| 1. | Increase back pressure and lower screw rotation speed
增加背压和降低螺杆转速 |
| 2. | Increase dose and decrease screw rotation speed
增加料量,降低螺杆转速 |
| 3. | Powerthe pole turns soon
螺杆转速 |
| 4. | Screw rotate speedr min
螺杆转速 |
| 5. | Slower rpm " s result in a more uniform melt by minimizing shear heat buildup
较低的螺杆转速会由于最小的剪热而导致更均匀的熔化。 |
| 6. | The lowest possible rpm is recommended to minimize fiber breakage and screw recovery should be set accordingly
建议用尽可能低的螺杆转速以减小纤维的绞断和螺杆松退应据此设定。 |
| 7. | The variation of the operating condition did not change the distributive range magnitude of the dispersed phase droplet
螺杆转速和挤出机产量的变化对末端分散相液滴直径的分布范围影响不大。 |
| 8. | The pan / pu hollow fibers were successfully fabricated when the spinning temperature was controlled from 190 ? to 200 ? and the rotate speed of screw less than 70r / min
结果表明纺丝温度在190 ? 200之间，螺杆转速70r min时，能够顺利纺制pan pu中空纤维。 |
| 9. | Based on the melting experiments of pp powder in twin - screw extruder , the melting capacity of different screw - thread sets and the revolution of the screw was studied
摘要通过对pp粉料在双螺杆挤出机中的熔融实验，研究了不同螺纹组合和螺杆转速对物料的熔融能力。 |
| 10. | Using three - dimensional particle trajectories dispersed droplet diameter at the outlet of screw element during compounding in a co - rotating intermeshing twin - screw extruder was computed
摘要用物料三维流动路径结合分散模型计算了螺纹元件出口处分散相液滴的直径，分析了螺杆转速、挤出机产量和液滴初始直径对末端分散相液滴直径的影响。 |
