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ADVANTAGES OF FINE
CARBURISING PROCESS
 Reduction of gas consumption
Reduction of Carburising time (for FC-
35-ACM)
Equalising of carburised depth between
pitch circle diameter and tooth root of a
gear
No gas generator required
FC-35
 Produces high quality carburisation
 Shortens the carburising time and increases the
productivity (estimated over 20% more productivity than
endothermic gas method)
 A Gas generator is not required
 The cost of atmosphere gas in the Continuous Furnace is
approximately one sixth of the endothermic gas method
and in the Batch Furnace, this figure is one eleventh.
 This process is effective in prevention of environmental
contamination in the Continuous Furnace because of
minimal exhaust gas generation (approximately 1/100 of
endothermic gas method and in the Batch Furnace, this
figure is 1/23.
 Shortens the seasoning time in a Batch Furnace.
 Less than half in the case of Batch Furnace as compared
to an Endothermic method.
FC-35-ACM
 Adding to the features of FC-35 the
productivity is further increased by
approximately 10% over the FC-35
method.
 Inhibits sooting in high carbon
potential carburising
FC-30
 Obtains the same quality as endothermic gas
method.
 The carburising time is same as in the
endothermic gas method
 The cost of atmosphere gas is approximately
one ninth of the endothermic gas method
 This process is effective in prevention of
environmental contamination in the Continuous
Furnace because of minimal exhaust gas
generation (approximately 1/100 of endothermic
gas method and in the Batch Furnace, this
figure is 1/23.
CONSTRUCTION OF A CONTINUOUS GAS CARBURISING
FURNACE
10111213 3459 12678
Degreas
ing
Furnace
Entrance
Chamber
Preheatin
g Zone
Carburisin
g
Diffusion
Zone
Turn
Position
Exit
conveyor
Quench Tank
Hardenin
g 2
Hardenin
g 1
ACM
PROCES
S
COMPARISION OF OPERATING CONDITIONS OF FC-35-ACM
AND ENDOGAS
Proces
s
Method
Process
Parameter
Preheatin
g 1
Preheatin
g 2
Carburising Diffusio
n
Turn
positio
n
Hardenin
g 1
Hardening
2
Endo
Gas
Temperat
ure
890 920 940 940 940 1 2
Carbon
Potential
- - 1.15 1.05 - - 0.80
FC-
35-
ACM
Tempera
Ture
930 930 940 940 940 830 850
Carbon
Potential
- - 1.25/
0.95
1.25/
0.95
- - 0.75
Cycle Time
Endogas – 70 min
FC-35-ACM – 45
min
Carburising Specifications
Material : SCM 420
Surface hrdness : Hv (10 kg) 730 over
E.C.D : 1.50 ~ 2.05 mm (at Hv (300g) 513)
Core hardness : Hv (1 kg) 300-500
OXYGEN PROBE CARBON POTENTIALATMOSPHERE
CONTROL SYSTEM
Endothermic
gas
Or Air or CO2
Oxygen Probe
FURNACE
Pv
0.90
Sv
0.90
mV-CP
converter
CP
Controller
Control Valve
Gas Line
Signal Line
Enrichmen
t Gas
ATMOSPHERE GAS COST COMPARISION
(INDIA)
210
170
320
0
180
0
0
0
180
0
15
0
0 200 400 600
POWER
LPG
(FURNACE)
LPG
(GENERATOR)
CO2
Typeofprocessgas
Running cost (Rs/ charge) 6 hours cycle
ENDOGAS FC-20 FC-35
Power – Rs.3.70 / KWH
LPG – Rs.55.27 / m3
CO3 – Rs.30.64 / m3
COMPARISION OF FC METHOD WITH ENDOTHERMIC GAS METHOD
CHARACTERST
IC
FC-20 FC-35 FC-35-ACM
SAVING GAS EXCELLENT GOOD GOOD
QUALITY SAME AS ENDO GOOD EXCELLENT
PRODUCITVITY SAME AS ENDO GOOD EXCELLENT
GOOD MEANS BETTER THAN ENDO
EXCEELENT MEANS MUCH BETTER THAN ENDO
ATMOSPHERE GAS COST COMPARISION (JAPAN)
0
100
200
300
400
500
600
700
800
FC 35 FC 20 ENDO
Atmosphere Gas Consumption (Continuous Furnace - 30 min cycle time)
Endo LPG Endo heat Enrich heat CO2
ATMOSPHERE GAS COST COMPARISION
(JAPAN)
0
50
100
150
200
250
300
FC 35 FC 20 ENDO
Atmosphere Gas Consumption - Batch Type Furnace - 6 hours cycle
time)
x1000Yen/year
Endo LPG Endo heat Enrich heat CO2
VARIATION OF FC-35 –ACM AND ENDO GAS
0
100
200
300
400
500
600
700
800
0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8 2 2.2
FC-35-ACM (45 MIN)
ENDO (70 MIN)
FC-35ACM AND FC-35
1. FC-35-ACM
930 Deg.c. x 6 hour – 830 Deg.c. x 0 min – 130 Deg.C. Mar quench
2. FC-35
930 Deg.C. x 6 hour – 850 Deg.C. x 0 min – 130 CM.Q
130 Dg.c. Mar Quench
Oxygen Probe : 1160 mV
3. Analysis method
Analysis of the carbon content is made by an emission spectro
analysis
FC-35-ACM
FC-35
1.1
1.0
0.9
0.8
0.7
0.6
0.5
0.4
0.3
0.2.
0.1
0
1.1 1.1 1.1 1.1
4. FC & FC-35-AC- CARBON CONTENT Rate %
Distance from surface (mm)
DISTANCE FROM SURFACE
CONVENTIONAL
ACM
ACM : AMPLITUDE CARBURISING METHOD
CP 1
CP 2
CONVENTIONAL MEHTOD
CP 2
CP 3
CP 1
CP 2
CP 3
ACM

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Fine Carb Advantages R2

  • 1. ADVANTAGES OF FINE CARBURISING PROCESS  Reduction of gas consumption Reduction of Carburising time (for FC- 35-ACM) Equalising of carburised depth between pitch circle diameter and tooth root of a gear No gas generator required
  • 2. FC-35  Produces high quality carburisation  Shortens the carburising time and increases the productivity (estimated over 20% more productivity than endothermic gas method)  A Gas generator is not required  The cost of atmosphere gas in the Continuous Furnace is approximately one sixth of the endothermic gas method and in the Batch Furnace, this figure is one eleventh.  This process is effective in prevention of environmental contamination in the Continuous Furnace because of minimal exhaust gas generation (approximately 1/100 of endothermic gas method and in the Batch Furnace, this figure is 1/23.  Shortens the seasoning time in a Batch Furnace.  Less than half in the case of Batch Furnace as compared to an Endothermic method.
  • 3. FC-35-ACM  Adding to the features of FC-35 the productivity is further increased by approximately 10% over the FC-35 method.  Inhibits sooting in high carbon potential carburising
  • 4. FC-30  Obtains the same quality as endothermic gas method.  The carburising time is same as in the endothermic gas method  The cost of atmosphere gas is approximately one ninth of the endothermic gas method  This process is effective in prevention of environmental contamination in the Continuous Furnace because of minimal exhaust gas generation (approximately 1/100 of endothermic gas method and in the Batch Furnace, this figure is 1/23.
  • 5. CONSTRUCTION OF A CONTINUOUS GAS CARBURISING FURNACE 10111213 3459 12678 Degreas ing Furnace Entrance Chamber Preheatin g Zone Carburisin g Diffusion Zone Turn Position Exit conveyor Quench Tank Hardenin g 2 Hardenin g 1 ACM PROCES S
  • 6. COMPARISION OF OPERATING CONDITIONS OF FC-35-ACM AND ENDOGAS Proces s Method Process Parameter Preheatin g 1 Preheatin g 2 Carburising Diffusio n Turn positio n Hardenin g 1 Hardening 2 Endo Gas Temperat ure 890 920 940 940 940 1 2 Carbon Potential - - 1.15 1.05 - - 0.80 FC- 35- ACM Tempera Ture 930 930 940 940 940 830 850 Carbon Potential - - 1.25/ 0.95 1.25/ 0.95 - - 0.75 Cycle Time Endogas – 70 min FC-35-ACM – 45 min Carburising Specifications Material : SCM 420 Surface hrdness : Hv (10 kg) 730 over E.C.D : 1.50 ~ 2.05 mm (at Hv (300g) 513) Core hardness : Hv (1 kg) 300-500
  • 7. OXYGEN PROBE CARBON POTENTIALATMOSPHERE CONTROL SYSTEM Endothermic gas Or Air or CO2 Oxygen Probe FURNACE Pv 0.90 Sv 0.90 mV-CP converter CP Controller Control Valve Gas Line Signal Line Enrichmen t Gas
  • 8. ATMOSPHERE GAS COST COMPARISION (INDIA) 210 170 320 0 180 0 0 0 180 0 15 0 0 200 400 600 POWER LPG (FURNACE) LPG (GENERATOR) CO2 Typeofprocessgas Running cost (Rs/ charge) 6 hours cycle ENDOGAS FC-20 FC-35 Power – Rs.3.70 / KWH LPG – Rs.55.27 / m3 CO3 – Rs.30.64 / m3
  • 9. COMPARISION OF FC METHOD WITH ENDOTHERMIC GAS METHOD CHARACTERST IC FC-20 FC-35 FC-35-ACM SAVING GAS EXCELLENT GOOD GOOD QUALITY SAME AS ENDO GOOD EXCELLENT PRODUCITVITY SAME AS ENDO GOOD EXCELLENT GOOD MEANS BETTER THAN ENDO EXCEELENT MEANS MUCH BETTER THAN ENDO
  • 10. ATMOSPHERE GAS COST COMPARISION (JAPAN) 0 100 200 300 400 500 600 700 800 FC 35 FC 20 ENDO Atmosphere Gas Consumption (Continuous Furnace - 30 min cycle time) Endo LPG Endo heat Enrich heat CO2
  • 11. ATMOSPHERE GAS COST COMPARISION (JAPAN) 0 50 100 150 200 250 300 FC 35 FC 20 ENDO Atmosphere Gas Consumption - Batch Type Furnace - 6 hours cycle time) x1000Yen/year Endo LPG Endo heat Enrich heat CO2
  • 12. VARIATION OF FC-35 –ACM AND ENDO GAS 0 100 200 300 400 500 600 700 800 0.2 0.4 0.6 0.8 1 1.2 1.4 1.6 1.8 2 2.2 FC-35-ACM (45 MIN) ENDO (70 MIN)
  • 13. FC-35ACM AND FC-35 1. FC-35-ACM 930 Deg.c. x 6 hour – 830 Deg.c. x 0 min – 130 Deg.C. Mar quench 2. FC-35 930 Deg.C. x 6 hour – 850 Deg.C. x 0 min – 130 CM.Q 130 Dg.c. Mar Quench Oxygen Probe : 1160 mV 3. Analysis method Analysis of the carbon content is made by an emission spectro analysis
  • 14. FC-35-ACM FC-35 1.1 1.0 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2. 0.1 0 1.1 1.1 1.1 1.1 4. FC & FC-35-AC- CARBON CONTENT Rate % Distance from surface (mm)
  • 16. ACM : AMPLITUDE CARBURISING METHOD CP 1 CP 2 CONVENTIONAL MEHTOD CP 2 CP 3 CP 1 CP 2 CP 3 ACM