The hydrodynamic and mass transfer characteristics of a downflow liquid jet loop reactor (D-JLR) were studied experimentally with water/air and CMC (carboxymethyl cellulose) solution/air systems. The effects of the ge...The hydrodynamic and mass transfer characteristics of a downflow liquid jet loop reactor (D-JLR) were studied experimentally with water/air and CMC (carboxymethyl cellulose) solution/air systems. The effects of the geometry, the operating parameters and the physical properties of the liquid phase on gas hold-up and mass transfer coefficient were measuered. Compared with other types of gas-liquid reactor, D-JLR shows higher mass transfer coefficient and lower energy dissipation rate, the optimum diameter ratio was found to be about 0.42-0.6. A model for gas hold-up in D-JLR with Newtonian and non-Newtonian fluids has been developed on the basis of the equation of motion and the concept of average mixing length. The prediction of gas hold-up with the model agreed with the experimental results of this work.展开更多
为了研究在下行床中烟丝的快速干燥动力学行为,利用冷态下行床烟丝运动特性检测装置和热态下行床快速干燥处理装置,在一定的风速条件下,考察在下行床中烟丝的运动规律和热风温度（180～300℃）对烟丝快速干燥过程的影响,并对烟丝快速干...为了研究在下行床中烟丝的快速干燥动力学行为,利用冷态下行床烟丝运动特性检测装置和热态下行床快速干燥处理装置,在一定的风速条件下,考察在下行床中烟丝的运动规律和热风温度（180～300℃）对烟丝快速干燥过程的影响,并对烟丝快速干燥动力学进行分析.结果表明：①在下行床中烟丝的下落是一个先加速后匀速的过程,加速段的距离小于1.2 m,匀速运动时烟丝的速度与含水率呈现线性关系,烟丝含水率与下落高度的关系可用指数关系描述;②在考察温度范围内烟丝的快速干燥过程为降速干燥过程,菲克第二定律可以较好地表征在下行床中烟丝的快速干燥动力学行为,该过程中,烟丝干燥过程有效扩散系数介于6.448x10-9～2.624x10-8 m2/s之间,表观活化能为5.23 k J/mol.展开更多
文摘The hydrodynamic and mass transfer characteristics of a downflow liquid jet loop reactor (D-JLR) were studied experimentally with water/air and CMC (carboxymethyl cellulose) solution/air systems. The effects of the geometry, the operating parameters and the physical properties of the liquid phase on gas hold-up and mass transfer coefficient were measuered. Compared with other types of gas-liquid reactor, D-JLR shows higher mass transfer coefficient and lower energy dissipation rate, the optimum diameter ratio was found to be about 0.42-0.6. A model for gas hold-up in D-JLR with Newtonian and non-Newtonian fluids has been developed on the basis of the equation of motion and the concept of average mixing length. The prediction of gas hold-up with the model agreed with the experimental results of this work.
文摘为了研究在下行床中烟丝的快速干燥动力学行为,利用冷态下行床烟丝运动特性检测装置和热态下行床快速干燥处理装置,在一定的风速条件下,考察在下行床中烟丝的运动规律和热风温度（180～300℃）对烟丝快速干燥过程的影响,并对烟丝快速干燥动力学进行分析.结果表明：①在下行床中烟丝的下落是一个先加速后匀速的过程,加速段的距离小于1.2 m,匀速运动时烟丝的速度与含水率呈现线性关系,烟丝含水率与下落高度的关系可用指数关系描述;②在考察温度范围内烟丝的快速干燥过程为降速干燥过程,菲克第二定律可以较好地表征在下行床中烟丝的快速干燥动力学行为,该过程中,烟丝干燥过程有效扩散系数介于6.448x10-9～2.624x10-8 m2/s之间,表观活化能为5.23 k J/mol.
