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    双分离器并联CFB系统的稳定性分析

    Stability Analysis on CFB System with Two Cyclones in Parallel

    • 摘要: 利用瞬态吹空法获得了循环流化床(CFB)分离器内气固阻力特性的非单调曲线,采用以Chen提出的分离器压降模型为基础的修正模型对特定气体质量流量下分离器压降随固体质量流量的变化进行了预测.根据质量守恒定律、各分离器压降相等和最小能量原理等约束条件,分析了双分离器并联CFB系统的运行稳定性.结果表明:随着入口固体质量流量的增大,分离器的压降先快速降低后缓慢升高;修正模型的分离器压降计算值与实验测量值吻合较好;当CFB系统分离器压降和循环流率在偏流区域时,双分离器并联CFB系统处于稳定的偏流运行状态.

       

      Abstract: Non-monotonic characteristic curves of pressure drop in cyclone of a circulating fluidized bed (CFB) system were measured using transient-blowing method, while relationship between the cyclone pressure drop and solid mass flow studied under specific gas mass flow with corrected model based on cyclone pressure drop approach proposed by Chen. Meanwhile, the stability of CFB system with two cyclones in parallel was analyzed according to the law of mass conservation and constraint conditions as equality in pressure drop of all cyclones, and the least-energy principle, etc. Results show that with the rise of inlet solid mass flow, the cyclone pressure drop first decreases quickly and then increases slowly; the calculated values of cyclone pressure drop based on corrected model fit well with experimental results; when the cyclone pressure drop and circulating flow rate of CFB system are in deviation region, the CFB system will run stably in deviation flow state.

       

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