Dynamic Behavior and Deformation Characteristics of Oil Droplets in Spiral Flow Field

The spiral flow field is the key to ensuring the performance of centrifugal and cyclonic separation equipment. The migration and deformation dynamics of oil droplets in a spiral flow field are a crucial topic to guide the design of separation equipment and parameter optimization. However, the droplet dynamics especially in a two-phase nonlaminar flow field is challenging and meaningful due to its complex interfaces and deformation behaviors. The deformation, migration, and breakup dynamic behaviors of discrete-phase oil droplets in the spiral flow field were innovatively investigated via numerical simulation and high-speed photography methods. Two distinct breakup modes─tensile breakup and impact breakup─were clearly identified by analyzing the morphological evolution of droplets in the spiral flow field. Simultaneously, through flow field analysis and the construction of oil droplet mechanical models, a predictive model was established and validated to describe the relationship among the inlet Reynolds number, pitch, and critical droplet breakup diameter. Results show that in the five-stage spiral tube, the peak tangential velocity migrates from the tube center to the outer wall between the first and second stages (where the initial droplet breakup occurs) and then stabilizes in the subsequent stages. Furthermore, the effect of the Reynolds number on droplet breakup shows that as the Reynolds number increases droplets are prone to undergo impact breakup. When <i>Re</i> ranges from 1000 to 60,000, the critical value for impact breakup increases from 2.4 to 5.5 mm. Further investigation into the effect of pitch on droplet breakup showed that increasing the pitch promotes breakup until the critical value of 60 mm, beyond which further increases inhibit breakup. This research provides new insights into the interface behavior of discrete phases in complex spiral flow fields and offers a practical reference for enhancing the performance of related separation equipment.

Authors

Institutions

Publication Details

Journal
Langmuir
Published
2025-12-23
DOI
https://doi.org/10.1021/acs.langmuir.5c05000
Primary Topic
Cyclone Separators and Fluid Dynamics
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Dynamic Behavior and Deformation Characteristics of Oil Droplets in Spiral Flow Field

Minghu Jiang, Kailei Zhou, Lixin Zhao, Shuai Guan et al.
Langmuir
Cyclone Separators and Fluid Dynamics
article

Dynamic Behavior and Deformation Characteristics of Oil Droplets in Spiral Flow Field

Minghu Jiang, Kailei Zhou, Lixin Zhao, Shuai Guan, Y. Chen, Lei Xing, Hanli Dong
article en

Abstract

The spiral flow field is the key to ensuring the performance of centrifugal and cyclonic separation equipment. The migration and deformation dynamics of oil droplets in a spiral flow field are a crucial topic to guide the design of separation equipment and parameter optimization. However, the droplet dynamics especially in a two-phase nonlaminar flow field is challenging and meaningful due to its complex interfaces and deformation behaviors. The deformation, migration, and breakup dynamic behaviors of discrete-phase oil droplets in the spiral flow field were innovatively investigated via numerical simulation and high-speed photography methods. Two distinct breakup modes─tensile breakup and impact breakup─were clearly identified by analyzing the morphological evolution of droplets in the spiral flow field. Simultaneously, through flow field analysis and the construction of oil droplet mechanical models, a predictive model was established and validated to describe the relationship among the inlet Reynolds number, pitch, and critical droplet breakup diameter. Results show that in the five-stage spiral tube, the peak tangential velocity migrates from the tube center to the outer wall between the first and second stages (where the initial droplet breakup occurs) and then stabilizes in the subsequent stages. Furthermore, the effect of the Reynolds number on droplet breakup shows that as the Reynolds number increases droplets are prone to undergo impact breakup. When <i>Re</i> ranges from 1000 to 60,000, the critical value for impact breakup increases from 2.4 to 5.5 mm. Further investigation into the effect of pitch on droplet breakup showed that increasing the pitch promotes breakup until the critical value of 60 mm, beyond which further increases inhibit breakup. This research provides new insights into the interface behavior of discrete phases in complex spiral flow fields and offers a practical reference for enhancing the performance of related separation equipment.

LangmuirVol. 42(1)
Daqing Oilfield General Hospital (CN), Beijing University of Chemical Technology (CN), Northeast Petroleum University (CN)
Openalex Percentile: Top 36%
Cyclone Separators and Fluid Dynamics
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.