Rounding-Based Moves for Metric Labeling

 
INDIAN RARE EARTHS LTD,KOLLAM
By
ARUN S MATHEW
M110321EE
IREL PROFILE
IREL is a Mining Industry under Atomic Energy of
Energy, Govt of India.
God’s Own Country is blessed with long coastal belt.
Kerala is endowed with heavy deposits of
. Ilmenite
. Rutile
. Zircon
. Monazite
. Sillimanite
Products and Specifications
Magnetic and Electrostatic Properties
of Sand components
Fluidised Bed Dryer
 
Principle of operation
Advantages and Disadvantages
Uniform particle mixing
Uniform temperature gradients
Ability to operate reactor in continuous state
Disadvantages
. High Exhaust temperature
. As it is a single stage dryer, initial temperatures
should be very.
Identifying Energy Conservation
Opportunities
Ideal Drying curve of FBD
Drying curve of FBD at IREL
Calculation of SEC
Suggestion 1
Introduction to spray dryer
 
Adding Spray dryer as the first stage
Rating= 12.65W, 22 A
Feed rate
 
= 50 kg/hr.
Assuming 70% increase in efficiency
SEC of FBD reduces to 1.58 kWh/kg
Energy consumption 158 kWh
Cost of Energy consumption before implementation of
spray dryer= 228X30X6= Rs. 41,040
Cost of Energy consumption after implementation of spray
dryer= 158X30X6= Rs. 28,440
Saving per month= Rs. 12,600/-
Initial investment= Rs. 5, 60,000/-
SPP= 3.5 years
Suggestion 2
Convection Recuperators
Flue type Recuperator
Typical Recuperator
 
Working of Recuperator
 
Significance of Recuperator in IREL
Internal temperature
  
= 200°C
Exhaust temperature
  
=160°C
Calorific value of fuel oil
 
= 43,000 kJ/kg
 
Cost of fuel oil
  
= Rs. 30/kg
For drying 100 kg of slurry energy required = 100X2.09X175= 36,575 kJ
 
Fuel  required for 100 kg
 
= 0.85 kg
 
Cost of fuel oil
  
=Rs. 25.50/-
Assuming efficiency of 40% and thereby increasing the temperature of
primary gas from 25°C to 64°C
For drying 100 kg of slurry energy required = 100X2.09X136= 28,424 kJ
 
Fuel  required for 100 kg
 
= 0.66 kg
 
Cost of fuel oil
  
=Rs. 19.83/-
 
SPP
   
= 1.63 years
Thankyou
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This work introduces rounding-based moves for metric labeling, exploring efficient move-making algorithms and linear programming relaxation. The method involves defining label sets, unary potentials, pairwise potentials, and utilizing expansion algorithms. It discusses complete rounding, interval rounding, hierarchical rounding, and their equivalence in solving labeling problems accurately. The approach involves iteratively defining labelings and solving easier sub-problems to optimize solutions effectively.

  • Rounding-Based Moves
  • Metric Labeling
  • Linear Programming Relaxation
  • Expansion Algorithm
  • Labeling Problems

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  1. INDIAN RARE EARTHS LTD,KOLLAM By ARUN S MATHEW M110321EE

  2. IREL PROFILE IREL is a Mining Industry under Atomic Energy of Energy, Govt of India. God s Own Country is blessed with long coastal belt. Kerala is endowed with heavy deposits of . Ilmenite . Rutile . Zircon . Monazite . Sillimanite

  3. Products and Specifications Product Specification Specific Gravity Bulk density (kg/m) Major Application 1. Ilmenite TiO2-58% 4.45-4.54 2600-2630 TiO2 pigment, Ti metal 2. Rutile TiO2-95% 4.18-4.24 2630-2650 Used as flux in welding electrode industry 3. Zircon ZrO2-65% 4.60-40.7 2900-3000 In ceramics refractories, foundries & glass industry 4. Sillimanite Al2O3-58% 3.2-3.25 1950-2050 In refractory bricks, castable cordierites 5. Zirflor ZrO2-64% ------------- 1800-1850 In refractory and foundry coating, opacifier in ceramic industry 6. Micro Zir ZrO2-63.5% ------------- --------------- In ceramic glasses, heat resistant porcelain, refractories, plastics etc 7. Garnet Abrasive for sand blasting water jet cutting & glass polishing 8. Monazite Raw material for production of rare earth compounds

  4. Magnetic and Electrostatic Properties of Sand components Components Magnetic Properties Electrostatic Properties Ilmenite Magnetic Conducting Rutile Non- magnetic Conducting Leucoxene Weakly magnetic Non conducting Monazite Weakly magnetic Non conducting Zircon Non-magnetic Non conducting Sillimanite Non-magnetic Non conducting Balance material Non-magnetic Non conducting

  5. Fluidised Bed Dryer

  6. Principle of operation

  7. Advantages and Disadvantages Uniform particle mixing Uniform temperature gradients Ability to operate reactor in continuous state Disadvantages . High Exhaust temperature . As it is a single stage dryer, initial temperatures should be very.

  8. Identifying Energy Conservation Opportunities Ideal Drying curve of FBD Drying curve of FBD at IREL

  9. Calculation of SEC Input Supply Total Amps Total power consumed= ? ??? ?? ?.? = ??.???? Total working hours = 2X3=6 hours Energy consumption = 227.716 kWh Feed rate = 100 kg/hr SEC = 2.28 kWh/kg = 415V, 50 Hz = 66A

  10. Suggestion 1 Introduction to spray dryer

  11. Adding Spray dryer as the first stage Rating= 12.65W, 22 A Feed rate = 50 kg/hr. Assuming 70% increase in efficiency SEC of FBD reduces to 1.58 kWh/kg Energy consumption 158 kWh Cost of Energy consumption before implementation of spray dryer= 228X30X6= Rs. 41,040 Cost of Energy consumption after implementation of spray dryer= 158X30X6= Rs. 28,440 Saving per month= Rs. 12,600/- Initial investment= Rs. 5, 60,000/- SPP= 3.5 years

  12. Suggestion 2 Convection Recuperators Flue type Recuperator Typical Recuperator

  13. Working of Recuperator

  14. Significance of Recuperator in IREL Internal temperature Exhaust temperature Calorific value of fuel oil Cost of fuel oil For drying 100 kg of slurry energy required = 100X2.09X175= 36,575 kJ Fuel required for 100 kg = 0.85 kg Cost of fuel oil =Rs. 25.50/- Assuming efficiency of 40% and thereby increasing the temperature of primary gas from 25 C to 64 C For drying 100 kg of slurry energy required = 100X2.09X136= 28,424 kJ Fuel required for 100 kg = 0.66 kg Cost of fuel oil =Rs. 19.83/- SPP = 1.63 years = 200 C =160 C = 43,000 kJ/kg = Rs. 30/kg

  15. Thankyou

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