Stage-Optimized Intensification of Spiral Separation: Process Deconstruction and a Novel Spiral Separator Design
The dynamic migration of mineral particles within spiral separators and its control via structural parameters are not yet fully understood, hindering efficiency improvements. To this end, a set of spiral separators with systematically adjusted structural parameters was designed. Extensive sampling of a 1–0.25 mm coal slurry yielded 120 samples from 6 separators, across 5 turns and 4 radial streams. Sink-float analysis revealed a well-defined three-stage separation mechanism: the roughing stage involves rapid segregation of light and heavy particles, while intermediate-density particles remain widely distributed; the intensified cleaning stage governs the radial migration of intermediate-density particles while simultaneously enriching the high-density and low-density fractions; and the final cleaning stage stabilizes the particle distribution and redirects misplaced particles. The influence of key structural parameters was also quantified: the composite cross-section outperformed cubic parabolic and elliptical profiles, markedly enhancing the separation of high-density and medium-high-density particles from the lighter product; increasing the trough inclination angle significantly promoted the radial inward migration of medium-high-density particles; a reduced pitch-to-diameter ratio effectively concentrated high-density and medium-high-density particles within inner and middle regions. Based on these insights, a “process intensification” strategy was proposed and materialized in a novel spiral separator design featuring stage-optimized, multi-parameter coordination. Performance evaluation demonstrated a separation efficiency of 94.74% under equivalent product quality constraints, a substantial improvement over conventional design. This work provides a fundamental, stage-specific understanding of particle separation dynamics and establishes a practical basis for the advanced design of high-efficiency spiral separation systems.
Authors
- Ruxia Chen (ORCID: https://orcid.org/0000-0002-5085-3824)
- Guichuan Ye
- Mingsheng Xia
- Shiqi Liu (ORCID: https://orcid.org/0000-0001-5023-4815)
- Chi Zhang (ORCID: https://orcid.org/0009-0009-9915-1493)
- Xiaomin Ma
- Qingxiang Liu
- Yuanpeng Fu
- Baoshan Zhu
- Xianshu Dong
Institutions
- Huaneng Clean Energy Research Institute (CN)
- Beibu Gulf University (CN)
- Taiyuan University of Technology (CN)
- Tsinghua University (CN)
Publication Details
- Journal
- Minerals
- Published
- 2026-01-29
- DOI
- https://doi.org/10.3390/min16020153
- Citations
- 1
- Primary Topic
- Granular flow and fluidized beds
- Type
- article
- Field-Weighted Citation Impact
- 41.77
Funders
- Tsinghua University
- Shanxi Research Institute for Clean Energy