to check and reduce inefficiencies in real-time,
say H Krishnan and R Krishnaiah in the concluding part of a two-part
series
Having captured and loaded production data into the SAP R/3 system for daily
report processing, process engineers were interested in getting real-time information
for better process control. Real-time data was available through workstations,
but gave factual data. What was needed was real-time information (and not data)
indicating the impact of operator actions on the bottomline.
In cement production, the focus is on controlling critical performance parameterspower
and fuel consumption. Hence these are reviewed by managers closely. However
at Rajashree Cements (Grasim Industries), fuel consumption (measured as Kcal/Kg
of clinker production) is not directly measured in the PLC systems. A heat balance
sheet is manually prepared wherein the total heat input is identified, and various
losses estimated based on process operating parameters such as air flow, temperatures
across kiln, ducts etc. From these, data fuel consumption (heat from coal burning)
is calculated. A sample sheet is shown here (Heat balance of the kiln). Earlier,
it was calculated manually, but now, it is generated by the PLC system on a
real-time basis.
Due to the complex calculations involved, and the need to collect more than
20 process parameters, the heat balance is not calculated continuously. Once
in two days, or during start ups or process upsets, data is taken from log sheets
by process engineers and calculations made. Hence the control room operators
are not able to monitor the impact of their actions upon these factors in real-time,
except in an indirect way.
Since this could contribute directly to operational improvement through better
monitoring, our team stepped in to provide a simple visual display for the control
room operator. The steps involved were several.
- Identifying the heat input, heat loss factors.
- Identifying the underlying theoretical calculation formulae.
- Identifying the process parameters required
- Identifying the instrument tags for these parameters,
if they are already measured by the PLC system
- Provide input screen for parameters not captured in PLC
system, as well for the constants.
- Develop the stepwise calculation.
- Connect the tags with parameter values in a spreadsheet,
for constant real time updation from PLC
- Make a visual display of critical performance parameters.
(heat input, heat output, loss of heat, heat utilised from fuel (Kcal/kg of
product) and false air in the system
Environment:
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What was needed was real-time
information indicating the impact of operator actions on the
bottomline
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Data was picked up from ABB MP280/1 system through an intermediate
real-time data analyser system named OSI-PI. Since a number of calculations
were involved, Excel was used as the interface for input as well as for display
of calculated output.
| Heat from coal burning Kcal/kg |
716 |
| False air (% Kiln) |
9.78 |
| False air (% Pyro) |
13.04 |
The final output sheet showing heat utilised, false air (%)
in the system is shown below. These values change based on real-time values
of tags.
Benefits:
- Control room operator can monitor critical parameters
and can also see the effect of his action in meaningful terms for improved
process control.
- Due to automation it is monitored continuously instead
of once in two days.
- Since this is an application using TCP/IP over LAN, it
can be installed in any PC even if it is away from the control room.
- Though the data can be monitored in real-time, to prevent
network choking, data is refreshed.
Lesson: Visual display and continuous feedback leads
to better operations.
| Heat input: |
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| Sensible heat of ambient air |
3.78 |
| Sensible heat of kiln feed |
13.69 |
| Sensible heat of fine coal |
1.08 |
| Heat from coal burning |
716.14 |
| (Back calculation)(Kcal/Kg) |
|
| Total |
734.69 |
| Heat output: |
|
| Heat of reaction (L) |
411.48 |
| Heat loss through pre-heater |
|
| Kiln |
58.10 |
| Pyro |
48.19 |
| Heat loss through rawmeal dust |
|
| Kiln |
1.74 |
| Pyro |
1.45 |
| Heat loss through evaporation |
5.25 |
| Surface loss through radiation &
convection |
85.13 |
| Heat loss through cooler exit gases |
95.35 |
| Heat loss through clinker |
28.00 |
| ( At 170oC ) |
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| Total |
734.69 |
H Krishnan, IT Head and R Krishnaiah, Senior Manager, Process
of Rajashree Cements
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