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An Optimal Power-Dispatching Control
System
for the Electrochemical Process of Zinc Based
on
Back-propagation and Hopfield Neural
Networks
Chunhua Yang, Geert Deconinck, Senior Member, IEEE, and
Weihua Gu, IEEE TRANSACTIONS ON INDUSTRIAL
ELECTRONICS, VOL. 50, NO. 5, OCTOBER 2003
Presented by: - Soumyadeep Nag
Aim
• The main aim of this project was to reduce the electricity consumed and associated
cost by a Zinc smeltery under a dynamic pricing environment
• To reduce the consumption during the peaks and increase the consumption during the
valley periods of dynamic pricing by optimizing the current supplied
Data Collection
• 4 months of data consisting of 6 values of the ratio Cs/Czn for 20 different current
densities giving a total of 120 experiments from where the current efficiency, cell
voltage and energy consumed were measured.
Procedure
• Modeling the process with Feed forward NN
• Modeling the constraints and framing the energy function
• Optimization with Hopfield NN
• Training the NNs with error back propagation algorithm
Results
• Implementation of the algorithm into the plant
• .7% reduction of cost per ton of zinc produced = 3052.2 kWhr/t to 3030.5 kWhr/t
• Yearly savings of 7,844,588$
Abstract
Arrangement of cells
Series connection of cells
Anode
cathode
Plant under consideration
• Zhuzhou smeltery – 250,000 tons of zinc/year
• Energy consumed – 800 million units
• Consists of 2 units – Unit A has 240 cells and Unit B
has 208 cells
• Dynamic pricing - 4 pricing periods
A = basic price = .054 $/kWhr
The electrochemical process of zinc
extraction
•The aim is to decrease the current
density during the period of high price
and increase the current density during
the period of low price
•Zinc output directly depends upon the
amount of current, or current density,
that passes through the electrodes
• However, too high or too low current
density may affect efficiency of the
process, product quality and may lead to
irregular production
SALPHERITE  Roasting
• 2ZnS + 3O2  2ZnO + 2SO2
Leaching
• ZnO + H2SO4  ZnSO4 + H2O
Electrolysis  Electro wining
• ZnSO4 + H2O = Zn + H2SO4 + 1/2O2
Objective functions and constraints
- Quantitative constraint
for daily output
- Qualitative constraint
imposed on current
density
Structure of a Hopfield network
• Symmetric
• Single layered
• Fully connected
Energy Function for Training the
Hopfield NN
Modified Energy Function
Training the Hopfield NN
Measured and computed data for the
120 experiments
Measured and computed data for the
120 experiments
Architecture of BPNN-V and BPNN-ῃ
Training the Hopfield NN
Training the BPNN
MSE for cell voltage
MSE for current
efficiency
Adjusting the weights
with error back
propagation
x(l) is the matrix of current weights and
biases
Results
BPNN modification with new samples
Obtaining the optimized schedule
Rectifier control and sensor
information collection including
current
Tracks the optimal current
Regulated rectifiers with SCRs after
the transformer that are current
controlled Provide alarms - Record data -
Diagnose faults – Generate trend
curves
Results
Quantity Change
Decrease in energy
consumed per ton of zinc
0.7%
Production deviation .5%
Total annual decrease in cost
of energy consumed
$ 7,844,588
Cost of energy saved due to
reduction in power
consumed during peak hours
$ 1 985 903
Cost of energy saved due to
increase in power consumed
during valley periods
$5,858,675
• Not only does it reduce the cost of production but it also relieves the grid during peak
load hours and levels the load by increasing the power consumed during the off – peak
hours, hence stabilizing the grid.
Test Code
w(1,1)=swarm(j,1,1);
w(1,2)=swarm(j,1,2);
w(2,1)=swarm(j,1,3);
w(2,2)=swarm(j,1,4);
b(1)= swarm(j,1,5);
b(2)= swarm(j,1,6);
y=w*O+b';
O(1)=(5/(1+exp(-y(1)))+5)';
O(2)=(6/(1+exp(-y(2)))+1)';
J(j)=(O(1)-9)^2+(O(2)-5)^2;
if J(j)<abs(swarm(:, 4, 1))
O
for dim=1:6
swarm(j, 3, dim) = swarm(j, 1, dim);
end
swarm(j, 4, 1) = J(j);
end
end
Test functions
J(j)=(x1-9)^2+(y-5)^2;
J(j)=(100*(x2-x1^2)^2 +(x1-1)^2);
J(j) = -20*exp(-.2*sqrt(.5*(x1^2+x2^2)))-
exp(.5*(cos(2*pi*x1)+cos(2*pi*x2)))+exp(1)+2
0;
Sphere function
Rosenbrock function
Ackley’s function
X1, x2 = 9,5
X1, x2 = 1,1
X1, x2 = 0,0
Results – Sphere function
X =
9.0000
4.9873
weights and biases
w =
0.0846 0.1352
0.0135 0.0972
b = 0.0223 0.0997
Value of the energy function
ans =
1.6226e-004
Results – Rosenbrock function
X=
1.0140
1.0288
weights and biases
w =
0.0157 0.0278
0.0302 0.0221
b = -0.0254 -0.0049
Value of the energy function
ans = 2.2793e-004
Ackley’s Function
O =
1.0e-003 *
0.1282
-0.0329
Value of the energy function
ans = 3.7479e-004
weights and biases
w =
0.0008 0.0055
0.0015 -0.0180
b =
1.0e-004 *
0.6434 -0.5106
Thank you

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Neural networks based zinc smeltry operation optimisation

  • 1. An Optimal Power-Dispatching Control System for the Electrochemical Process of Zinc Based on Back-propagation and Hopfield Neural Networks Chunhua Yang, Geert Deconinck, Senior Member, IEEE, and Weihua Gu, IEEE TRANSACTIONS ON INDUSTRIAL ELECTRONICS, VOL. 50, NO. 5, OCTOBER 2003 Presented by: - Soumyadeep Nag
  • 2. Aim • The main aim of this project was to reduce the electricity consumed and associated cost by a Zinc smeltery under a dynamic pricing environment • To reduce the consumption during the peaks and increase the consumption during the valley periods of dynamic pricing by optimizing the current supplied Data Collection • 4 months of data consisting of 6 values of the ratio Cs/Czn for 20 different current densities giving a total of 120 experiments from where the current efficiency, cell voltage and energy consumed were measured. Procedure • Modeling the process with Feed forward NN • Modeling the constraints and framing the energy function • Optimization with Hopfield NN • Training the NNs with error back propagation algorithm Results • Implementation of the algorithm into the plant • .7% reduction of cost per ton of zinc produced = 3052.2 kWhr/t to 3030.5 kWhr/t • Yearly savings of 7,844,588$ Abstract
  • 3. Arrangement of cells Series connection of cells Anode cathode
  • 4. Plant under consideration • Zhuzhou smeltery – 250,000 tons of zinc/year • Energy consumed – 800 million units • Consists of 2 units – Unit A has 240 cells and Unit B has 208 cells • Dynamic pricing - 4 pricing periods A = basic price = .054 $/kWhr
  • 5. The electrochemical process of zinc extraction •The aim is to decrease the current density during the period of high price and increase the current density during the period of low price •Zinc output directly depends upon the amount of current, or current density, that passes through the electrodes • However, too high or too low current density may affect efficiency of the process, product quality and may lead to irregular production SALPHERITE  Roasting • 2ZnS + 3O2  2ZnO + 2SO2 Leaching • ZnO + H2SO4  ZnSO4 + H2O Electrolysis  Electro wining • ZnSO4 + H2O = Zn + H2SO4 + 1/2O2
  • 6. Objective functions and constraints - Quantitative constraint for daily output - Qualitative constraint imposed on current density
  • 7. Structure of a Hopfield network • Symmetric • Single layered • Fully connected
  • 8. Energy Function for Training the Hopfield NN
  • 11. Measured and computed data for the 120 experiments
  • 12. Measured and computed data for the 120 experiments
  • 13. Architecture of BPNN-V and BPNN-ῃ
  • 15. Training the BPNN MSE for cell voltage MSE for current efficiency Adjusting the weights with error back propagation x(l) is the matrix of current weights and biases
  • 16. Results BPNN modification with new samples Obtaining the optimized schedule Rectifier control and sensor information collection including current Tracks the optimal current Regulated rectifiers with SCRs after the transformer that are current controlled Provide alarms - Record data - Diagnose faults – Generate trend curves
  • 17. Results Quantity Change Decrease in energy consumed per ton of zinc 0.7% Production deviation .5% Total annual decrease in cost of energy consumed $ 7,844,588 Cost of energy saved due to reduction in power consumed during peak hours $ 1 985 903 Cost of energy saved due to increase in power consumed during valley periods $5,858,675 • Not only does it reduce the cost of production but it also relieves the grid during peak load hours and levels the load by increasing the power consumed during the off – peak hours, hence stabilizing the grid.
  • 18. Test Code w(1,1)=swarm(j,1,1); w(1,2)=swarm(j,1,2); w(2,1)=swarm(j,1,3); w(2,2)=swarm(j,1,4); b(1)= swarm(j,1,5); b(2)= swarm(j,1,6); y=w*O+b'; O(1)=(5/(1+exp(-y(1)))+5)'; O(2)=(6/(1+exp(-y(2)))+1)'; J(j)=(O(1)-9)^2+(O(2)-5)^2; if J(j)<abs(swarm(:, 4, 1)) O for dim=1:6 swarm(j, 3, dim) = swarm(j, 1, dim); end swarm(j, 4, 1) = J(j); end end
  • 19. Test functions J(j)=(x1-9)^2+(y-5)^2; J(j)=(100*(x2-x1^2)^2 +(x1-1)^2); J(j) = -20*exp(-.2*sqrt(.5*(x1^2+x2^2)))- exp(.5*(cos(2*pi*x1)+cos(2*pi*x2)))+exp(1)+2 0; Sphere function Rosenbrock function Ackley’s function X1, x2 = 9,5 X1, x2 = 1,1 X1, x2 = 0,0
  • 20. Results – Sphere function X = 9.0000 4.9873 weights and biases w = 0.0846 0.1352 0.0135 0.0972 b = 0.0223 0.0997 Value of the energy function ans = 1.6226e-004
  • 21. Results – Rosenbrock function X= 1.0140 1.0288 weights and biases w = 0.0157 0.0278 0.0302 0.0221 b = -0.0254 -0.0049 Value of the energy function ans = 2.2793e-004
  • 22. Ackley’s Function O = 1.0e-003 * 0.1282 -0.0329 Value of the energy function ans = 3.7479e-004 weights and biases w = 0.0008 0.0055 0.0015 -0.0180 b = 1.0e-004 * 0.6434 -0.5106

Editor's Notes

  1. Why has hopfield net been used for this purpose and not any other net?