设计了一种基于中空纤维膜的螺旋缠绕式空气隙膜蒸馏组件，以模拟海水为原料液，考察了热料液进口温度T₃、料液流量F、缠绕角度、空气隙厚度、内芯长度对膜通量和造水比的影响。实验结果表明，膜通量和造水比均随着热料液进口温度的增加而明显增大；当料液流量增加时，膜通量增大，造水比呈相反趋势；随着空气隙厚度的增加，膜通量和造水比均逐渐减小；膜通量和造水比均随着缠绕角度的增加而减小；内芯长度增加使得造水比提高，而膜通量则降低。实验过程中膜通量和造水比的最高值分别达到6.1 kg/（m²·h）和5.8，产水电导率始终保持在20.0 μS/cm以下。

A spirally wound air-gap membrane distillation module based on hollow fiber is designed for seawater desalination.Taking simulated seawater as feed liquid,the effect of the inlet temperature of hot feed,hot feed flow rate,winding angle,air gap thickness and the length of inner core on membrane permeate flux (J_W) and gained output ratio (GOR) are studied.The results show that both J_W and GOR increase with the increasing inlet temperature of hot feed.When the hot feed flow rate increases,J_W will increase while GOR will decrease.Both J_W and GOR decrease with increasing air gap thickness and winding angle.A larger length of inner core will make J_W increase and draw GOR to drop.The maximum of J_W is 6.1 kg·m^-2·h^-1and that of GOR is 5.8 during the experiments.The permeate conductivity has remained below 20.0 μS·cm^-1.