Please wait a minute...
Chin. Phys. B, 2021, Vol. 30(5): 054702    DOI: 10.1088/1674-1056/abd75e
ELECTROMAGNETISM, OPTICS, ACOUSTICS, HEAT TRANSFER, CLASSICAL MECHANICS, AND FLUID DYNAMICS Prev   Next  

Impact mechanism of gas temperature in metal powder production via gas atomization

Peng Wang(汪鹏)1,2, Jing Li(李静)1,2,‡, Xin Wang(王欣)1,2, Bo-Rui Du(杜博睿)1,2, Shi-Yuan Shen(申世远)1,2, Xue-Yuan Ge(葛学元)1,2,§, and Miao-Hui Wang(王淼辉)1,2,†
1 State Key Laboratory of Advanced Forming Technology and Equipment, China Academy of Machinery Science & Technology, Beijing 100083, China;
2 Beijing National Innovation Institute of Lightweight Ltd, Beijing 100083, China
Abstract  This paper aims at studying the influence mechanism of gas temperatures (300 K, 400 K, 500 K, and 600 K) on gas atomization by simulating the integral atomization process of the close-coupled nozzle in vacuum induction gas atomization (VIGA). The primary atomization is simulated by the volume of fluid (VOF) approach, and the second atomization is studied by the discrete phase model (DPM) combined with the instability breakage model. The results show that, at an increased gas temperature, the influences of gas-liquid contact angle and gas temperature in the recirculation zone on the primary atomization are virtually negligible. However, increasing the gas temperature will increase the gas-liquid relative velocity near the recirculation zone and decrease the melt film thickness, which are the main reasons for the reduced mass median diameter (MMD, d50) of primary atomized droplets. During the secondary atomization, increasing the gas temperature from 300 K to 600 K results in an increase in the droplet dispersion angle, which is beneficial to the formation of spherical metal powder. In addition, increasing the gas temperature, the positive effect of gas-liquid relative velocity increase on droplets refinement overweighs the negative influence of the GMR decrease, resulting in the reduced MMD and diameter distribution interval. From the analysis of the atomization mechanism, the increase in atomization efficiency caused by increasing the temperature of the atomizing gas, including primary atomization and secondary atomization, is mainly due to the increase in the gas drag force difference between the inner and outer sides of the annular liquid film.
Keywords:  metallic powders      VIGA technology      argon temperature      two-phase flow  
Received:  22 October 2020      Revised:  24 December 2020      Accepted manuscript online:  30 December 2020
PACS:  47.45.Ab (Kinetic theory of gases)  
  75.47.Np (Metals and alloys)  
  81.20.Ev (Powder processing: powder metallurgy, compaction, sintering, mechanical alloying, and granulation)  
  47.55.df (Breakup and coalescence)  
Fund: Project supported by the Open Fund of State Key Laboratory of Advanced Forming Technology and Equipment (Grant No. SKL2019006) and the National Natural Science Foundation of China (Grant No. 51975240).
Corresponding Authors:  Miao-Hui Wang, Jing Li, Xue-Yuan Ge     E-mail:  wangmh@camtc.com.cn;lijing2012@buaa.edu.cn;gexueyuan@163.com

Cite this article: 

Peng Wang(汪鹏), Jing Li(李静), Xin Wang(王欣), Bo-Rui Du(杜博睿), Shi-Yuan Shen(申世远), Xue-Yuan Ge(葛学元), and Miao-Hui Wang(王淼辉) Impact mechanism of gas temperature in metal powder production via gas atomization 2021 Chin. Phys. B 30 054702

[1] Beckers D, Ellendt N, Fritsching U and Uhlenwinkel V 2020 Adv. Powder Technol. 31 300
[2] DebRoy T, Wei H, Zuback J, Mukherjee T, Elmer J, Milewski J, Beese A M, Wilson-Heid A D, De A and Zhang W 2018 Prog. Mater. Sci. 92 112
[3] Thompson J S, Hassan O, Rolland S and Sienz J 2016 Powder Technol. 291 75
[4] Tang J, Nie Y, Lei Q and Li Y 2019 Adv. Powder Technol. 30 2330
[5] Baskoro A S, Supriadi S, Dharmanto, Anis M and Munir B 2019 Matec Web of Conferences 269
[6] Li X G and Fritsching U 2017 J. Mater. Process. Technol. 239 1
[7] Henein H, Uhlenwinkel V and Fritsching U 2017 Metal sprays and spray deposition (Cham: Springer) pp. 1-563
[8] Mullis A, McCarthy I and Cochrane R 2011 J. Mater. Process. Technol. 211 1471
[9] Motaman S, Mullis A M, Cochrane R F and Borman D J 2015 Metallurgical and Materials Transactions B 46 1990
[10] Si C R, Zhang X J, Wang J B and Li Y J 2014 International Journal of Minerals, Metallurgy, and Materials 21 627
[11] Zeoli N 2011 Multiphase modelling of the characteristics of close coupled gas atomization (Birmingham: Aston University)
[12] Arachchilage K H, Haghshenas M, Park S, Zhou L, Sohn Y, McWilliams B, Cho K and Kumar R 2019 Adv. Powder Technol. 30 2726
[13] Zhang M and Zhang Z 2020 Mater. Today Commun. 25 101423
[14] Wei M, Chen S, Sun M, Liang J and Wang M 2020 Powder Technol. 367 724
[15] Motaman S, Mullis A M, Cochrane R F, McCarthy I N and Borman D J 2013 Computers & Fluids 88 1
[16] Zeoli N, Tabbara H and Gu S 2011 Chem. Eng. Sci. 66 6498
[17] Kaiser R, Li C, Yang S and Lee D 2018 Adv. Powder Technol. 29 623
[18] Zeoli N, Tabbara H and Gu S 2012 Appl. Phys. A 108 783
[19] Mi J, Figliola R S and Anderson I E 1996 Mater. Sci. Eng. A 208 20
[20] Markus S, Fritsching U and Bauckhage K 2002 Mater. Sci. Eng. A 326 122
[21] Wang P, Li J, Wang X, Liu H S, Fan B, Gan P, Guo R F, Ge X Y and Wang M H 2020 Chin. Phys. B 30 027502
[22] Ashgriz N 2011 Handbook of atomization and sprays: theory and applications (New York: Springer Science & Business Media) pp. 1-927
[23] Lagutkin S, Achelis L, Sheikhaliev S, Uhlenwinkel V and Srivastava V 2004 Materials Science and Engineering: A 383 1
[24] Fritsching U 2004 Spray simulation: Modeling and numerical simulation of sprayforming metals ((New York: Cambridge University Press) pp. 1-269
[25] Zeoli N and Gu S 2008 Comput. Mater. Sci. 43 268
[26] Zeoli N, Gu S and Kamnis S 2008 International Journal of Heat and Mass Transfer 51 4121
[27] Taylor G 1963 The scientific papers of GI Taylor 3 457
[28] Matsson J 2020 An Introduction to ANSYS Fluent 2019 (New York: SDC Publications) pp. 75-70
[29] Matsson J 2020 An Introduction to ANSYS Fluent (New York: SDC Publications) pp. 86-126
[30] Allimant A, Planche M P, Bailly Y, Dembinski L and Coddet C 2009 Powder Technol. 190 79
[31] Ting J and Anderson I E 2004 Materials Science and Engineering:A 379 264
[32] ünal A 1989 Metallurgical Transactions B 20 613
[33] Senkov O N, Senkova S V, Scott J M and Miracle D B 2005 Mater. Sci. Eng. A 393 12
[34] Lubanska H 1970 JOM 22 45
[1] Mechanism from particle compaction to fluidization of liquid-solid two-phase flow
Yue Zhang(张悦), Jinchun Song(宋锦春), Lianxi Ma(马连喜), Liancun Zheng(郑连存), Minghe Liu(刘明贺). Chin. Phys. B, 2020, 29(1): 014702.
[2] Gradient-augmented hybrid interface capturing method for incompressible two-phase flow
Zheng Fu(付峥), Shi-Yu Wu(吴士玉), Kai-Xin Liu(刘凯欣). Chin. Phys. B, 2016, 25(6): 064701.
[3] Three-dimensional multi-relaxation-time lattice Boltzmann front-tracking method for two-phase flow
Hai-Qiong Xie(谢海琼), Zhong Zeng(曾忠), Liang-Qi Zhang(张良奇). Chin. Phys. B, 2016, 25(1): 014702.
[4] Multi-scale complexity entropy causality plane: An intrinsic measure for indicating two-phase flow structures
Dou Fu-Xiang (窦富祥), Jin Ning-De (金宁德), Fan Chun-Ling (樊春玲), Gao Zhong-Ke (高忠科), Sun Bin (孙斌). Chin. Phys. B, 2014, 23(12): 120502.
[5] Markov transition probability-based network from time series for characterizing experimental two-phase flow
Gao Zhong-Ke (高忠科), Hu Li-Dan (胡沥丹), Jin Ning-De (金宁德). Chin. Phys. B, 2013, 22(5): 050507.
[6] Multi-relaxation-time lattice Boltzmann front tracking method for two-phase flow with surface tension
Xie Hai-Qiong (谢海琼), Zeng Zhong (曾忠), Zhang Liang-Qi (张良奇), Liang Gong-You (梁功有), Hiroshi Mizuseki, Yoshiyuki Kawazoe. Chin. Phys. B, 2012, 21(12): 124703.
[7] Complex network analysis in inclined oil--water two-phase flow
Gao Zhong-Ke(高忠科) and Jin Ning-De(金宁德) . Chin. Phys. B, 2009, 18(12): 5249-5258.
[8] A hybrid scheme for computing incompressible two-phase flows
Zhou Jun(周军), Cai Li(蔡力), and Zhou Feng-Qi(周凤岐). Chin. Phys. B, 2008, 17(5): 1535-1544.
No Suggested Reading articles found!