Modeling and simulation of surface reactions and reactive flow of a nitriding process

被引:10
作者
Ozdemir, I. Bedii [1 ]
Lippmann, Nils [2 ]
机构
[1] Istanbul Tech Univ, Fac Mech Engn, TR-34437 Istanbul, Turkey
[2] Bosch Automot Diesel Syst Co Ltd, Heat Treatment & C Coating RBCD MOE9, Wuxi 214028, Jiangsu, Peoples R China
关键词
Nitriding process; CFD; Reactive flows; AMMONIA DECOMPOSITION; HETEROGENEOUS DECOMPOSITION; CATALYTIC REACTIONS; IRON NITRATION; KINETICS; HYDROGEN; DENITROGENATION; NITROGENATION; ADSORPTION; PLATINUM;
D O I
10.1016/j.surfcoat.2013.01.019
中图分类号
TB3 [工程材料学];
学科分类号
0805 ; 080502 ;
摘要
Due to wide use of ammonia in gas nitriding processes, a numerical study has been undertaken to determine the ammonia decomposition rates over an injector body which was used as a steel catalyst under conditions likely to be employed in such applications. With the extrapolation of the data available for noble surfaces, intrinsic rate data have been obtained for the process temperatures of around 520 degrees C in furnace conditions with pressures varying between -100 and 900 Pa around the atmospheric pressure. The computational setup for surface reactions and furnace flow modeling was designed to match the in-service furnace used in Bosch production plants and contained 4.6 million mesh points and results were obtained with URANS k-epsilon turbulence model. Simulations revealed spatial variations of nascent nitrogen coverages over the injector surfaces and this distribution well agreed with the experimental thickness measurements on the same injector. Furthermore results indicated that the time scale defined by means of local average velocities was not the most relevant parameter to describe the advance of the surface reactions. Hence, the definition of time scale needed to be modified to include the scale of the fluctuation velocity of the turbulent transport in the vicinity of the wall and the local length scale associated with the surface. Such a time scale was shown to imitate the reactivity on the surface very well. It was also clear that when the velocities around the parts in the furnace were set high, flow separated and vortices were formed at both ends of the injectors, which blocked and further destabilized the flow inside the injector passages. (c) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:151 / 162
页数:12
相关论文
共 31 条
[11]  
Kee R.J., 2005, Chemically Reacting Flow: Theory and Practice
[12]   Studies of the Kinetics of Ammonia Decomposition on Promoted Nanocrystalline Iron Using Gas Phases of Different Nitriding Degree [J].
Kielbasa, Karolina ;
Pelka, Rafal ;
Arabczyk, Walerian .
JOURNAL OF PHYSICAL CHEMISTRY A, 2010, 114 (13) :4531-4534
[13]  
Knerr C.H., 1991, ASM HDB VOL 4, V4, P387
[14]  
Launder B. E., 1974, Computer Methods in Applied Mechanics and Engineering, V3, P269, DOI 10.1016/0045-7825(74)90029-2
[15]   Study of the Kinetics of Ammonia Synthesis and Decomposition on Iron and Cobalt Catalysts [J].
Lendzion-Bielun, Z. ;
Pelka, R. ;
Arabczyk, W. .
CATALYSIS LETTERS, 2009, 129 (1-2) :119-123
[16]   KINETICS OF NH3 DECOMPOSITION ON POLYCRYSTALLINE PT1 [J].
LOFFLER, DG ;
SCHMIDT, LD .
JOURNAL OF CATALYSIS, 1976, 41 (03) :440-454
[17]   Kinetics of catalytic reactions with two types of sites: nonuniform surfaces [J].
Murzin, DY .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (08) :1299-1306
[18]   KINETICS OF AMMONIA DECOMPOSITION ON VANADIUM NITRIDE [J].
OYAMA, ST .
JOURNAL OF CATALYSIS, 1992, 133 (02) :358-369
[19]   Studies of the Kinetics of Reaction Between Iron Catalysts and Ammonia-Nitriding of Nanocrystalline Iron with Parallel Catalytic Ammonia Decomposition [J].
Pelka, R. ;
Arabczyk, W. .
TOPICS IN CATALYSIS, 2009, 52 (11) :1506-1516
[20]   Catalytic Ammonia Decomposition Over Fe/Fe4N [J].
Pelka, R. ;
Moszynska, I. ;
Arabczyk, W. .
CATALYSIS LETTERS, 2009, 128 (1-2) :72-76