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COMPRESSED AIR DRYING
UNEXPECTED WAYS
IN ENERGY SAVINGS
SPECIFIC ENERGY FOR COMPRESSED AIR
0,100
0,110
0,120
0,130
0,140
0,150
0,160
0,170
0,180
18 39 63 76 100
kWh/m³
Compressor’s load in %
GA55 VSD IFD
SPECIFIC ENERGY FOR COMPRESSED AIR
0,100
0,110
0,120
0,130
0,140
0,150
0,160
0,170
0,180
18 39 63 76 100%
kWh/m³
18% load
Air flow [m³/h] 94
Specific energy for compr. air
[kWh/m³]
0.173
Total power consumption [kW] 16.3 kW
SPECIFIC ENERGY FOR COMPRESSED AIR
0,100
0,110
0,120
0,130
0,140
0,150
0,160
0,170
0,180
18 39 63 76 100%
kWh/m³
63% load
Air flow [m³/h] 381
Specific energy for compr. air
[kWh/m³]
0.114
Total power consumption [kW] 43.4 kW
SPECIFIC ENERGY FOR COMPRESSED AIR
18% load 63% load
Differenc
e
Air flow [m³/h] 94 381 287
Specific energy for compr. air
[kWh/m³]
0.173 0.114 0,095
Total power consumption [kW] 16.3 kW 43.4 kW 27.1 kW
LOWER SPECIFIC ENERGY through ADDITIONAL compressed air
equipment!
MAXIMIZING COMPRESSOR’S LOAD
REDUCES
SPECIFIC ENERGY COSTS
OF COMPRESSED AIR
FACT 1
STANDARD COMPRESSED AIR DRYER
0
50
100%
Heating
Compressed Air
80°C 180°CEnergy requirement at:
2-CIRCUIT COMPRESSED AIR DRYER
0
50
100%
Heating
Compressed Air
80°C 180°CEnergy requirement at:
2-CIRCUITS COMPRESSED AIR DRYER
0
50
100%
Heating
Compressed Air
Standard Two-circuits
80°C
80°C
180°C
180°C
Energy requirement:
ONLY POSSIBLE THROUGH PATENTED CARD-SYSTEM
CARD M CARD L
THE MAJOR TASK OF DRYING IS TO HEAT-UP!
2-CIRCUIT SYSTEM
DRASTICALLY REDUCES
ENERGY COSTS
OF COMPRESSED AIR DRYING
FACT 2
METHODS OF ENERGY RECOVERY
High-level
placement of CARD
reduces
energy costs
up to 10%
METHODS OF ENERGY RECOVERY
0
50
100%
Heating
Compressed Air
20°C 35°CSecondary air inlet temperature:
ENERGY CONSUMPTION OF
A DRYING PROCESS
WITH 80°C
METHODS OF ENERGY RECOVERY
Heat recovery from plant’s energy resources
METHODS OF ENERGY RECOVERY
Heat recovery
from integrated
air compressor
CARD R
METHODS OF ENERGY RECOVERY
0
50
100%
Heating
Compressed Air
w/o withHeat recovery:
ENERGY CONSUMPTION OF
A DRYING PROCESS
WITH 80°C
METHODS OF ENERGY RECOVERY
Heat and air recovery on blow-molding applications
METHODS OF ENERGY RECOVERY
0
50
100%
Heating
Compressed Air
w/o withAir and heat recovery:
ENERGY CONSUMPTION OF
A DRYING PROCESS
WITH 80°C
0
50
100%
36%
22%
Standard Two-circuits High-level Heat recovery
Heat & air
recovery
METHODS OF ENERGY RECOVERY
100
%
38%
0,1%
CARD (2-CIRCUIT-SYSTEM)
ENABLES UNIQUE WAYS
OF ENERGY RECOVERY
TO LOWER
ENERGY REQUIREMENTS
FACT 3
0
25
50
75
100
Desiccant dryer
new
Desiccant dryer
20% less efficiency
CARD
2-circuits
CARD
high-level
CARD
heat recovery
%
ANALOGY TO COMMON DRYING SYSTEMS
TOTAL ENERGY CONSUMPTION
ANALOGY TO COMMON DRYING SYSTEMS
ENERGY REQUIREMENT FOR DRY AIR ON DESICCANT SYSTEM
23.2 kW for 1000kg air = 0.028 kW/m³
36.0 kW for 1000kg air = 0.043 kW/m³
Density of air: 1,2041 kg/m³
ENERGY REQUIREMENT FOR COMPRESSED AIR
0.110 kW/m³
0.150 kW/m³
0,100
0,120
0,140
0,160
0,180
kWh/m³
ANALOGY TO COMMON DRYING SYSTEMS
225L DRYING HOPPER
Desic. Dry.
new
Desic. Dry.
20%
CARD
2-circuit
CARD
High-level
CARD
Recovery
Energy for dry air 2.0 kW 2.4 kW 2.0 kW 2.0 kW 2.0 kW
Energy to heat-up material 1.5 kW 1.5 kW 1.5 kW 1.1kW 0.0 kW
Total 3.5 kW 3.9 kW 3.5 kW 3.1 kW 2.0 kW
ADVANTAGES ON CARD(2-CIRCUITS)-SYSTEM
 THE LONGER THE OPERATING TIME THE
HIGHER THE ENERGY SAVINGS
 NO MAINTENANCE COSTS
 CONSTANT DRYING EFFICIENCY FOR FULL
LIFE-TIME
DRYING WITH
COMPRESSED AIR
IS NOT EXPENSIVE!
FACT 4
THANK YOU!

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2015 11-19-card unexpected-wies_farragtech

  • 1. COMPRESSED AIR DRYING UNEXPECTED WAYS IN ENERGY SAVINGS
  • 2. SPECIFIC ENERGY FOR COMPRESSED AIR 0,100 0,110 0,120 0,130 0,140 0,150 0,160 0,170 0,180 18 39 63 76 100 kWh/m³ Compressor’s load in % GA55 VSD IFD
  • 3. SPECIFIC ENERGY FOR COMPRESSED AIR 0,100 0,110 0,120 0,130 0,140 0,150 0,160 0,170 0,180 18 39 63 76 100% kWh/m³ 18% load Air flow [m³/h] 94 Specific energy for compr. air [kWh/m³] 0.173 Total power consumption [kW] 16.3 kW
  • 4. SPECIFIC ENERGY FOR COMPRESSED AIR 0,100 0,110 0,120 0,130 0,140 0,150 0,160 0,170 0,180 18 39 63 76 100% kWh/m³ 63% load Air flow [m³/h] 381 Specific energy for compr. air [kWh/m³] 0.114 Total power consumption [kW] 43.4 kW
  • 5. SPECIFIC ENERGY FOR COMPRESSED AIR 18% load 63% load Differenc e Air flow [m³/h] 94 381 287 Specific energy for compr. air [kWh/m³] 0.173 0.114 0,095 Total power consumption [kW] 16.3 kW 43.4 kW 27.1 kW LOWER SPECIFIC ENERGY through ADDITIONAL compressed air equipment!
  • 6. MAXIMIZING COMPRESSOR’S LOAD REDUCES SPECIFIC ENERGY COSTS OF COMPRESSED AIR FACT 1
  • 7. STANDARD COMPRESSED AIR DRYER 0 50 100% Heating Compressed Air 80°C 180°CEnergy requirement at:
  • 8. 2-CIRCUIT COMPRESSED AIR DRYER 0 50 100% Heating Compressed Air 80°C 180°CEnergy requirement at:
  • 9. 2-CIRCUITS COMPRESSED AIR DRYER 0 50 100% Heating Compressed Air Standard Two-circuits 80°C 80°C 180°C 180°C Energy requirement:
  • 10. ONLY POSSIBLE THROUGH PATENTED CARD-SYSTEM CARD M CARD L
  • 11. THE MAJOR TASK OF DRYING IS TO HEAT-UP!
  • 12. 2-CIRCUIT SYSTEM DRASTICALLY REDUCES ENERGY COSTS OF COMPRESSED AIR DRYING FACT 2
  • 13. METHODS OF ENERGY RECOVERY High-level placement of CARD reduces energy costs up to 10%
  • 14. METHODS OF ENERGY RECOVERY 0 50 100% Heating Compressed Air 20°C 35°CSecondary air inlet temperature: ENERGY CONSUMPTION OF A DRYING PROCESS WITH 80°C
  • 15. METHODS OF ENERGY RECOVERY Heat recovery from plant’s energy resources
  • 16. METHODS OF ENERGY RECOVERY Heat recovery from integrated air compressor CARD R
  • 17. METHODS OF ENERGY RECOVERY 0 50 100% Heating Compressed Air w/o withHeat recovery: ENERGY CONSUMPTION OF A DRYING PROCESS WITH 80°C
  • 18. METHODS OF ENERGY RECOVERY Heat and air recovery on blow-molding applications
  • 19. METHODS OF ENERGY RECOVERY 0 50 100% Heating Compressed Air w/o withAir and heat recovery: ENERGY CONSUMPTION OF A DRYING PROCESS WITH 80°C
  • 20. 0 50 100% 36% 22% Standard Two-circuits High-level Heat recovery Heat & air recovery METHODS OF ENERGY RECOVERY 100 % 38% 0,1%
  • 21. CARD (2-CIRCUIT-SYSTEM) ENABLES UNIQUE WAYS OF ENERGY RECOVERY TO LOWER ENERGY REQUIREMENTS FACT 3
  • 22. 0 25 50 75 100 Desiccant dryer new Desiccant dryer 20% less efficiency CARD 2-circuits CARD high-level CARD heat recovery % ANALOGY TO COMMON DRYING SYSTEMS TOTAL ENERGY CONSUMPTION
  • 23. ANALOGY TO COMMON DRYING SYSTEMS ENERGY REQUIREMENT FOR DRY AIR ON DESICCANT SYSTEM 23.2 kW for 1000kg air = 0.028 kW/m³ 36.0 kW for 1000kg air = 0.043 kW/m³ Density of air: 1,2041 kg/m³ ENERGY REQUIREMENT FOR COMPRESSED AIR 0.110 kW/m³ 0.150 kW/m³ 0,100 0,120 0,140 0,160 0,180 kWh/m³
  • 24. ANALOGY TO COMMON DRYING SYSTEMS 225L DRYING HOPPER Desic. Dry. new Desic. Dry. 20% CARD 2-circuit CARD High-level CARD Recovery Energy for dry air 2.0 kW 2.4 kW 2.0 kW 2.0 kW 2.0 kW Energy to heat-up material 1.5 kW 1.5 kW 1.5 kW 1.1kW 0.0 kW Total 3.5 kW 3.9 kW 3.5 kW 3.1 kW 2.0 kW
  • 25. ADVANTAGES ON CARD(2-CIRCUITS)-SYSTEM  THE LONGER THE OPERATING TIME THE HIGHER THE ENERGY SAVINGS  NO MAINTENANCE COSTS  CONSTANT DRYING EFFICIENCY FOR FULL LIFE-TIME
  • 26. DRYING WITH COMPRESSED AIR IS NOT EXPENSIVE! FACT 4