Application & Process List
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- Hardness on the surface
- Wear resistance
- Strain resistance
- Absence of intergranular oxidation
- Superficial surface fixing by chemical reaction of the carburizing element
- Inward diffusion
- Superficial hardening of the parts using martensitic quenching
- Increased compressive residual stresses
In low pressure, the efficiency of introducing nitrogen in the materials is proved when ammonia is introduced into the combustion chamber during certain stages of intermediate and final diffusion.
The NH3 partial pressure is the same when carburizing. The number and length of carbonitriding steps depend on the depth and the concentration of nitrogen desired under the surface. The process temperature can reach 960°C and is much higher than atmosphericarbonitriding. This allows deep diffusion of nitrogen – up to 1 mm – and nitrogen levels on the surface of up to 0.6%, with much shorter time cycles.
The gases produced by cracking are burned downstream of the pumping unit in order to meet environmental standards. CNBP offers undeniable resistance gains to gearing strain.
It has been demonstrated that, in the case of transmission pinions, the combination of CNBP and staged gas quenching during the martensitic phase 180°C-200°C-STOP-QUENCH- produced strain resistance gains of about 30%, as shown by the Woelher curves regarding low pressure carburizing followed by direct gas quenching.
This method is very promising for future development of high torque transmissions.
Gas direction is variable – either from top to bottom or bottom to top – thanks to an ingeniousystem of f lateral shells moving with a set of 2 cylinders in 1 second. The advantage of this alternating flow is to offer the possibility to reduce the thermal gradients between the top and bottom of the load, and therefore, improving the hardness tolerance and distortion. The programming of this alternating flow is specific to each recipe.
The load is cooled from top to bottom. It is carried out by using two water/gas heat exchangers located on each side of the load. The water and temperature flow process the cooling power of exchangers and thus the cooling rate of the load.
The nitrogen gas flow is performed by two 130 KWatts axial turbines, located above the load, in the upper part of the cell. The turbine concept is crucial to optimize the gas velocity and the power of the engines.
The quenching speed during quenching can be modulated and adjusted by changing the turbine speed quench pressure.
Over time, improvements were made in chamber design to even cell cooling: turbine blades, grid flow distribution, supply and exchanger surfaces etc.
Two Versions Exists:
- Cold oil version: area of work: 60 to 100°C
- Hot oil version: area of work: 110 to 180°C
This cell works under vacuum or under partial nitrogen pressure, thus ensuring the absence of oxidation on the surface of the low pressure carburized parts.
It has an internal lift and two level positioning: Quenching and dewatering / loading unloading.
The e oil, vigorously stirred by two immersed hydraulic brewers, can handle large loads thus limiting calefaction phenomena. The layout of these brewers is different depending on the tray version.
The oil speed can vary and can reach 1,3m/sec
The oil cooling is ensured by a continuous water/oil or air/oil exchanger group depending on the operating temperature. Installation of the quench tank requires the construction of a waterproof and airtight tank.
Optional, if the parts are to undergo intermediate machining before the oil quenching, accelerated load cooling with 1 bar nitrogen can be achieved with a turbine located in the upper part of the quenching tank. The nitrogen is cooled using an internal water/gas heat exchanger.