微米尺度液滴与尘粒作用后反弹行为特性研究

doi:10.11949/0438-1157.20250129

化工学报 ›› 2025, Vol. 76 ›› Issue (8): 3990-4003.DOI: 10.11949/0438-1157.20250129

微米尺度液滴与尘粒作用后反弹行为特性研究

张伟¹(), 武齐永¹, 孙华中², 胡适², 朱小龙²(), 孔帅³

^1.北京特种工程设计研究院，北京 100028
^2.中国科学技术大学，火灾安全全国重点实验室，安徽合肥 230026
^3.国网山东省电力公司电力科学研究院，山东济南 250003

收稿日期:2025-02-12 修回日期:2025-03-24 出版日期:2025-08-25 发布日期:2025-09-17
通讯作者: 朱小龙
作者简介:张伟（1976—），男，博士，高级工程师，13552985272@163.com
基金资助:
中国人民解放军某部“火灾预警及自动灭火功能的集成化UPS电池设备试验样机研制”项目;国家自然科学基金项目(52404260);国家卫生健康委粉尘危害工程防护重点实验室开放课题(KLECDH2023020102);山东省自然科学基金项目(ZR2024QE236)

Study on rebound behavior characteristics of droplets and dust particles at micron-scale

Wei ZHANG¹(), Qiyong WU¹, Huazhong SUN², Shi HU², Xiaolong ZHU²(), Shuai KONG³

^1.Beijing Special Engineering Design Institute, Beijing 100028, China
^2.State Key Laboratory of Fire Science, University of Science and Technology of China, Hefei 230026, Anhui, China
^3.State Grid Shandong Electric Power Research Institute, Jinan 250003, Shandong, China

Received:2025-02-12 Revised:2025-03-24 Online:2025-08-25 Published:2025-09-17
Contact: Xiaolong ZHU

摘要/Abstract

摘要：

细水雾除尘技术因具有环保、安全、经济等优势被广泛应用，但尘-雾碰撞时的反弹现象导致降尘效果不佳，且目前对其反弹动力学机制认识不足，缺乏理论指导。本研究针对生产性粉尘及大颗粒烟尘（直径1~125 μm），通过数值模拟分析其与相近直径雾滴碰撞时的反弹行为，并构建了考虑接触角、液滴-颗粒直径比、碰撞速度、液滴黏度、表面张力等多因素的反弹预测模型，得出了反弹临界条件。结果表明，反弹现象主要发生在液滴低速碰撞疏水颗粒时，且雾滴粒径越小，反弹临界速度越大；降低接触角可有效抑制反弹，当接触角小于90°时，反弹现象消失。本研究揭示了影响反弹行为的多重因素，可定量预测尘-雾碰撞反弹行为，为水雾降尘系统的设计优化提供理论依据。

关键词: 粉尘, 烟颗粒, 水雾降尘, 烟颗粒洗消, 固液碰撞, 微米尺度

Abstract:

This study investigates the rebound dynamics during the collision between mist droplets and particulate matter, aiming to provide theoretical guidance for particle settlement in water mist technology applications. We focused on particles ranging from 1 μm to 125 μm and used numerical simulations to analyze their rebound behavior when colliding with droplets of similar diameters. Scatter plots of collision behavior were analyzed to obtain a fitting curve for the critical rebound condition, and a physical model was constructed. The model developed in this study involves more dependent variable parameters than previous predictive equations for critical rebound conditions, comprehensively revealing the multiple factors influencing rebound behavior. The research indicates that rebound phenomena mainly occur when droplets collide with hydrophobic particles at low speeds. Smaller droplet sizes result in higher critical rebound velocities, explaining why smaller particles are more difficult to settle through water mist in dust suppression practices. Reducing the dust-mist contact angle can effectively inhibit the rebound, and the rebound phenomenon disappears when the contact angle is less than 90°. The research findings can quantitatively predict the occurrence of a rebound during a dust-mist collision, thereby guiding the optimization of water mist operating parameters in the practice of dust settlement and ultimately promoting significant improvements in dust removal efficiency. This study provides a comprehensive understanding of the rebound dynamics and offers practical guidance for enhancing the effectiveness of water mist technology in dust control applications.

Key words: dust, smoke particles, water mist dust suppression, smoke particle decontamination, solid-liquid collision, micron-scale

中图分类号:

X 964

张伟, 武齐永, 孙华中, 胡适, 朱小龙, 孔帅. 微米尺度液滴与尘粒作用后反弹行为特性研究[J]. 化工学报, 2025, 76(8): 3990-4003.

Wei ZHANG, Qiyong WU, Huazhong SUN, Shi HU, Xiaolong ZHU, Shuai KONG. Study on rebound behavior characteristics of droplets and dust particles at micron-scale[J]. CIESC Journal, 2025, 76(8): 3990-4003.

图/表 20

图1 传统水雾降尘机理示意图

Fig.1 Schematic diagram of traditional water mist dust removal mechanism

表1 不同雾化方法产生的雾场特性典型参数

Table 1 Typical parameters of fog field characteristics generated by different atomization methods

雾化方法	水压/MPa	气压/ MPa	索特尔平均粒径/μm	射程/m	速度/ (m·s^-1)
单相高压雾化^[11-12]	6~10	无	30~80	< 3	12~30
两相雾化^[7,13-15]	< 0.5	< 0.6	< 30	< 1	< 10
超声雾化^[16-17]	< 0.5	< 0.5	< 30	1.5~2	4~11
超音速气流雾化^[9]	< 0.5	< 0.5	5~20	4.9~7	< 600

表2 不同理化特性改善方法处理后雾滴的表面张力

Table 2 Surface tension of fog droplets treated with different physicochemical properties improvement methods

液滴理化特性改善方法	表面张力/(mN·m^-1)
磁化水^[18]	69~72
多组分水雾^[19-20]	29~40
磁化+多组分水雾^[21]	26~32
荷电水雾^[18]	12~20

表3 不同类型液体与固体的湿润特性

Table 3 Wetting characteristics of different types of liquids and solids

固体类型	液体类型	接触角	液体表面张力σ/(mN·m^-1)	液体黏度μ/(mPa·s)	来源
ST1：聚硅烷处理的二氧化硅（高度疏水）	蒸馏水	α = 168.4°，β = 91.4°	72.3	1.04	实测
ST1：聚硅烷处理的二氧化硅（高度疏水）	浓度为1 mmol·L^-1的CTAB溶液	α = 151.2°，β = 15.2°	34.2	1.04	实测
ST2：石墨（中度疏水）	蒸馏水	α = 90.0°，β = 23.0°	72.0	1.04	文献[25]
ST2：石墨（中度疏水）	浓度为1 mmol·L^-1的CTAB溶液	α = 62.0°，β = 17.0°	34.2	1.04	文献[25]
ST3：二氧化硅（亲水）	蒸馏水	α = 25.0°，β = 7.5°	72.0	1.04	文献[25]

图2 计算域

Fig.2 Computational domain

表4 不同颗粒尺寸对应的计算域尺寸

Table 4 Computational domain sizes corresponding to different particle sizes

颗粒直径/μm	计算域尺寸/μm
3000	21000×6600
2000	14000×4400
125	875×275
25	175×55
5	35×11
1	7×2.2
0.2	1.4×0.44

图3 不同网格尺寸条件下液滴形态对比（v0= 4.17 m·s-1，dp= 3 mm，dl = 3.93 mm，α = 168.4°，β = 91.4°）

Fig.3 Comparison of droplet morphology under different grid size conditions

图4 模拟结果与文献[29]中实验记录的液滴形态对比（dp = 2 mm）

Fig.4 Comparison between simulation results and experimental droplet morphology recorded in Ref.[29] (dp = 2 mm)

表5 研究黏度的影响时设置的条件参数

Table 5 Condition parameters set when studying the influence of viscosity

常量

变量

液滴-颗粒直径比Ω

液滴表面

张力σ/

(mN·m^-1)

接触角

液滴黏度μ/(mPa·s)

碰撞速度v₀/(m·s^-1)

颗粒直径

d_p/μm

图5 铺展和收缩过程中接触角的变化过程

Fig.5 The change process of the contact angle during spreading and shrinking

表6 研究表面张力和接触角影响时的条件参数设置

Table 6 Condition parameter settings when the effects of surface tension and contact angle are investigated

常量		变量
液滴-颗粒直径比Ω	液滴黏度μ/(mPa·s)	碰撞速度v₀/(m·s^-1)	颗粒直径d_p/μm	液滴表面张力σ/(mN·m^-1)	接触角
1.31	1.04	1~500	1, 5, 25, 125 (ST1)	72 (纯水)	α = 168.4°，β =91.4°
1.31	1.04	1~500	1, 5, 25, 125 (ST1)	34.2 (CTAB)	α =151.2°，β =15.2°

表7 研究接触角影响反弹临界条件时的条件参数设置

Table 7 The condition parameter setting is studied when the contact angle affects the rebound critical condition

常量			变量
液滴- 颗粒直径比Ω	液滴表面张力σ/(mN·m^-1)	液滴黏度μ/(mPa·s)	颗粒直径d_p/μm	碰撞速度 v₀/(m·s^-1)	接触角
1.31	72	1.04	1, 5, 25, 125	1~500	α = β = 168.4°
					α = β = 151.2°
					α = β = 120°
					α = β = 100°
					α = β = 90°
					α = β = 80°

图6 不同接触角条件下碰撞行为分布散点图——分界线拟合曲线；反弹；未反弹

Fig.6 Scatter plot of collision behavior distribution under different contact angle conditions

表8 无量纲参数解释

Table 8 Dimensionless parameter interpretation

液滴无量纲参数	参数解释
$R e = ρ l d l v l μ l$	ρ_l 为液滴密度，d_l 为液滴直径，v_l 为尘雾相对速度，μ_l 为液滴动力黏度
$O h = μ l ρ l d l σ$	μ_l 为液滴动力黏度，ρ_l 为液滴密度，d_l 为液滴直径，σ为液滴表面张力
$W e = ρ l v l 2 l σ$	ρ_l 为液滴密度，v_l 为尘雾相对速度，l为液滴特征长度（在本文中为液滴直径d_l ），σ为液滴表面张力

表8 无量纲参数解释

Table 8 Dimensionless parameter interpretation

液滴无量纲参数	参数解释
$R e = ρ l d l v l μ l$	ρ_l 为液滴密度，d_l 为液滴直径，v_l 为尘雾相对速度，μ_l 为液滴动力黏度
$O h = μ l ρ l d l σ$	μ_l 为液滴动力黏度，ρ_l 为液滴密度，d_l 为液滴直径，σ为液滴表面张力
$W e = ρ l v l 2 l σ$	ρ_l 为液滴密度，v_l 为尘雾相对速度，l为液滴特征长度（在本文中为液滴直径d_l ），σ为液滴表面张力

表9 不同接触角条件下的反弹边界条件方程

Table 9 Bounce-back boundary condition equations for different contact angles

条件编号	接触角	液滴表面张力σ/(mN·m^-1)	反弹边界条件方程
1	𝛼α = 168.4° β = 91.4°	72	5.807 = $R e c r 1.080$ Oh，R²=0.9998 0.00965 ≤ Oh ≤ 0.0483
2	𝛼α = 168.4° β = 168.4°	72	7.301 = $R e c r 1.119$ Oh，R² = 0.9987 0.00965 ≤ Oh ≤ 0.0483
3	𝛼α = 151.2° β = 151.2°	72	10.034 = $R e c r 1.189$ Oh，R² = 0.9989 0.00965 ≤ Oh ≤ 0.0483
4	𝛼α = 120.0° β = 120.0°	72	12.491 = $R e c r 1.274$ Oh，R² = 0.9962 0.00965 ≤ Oh ≤ 0.0483
5	𝛼α = 100.0° β = 100.0°	72	9.077 = $R e c r 1.238$ Oh，R² = 0.9967 0.00965 ≤ Oh ≤ 0.0483
6	𝛼α = 90.0° β = 90.0°	72	6.663= $R e c r 1.186$ Oh，R² = 0.9965 0.00965 ≤ Oh ≤ 0.0311
7	𝛼α = 80.0° β = 80.0°	72	当Oh=0.00965，Re = 219.99 当Oh ≥ 0.0193，无反弹现象

表9 不同接触角条件下的反弹边界条件方程

Table 9 Bounce-back boundary condition equations for different contact angles

条件编号	接触角	液滴表面张力σ/(mN·m^-1)	反弹边界条件方程
1	𝛼α = 168.4° β = 91.4°	72	5.807 = $R e c r 1.080$ Oh，R²=0.9998 0.00965 ≤ Oh ≤ 0.0483
2	𝛼α = 168.4° β = 168.4°	72	7.301 = $R e c r 1.119$ Oh，R² = 0.9987 0.00965 ≤ Oh ≤ 0.0483
3	𝛼α = 151.2° β = 151.2°	72	10.034 = $R e c r 1.189$ Oh，R² = 0.9989 0.00965 ≤ Oh ≤ 0.0483
4	𝛼α = 120.0° β = 120.0°	72	12.491 = $R e c r 1.274$ Oh，R² = 0.9962 0.00965 ≤ Oh ≤ 0.0483
5	𝛼α = 100.0° β = 100.0°	72	9.077 = $R e c r 1.238$ Oh，R² = 0.9967 0.00965 ≤ Oh ≤ 0.0483
6	𝛼α = 90.0° β = 90.0°	72	6.663= $R e c r 1.186$ Oh，R² = 0.9965 0.00965 ≤ Oh ≤ 0.0311
7	𝛼α = 80.0° β = 80.0°	72	当Oh=0.00965，Re = 219.99 当Oh ≥ 0.0193，无反弹现象

图7 接触角对反弹临界条件的影响α = β = 168.4°;α = β = 151.2°;α = β = 120°; α = β = 100°;α = β = 90°

Fig.7 Influence of contact angle on rebound critical condition

图8 式（3）在不同前进角下的常数值变化

Fig.8 Constant value change of equation (3) under different advance angles

图9 方程中不同角度定义示意图

Fig.9 Schematic of the definition of different angles in the equation

表10 前人研究中的Wecr 与本研究的结果对比

Table 10 Comparison of Wecr in previous studies with the results of this study

α/(°)	β/(°)	Oh	Ω	式（30）得出的We_cr	式（31）得出的We_cr	式（36）得出的We_cr	前人文献中的We_cr	来源
90	23	0.00211	0.31	128.59	115.43	62.43	63.21	文献^[23]的实验结果
90	23	0.00211	0.62	27.86	29.01	15.61	15.80
90	23	0.00211	1.24	5.65	7.37	3.90	3.95
90	23	0.00211	1.31	5.03	6.62	3.50	3.54
160	23	0.00262	2.00	5.65	2.79	2.53	< 3.96	文献^[28]的模拟结果
160	23	0.00262	1.00	24.90	11.09	10.14	9.87~30.23
160	23	0.00262	0.67	51.66	50.66	12.27	70~90
160	23	0.00262	0.50	95.29	89.83	21.82	130~150
160	23	0.00262	0.33	222.17	201.68	49.09	130~150
125	23	0.00262	2.00	7.30	4.51	1.49	< 3.96
125	23	0.00262	1.00	16.82	17.96	5.95	9.87~30.23
125	23	0.00262	0.67	40.73	40.73	4.65	70~90
125	23	0.00262	0.50	75.90	72.20	8.27	130~150
125	23	0.00262	0.33	178.60	162.06	18.60	130~150
90	23	0.00262	2.00	2.46	2.78	1.40	< 3.96
90	23	0.00262	1.00	9.17	11.07	5.60	3.96~9.87
90	23	0.00262	0.67	23.61	25.16	6.78	70~90
90	23	0.00262	0.50	45.50	44.57	12.05	130~150
90	23	0.00262	0.33	110.29	99.96	27.11	130~150

图10 不同液滴直径和黏度条件下的反弹临界速度预测值

Fig.10 Predicted values of the critical velocity of rebound for different droplet diameters and viscosities

参考文献 34

[1]	谢文博, 魏婉笛. 李珏: 职防路上我看到繁星满天[R/OL]. (2023-04-28). .
	Xie W B, Wei W D. Li Jue: I saw a starry sky on the way to work defense[R/OL]. (2023-04-28). .
[2]	袁亮. 煤矿粉尘防控与职业安全健康科学构想[J]. 煤炭学报, 2020, 45(1): 1-7.
	Yuan L. Scientific conception of coal mine dust control and occupational safety[J]. Journal of China Coal Society, 2020, 45(1): 1-7.
[3]	王运敏, 李刚, 刘建国, 等. 我国非煤矿山职业健康防控技术研究现状、挑战及展望[J]. 金属矿山, 2024(9): 1-12.
	Wang Y M, Li G, Liu J G, et al. Current status, challenges and prospects of occupational health control technology in China's non-coal mines[J]. Metal Mine, 2024(9): 1-12.
[4]	天津市消防救援总队. 已发32起!致235死, 475伤![R/OL]. (2023). .
	Tianjin Fire rescue Corps. 32 cases have been sent! 235 dead, 475 wounded![R/OL]. (2023). .
[5]	王国法, 庞义辉, 任怀伟, 等. 矿山智能化建设的挑战与思考[J]. 智能矿山, 2022, 3(10): 2-15.
	Wang G F, Pang Y H, Ren H W, et al. Challenges and thinking of mine intelligent construction[J]. Journal of Intelligent Mine, 2022, 3(10): 2-15.
[6]	马素平, 寇子明. 喷雾降尘机理的研究[J]. 煤炭学报, 2005, 30(3): 297-300.
	Ma S P, Kou Z M. Study on mechanism of reducing dust by spray[J]. Journal of China Coal Society, 2005, 30(3): 297-300.
[7]	蒋仲安, 王亚朋, 许峰. 金属矿山气-水喷头雾化特性及降尘能力实验研究[J]. 中南大学学报(自然科学版), 2020, 51(1): 184-192.
	Jiang Z A, Wang Y P, Xu F. Experimental study on atomization characteristics and dust reduction capacity of gas-water nozzles in metal mines[J]. Journal of Central South University (Science and Technology), 2020, 51(1): 184-192.
[8]	李刚, 吴超. 超声干雾抑尘机理及其技术参数优化研究[J]. 中国安全科学学报, 2015, 25(3): 108-113.
	Li G, Wu C. Research on mechanism and parameters optimization of ultrasonic atomization technique for dust removal[J]. China Safety Science Journal, 2015, 25(3): 108-113.
[9]	张天. 超音速汲水式气动雾化细观动力学特性及捕尘机理研究[D]. 阜新: 辽宁工程技术大学, 2021.
	Zhang T. Study on meso-dynamic characteristics and dust catching mechanism of supersonic pumping pneumatic atomization[D]. Fuxin: Liaoning Technical University, 2021.
[10]	金龙哲, 刘建国, 林清侠, 等. 矿山喷雾降尘技术研究与应用现状综述[J]. 金属矿山, 2023(7): 2-17.
	Jin L Z, Liu J G, Lin Q X, et al. Review on the research and application of water spray dust-reduction technology in mines[J]. Metal Mine, 2023(7): 2-17.
[11]	田畅. X型旋流压力喷嘴雾化参数及降尘效率预测模型[D]. 湘潭: 湖南科技大学, 2019.
	Tian C. Prediction model of atomization parameters and dust removal efficiency of X-type swirl pressure nozzle[D]. Xiangtan: Hunan University of Science and Technology, 2019.
[12]	徐翠翠. 喷嘴内外流场雾化特性及尘雾耦合降尘试验研究[D]. 青岛: 山东科技大学, 2018.
	Xu C C. Experimental study on atomization characteristics of flow field inside and outside nozzle and dust suppression coupled with dust and fog[D]. Qingdao: Shandong University of Science and Technology, 2018.
[13]	房雪明. 综采面气液两相喷射微细水雾降尘技术及应用[D]. 淮南: 安徽理工大学, 2022.
	Fang X M. Dust suppression technology and application of gas-liquid two-phase jet micro-water mist in fully mechanized mining face[D]. Huainan: Anhui University of Science & Technology, 2022.
[14]	宋皓然. 内混式空气雾化喷嘴结构优化与实验研究[D]. 淮南: 安徽理工大学, 2022.
	Song H R. Structure optimization and experimental study of internal mixing air atomization nozzle[D]. Huainan: Anhui University of Science & Technology, 2022.
[15]	江丙友, 张琦, 朱志辉, 等. 湿式除尘器中气水喷雾降尘效果试验研究[J]. 金属矿山, 2023(7): 82-90.
	Jiang B Y, Zhang Q, Zhu Z H, et al. Experimental study on dust reduction effect of air-water spray in wet dust collector[J]. Metal Mine, 2023(7): 82-90.
[16]	邬高高, 王鹏飞, 刘荣华, 等. 供气压力对流体型超声喷嘴雾化特性及降尘效率的影响[J]. 煤炭学报, 2021, 46(6): 1898-1906.
	Wu G G, Wang P F, Liu R H, et al. Impact of air supply pressure on the atomization characteristics and dust removal efficiency of fluid ultrasonic nozzle[J]. Journal of China Coal Society, 2021, 46(6): 1898-1906.
[17]	李刚, 吴将有, 金龙哲, 等. 我国金属矿山粉尘防治技术研究现状及展望[J]. 金属矿山, 2021(1): 154-167.
	Li G, Wu J Y, Jin L Z, et al. Study status and prospect of dust control technology for metal mines in China[J]. Metal Mine, 2021(1): 154-167.
[18]	李哲, 葛少成, 孙丽英, 等. 磁化荷电水雾最佳降尘参数确定实验研究[J]. 中国安全生产科学技术, 2022, 18(11): 77-84.
	Li Z, Ge S C, Sun L Y, et al. Experimental study on determination of optimal dust reduction parameters of magnetized charged water mist[J]. Journal of Safety Science and Technology, 2022, 18(11): 77-84.
[19]	王晓楠. 表面活性剂复配对煤尘润湿性的协同效应研究[D]. 淮南: 安徽理工大学, 2020.
	Wang X N. Study on synergistic effect of surfactant combination on coal dust wettability[D]. Huainan: Anhui University of Science & Technology, 2020.
[20]	李国春, 齐国栋, 孔帅, 等. 环保型泡沫灭火剂在变压器油表面的铺展特性研究[J]. 山东电力技术, 2024, 51(8): 67-77.
	Li G C, Qi G D, Kong S, et al. Study on the spreading characteristics of environmentally friendly foam fire extinguishing agent on transformer oil surface [J]. Shandong Electric Power Technology, 2024, 51(8): 67-77.
[21]	周群. 煤矿井下活性磁化水降尘机制及技术研究[D]. 徐州: 中国矿业大学, 2019.
	Zhou Q. Study on dust suppression mechanism and technology of active magnetized water in coal mine[D]. Xuzhou: China University of Mining and Technology, 2019.
[22]	Mitra S, Doroodchi E, Pareek V, et al. Collision behaviour of a smaller particle into a larger stationary droplet[J]. Advanced Powder Technology, 2015, 26(1): 280-295.
[23]	Malgarinos I, Nikolopoulos N, Gavaises M. A numerical study on droplet-particle collision dynamics[J]. International Journal of Heat and Fluid Flow, 2016, 61: 499-509.
[24]	韩方伟, 张金宜, 赵月, 等. 液滴在球形粉尘表面的动力润湿特性[J]. 煤炭学报, 2021, 46(8): 2614-2622.
	Han F W, Zhang J Y, Zhao Y, et al. Kinetic wetting characteristics of droplet on the surface of spherical dust[J]. Journal of China Coal Society, 2021, 46(8): 2614-2622.
[25]	Zhu X L, Wang D M, Craig V S J. Interaction of particles with surfactant thin films: implications for dust suppression[J]. Langmuir, 2019, 35(24): 7641-7649.
[26]	Li X, Dong Z Q, Wang L P, et al. A magnetic field coupling fractional step lattice Boltzmann model for the complex interfacial behavior in magnetic multiphase flows[J]. Applied Mathematical Modelling, 2023, 117: 219-250.
[27]	Li X, Dong Z Q, Li Y, et al. A fractional-step lattice Boltzmann method for multiphase flows with complex interfacial behavior and large density contrast[J]. International Journal of Multiphase Flow, 2022, 149: 103982.
[28]	Yoon I, Shin S. Direct numerical simulation of droplet collision with stationary spherical particle: a comprehensive map of outcomes[J]. International Journal of Multiphase Flow, 2021, 135: 103503.
[29]	Banitabaei S A, Amirfazli A. Droplet impact onto a solid sphere: effect of wettability and impact velocity[J]. Physics of Fluids, 2017, 29(6): 062111.
[30]	Banitabaei S A, Amirfazli A. Droplet impact onto a solid sphere in mid-air: effect of viscosity, gas density, and diameter ratio on impact outcomes[J]. Physics of Fluids, 2020, 32(3): 037102.
[31]	Pasandideh-Fard M, Chandra S, Mostaghimi J. A three-dimensional model of droplet impact and solidification[J]. International Journal of Heat and Mass Transfer, 2002, 45(11): 2229-2242.
[32]	Khojasteh D, Bordbar A, Kamali R, et al. Curvature effect on droplet impacting onto hydrophobic and superhydrophobic spheres[J]. International Journal of Computational Fluid Dynamics, 2017, 31(6/7/8): 310-323.
[33]	Liu X H, Zhao Y M, Chen S, et al. Numerical research on the dynamic characteristics of a droplet impacting a hydrophobic tube[J]. Physics of Fluids, 2017, 29(6): 062105.
[34]	Mundo C, Sommerfeld M, Tropea C. Droplet-wall collisions: experimental studies of the deformation and breakup process[J]. International Journal of Multiphase Flow, 1995, 21(2): 151-173.

微米尺度液滴与尘粒作用后反弹行为特性研究

Study on rebound behavior characteristics of droplets and dust particles at micron-scale

RichHTML

PDF (PC)

可视化

摘要/Abstract

引用本文

使用本文

图/表 20

参考文献 34

相关文章 13

编辑推荐

Metrics

本文评价

[1]	马晓文, 程扬帆, 李世周, 梁茹萍, 鲍忠奥. 粒径对TiH₂粉尘云燃爆特性及温度分布特征的影响[J]. 化工学报, 2025, 76(8): 4341-4349.
[2]	张帅, 喻健良, 丁建飞, 闫兴清. 气流输运工况玉米淀粉爆炸火焰传播与压力特性实验研究[J]. 化工学报, 2024, 75(5): 2072-2080.
[3]	李珍宝, 李超, 王虎, 王绍瑞, 黎泉. MPP抑制铝镁合金粉尘爆炸微观机理研究[J]. 化工学报, 2023, 74(8): 3608-3614.
[4]	蔡骁, 张龙凯, 王金华, 黄佐华. 单颗粒铁粉燃烧特性及产物形貌分析[J]. 化工学报, 2023, 74(11): 4702-4709.
[5]	吴延鹏, 栾珊珊, 苏伟, 邢奕, 钱付平. 钢铁厂原料堆粉尘无组织排放抑制技术进展[J]. 化工学报, 2021, 72(S1): 53-62.
[6]	孟凯, 许建良, 代正华, 刘海峰, 王辅臣, 龚剑洪. 水分子对初始碳烟颗粒形成过程影响的分子动力学模拟[J]. 化工学报, 2019, 70(6): 2237-2243.
[7]	吴延鹏, 郭占闯. 超疏水表面防附尘性能实验分析[J]. 化工学报, 2018, 69(S2): 365-372.
[8]	张斌, 胡恩柱, 刘天霞, 胡献国. 生物质燃油碳烟颗粒的形貌、结构与组分表征[J]. 化工学报, 2015, 66(1): 441-448.
[9]	朱辉, 付海明, 亢燕铭. 荷尘状态单纤维过滤压降数值计算与分析[J]. 化工学报, 2012, 63(12): 3927-3936.
[10]	张星, 姬忠礼, 陈鸿海, 熊至宜. 高压天然气管道内粉尘在线检测方法 [J]. 化工学报, 2010, 61(9): 2334-2339.
[11]	王延吉 ; 胡洁; 薛伟 ;赵新强. 催化反应过程绿色集成系统 [J]. CIESC Journal, 2007, 58(11): 2689-2696.
[12]	刘章现，冯兴华，杨甲文. 炭素厂生产车间粉尘及沥青烟治理工程设计 [J]. CIESC Journal, 2006, 25(7): 837-.
[13]	梁红;叶代启;林维明;付名利;何雄彬 . Sn催化剂对柴油车排气颗粒去除效果 [J]. CIESC Journal, 2004, 55(11): 1869-1873.