张明刚, 王磊, 卢志明. DZSN2828型三质体智能脱泥细筛在西庞洗煤厂的应用[J]. 选煤技术, 2023, 51(5): 81-84. DOI: 10.16447/j.cnki.cpt.2023.05.016
    引用本文: 张明刚, 王磊, 卢志明. DZSN2828型三质体智能脱泥细筛在西庞洗煤厂的应用[J]. 选煤技术, 2023, 51(5): 81-84. DOI: 10.16447/j.cnki.cpt.2023.05.016
    ZHANG Minggang, WANG Lei, LU Zhiming. Application of the DZSN2828 intelligent 3-mass fine desliming screen at Xipang Coal Preparation Plant[J]. Coal Preparation Technology, 2023, 51(5): 81-84. DOI: 10.16447/j.cnki.cpt.2023.05.016
    Citation: ZHANG Minggang, WANG Lei, LU Zhiming. Application of the DZSN2828 intelligent 3-mass fine desliming screen at Xipang Coal Preparation Plant[J]. Coal Preparation Technology, 2023, 51(5): 81-84. DOI: 10.16447/j.cnki.cpt.2023.05.016

    DZSN2828型三质体智能脱泥细筛在西庞洗煤厂的应用

    Application of the DZSN2828 intelligent 3-mass fine desliming screen at Xipang Coal Preparation Plant

    • 摘要: 为解决击打式固定弧形筛筛下“跑粗”、筛上“夹细”导致的粗精煤泥灰分、水分偏高的问题,并避免系统内形成不必要内循环,西庞洗煤厂通过充分调研国内常见粗精煤泥脱水工艺、设备,综合考虑现有场地条件,在不改变脱泥筛+煤泥离心机脱水工艺的条件下,以三质体智能脱泥细筛替代原击打式固定弧形筛进行了技改。技改实践表明:相较改造前,改造后的三质体智能脱泥细筛筛上物中<0.25 mm粒级的产率减少了10.70个百分点,筛上物灰分降低了0.85个百分点;筛下物中>0.25 mm粒级的产率减少了46.24个百分点,尤其是>0.5 mm粒级的产率减少了9.03个百分点,有效解决了改造前粗煤泥脱泥、脱水环节存在的问题,不仅可避免重介“背灰”,而且并有利于改善浮选柱分选条件。三质体智能脱泥细筛在西庞洗煤厂的成功应用可为存在类似问题选煤厂的改造提供有益借鉴。

       

      Abstract: Because of the failure of the impact-type fixed sieve bend to retain the coarser particles, and the presence of fine size in its overflow, the clean coarse coal is rendered considerably high in both ash and moisture. To deal with this situation and avoid the formation of unnecessary internal circulation in the system, technical transformation work is made by Xipang Coal Preparation Plant, following a thorough technical survey of the clean coarse slime dewatering processes and equipment commonly applied in China, and by taking overall consideration of the plant′s existing site conditions. The plant finally opts for the use of the intelligent 3-mass fine desliming screen to replace the fixed sieve bend, with the existing processes of using desliming screen plus dewatering centrifuge remaining unchanged. As indicated by field practice, with the use of the three-mass fine screen, the yield of the <0.25 mm size in the screen′s overflow and the ash of the latter both see a drop by 10.70 percentage points and 0.85 percentage point, respectively; the yield of the >0.25 mm size in the screen′s underflow, especially that of the >0.5 mm size are both reduced by 46.24 percentage points and 9.03 percentage points, respectively; and the problems arising in the coarse slime desliming and dewatering links have been effectively eliminated, making it possible for the heavy medium separation system to operate with lesser reduction of the ash of its clean coal product, and improve the working conditions of the flotation column. The successful application of the intelligent 3-mass fine screen provides a certain reference for the plants to make similar technical renovations.

       

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