condensed gas meaning in English
冷凝气体, 凝聚气体
Examples
- 7 . . based on fluid inclusion and oil and gas geochemical character , it is concluded that low mature gas came from banqiao depression and condensed gas and high mature gas came from banqiao depression and qikou depression
据此作出预测，千米桥潜山的油气勘探，应以寻找临近板桥凹陷一侧的凝析油气藏为主，而临近歧口凹陷一侧则比较可能发现气藏。 - 6 . the character of hydrocarbon production and high gas - oil ratio show that the main migration facies in buried hills is gas facies ( including condensed gas facies ) . the early migration facies is condensed gas facies , later , gas facies
6烃类产物的特征和气油比比较高，这表明潜山以气相(包括凝析气相)运移为主：早期的运移为凝析气相，晚期为气相。 - The condensation heat - exchange characteristic of a separate - type heat - pipe was studied on a 1 : 1 model . the heat pipe is heated by electricity , and working fluid is distilled water , and it is cooled by air . the experimental results show that , ( 1 ) when charging liquid ratio is 45 % , condensation heat - exchange coefficient reaches to maxium ; ( 2 ) when there is not non - condensing gas , the coeffcient decreases a little with the increase of vapour pressure , and it decreases by 9 . 5 % when the pressure increases from 0 . 16mpa to 0 . 36mpa ; ( 3 ) when there is non - condensing gas , the coefficient decreases a little , but when the gas is discharged by an exhaust value , it can be improved , when the volume content of the gas is 2 . 5 % , it can increased by 22 % ; ( 4 ) the effect of the non - condensing gas on the coefficient decreases with the increase of the pressure , and when the volume content of the gas is 5 % and the pressure increases from 0 . 16mpa to 0 . 36mpa , the coefficient increases by 6 % . the relative curves are given between condensation heat - exchange coefficient and air flowrate , charging liquid ratio and vapour pressure
建立了空气冷却实验台，热管的加热方式为电加热，工质为蒸馏水.在1 1模型上对分离式热管管内凝结换热特性、不凝性气体对凝结换热的影响及不凝性气体的扩散规律进行了试验，得出分离式热管有一最佳充液率，其值为45 %左右；凝结换热系数随着蒸汽压力的增加略有降低，在实验的压力范围内，降低了9 . 5 % ；不凝性气体对分离式热管的凝结换热仅影响冷凝段下部较小部分，通过排气阀排出不凝性气体可有效地改善冷凝段下部的凝结换热；随着压力的增加，不凝性气体对分离式热管冷凝段的影响减少.这些结论可用于分离式热管换热器的工程设计和控制 - Abstract : the condensation heat - exchange characteristic of a separate - type heat - pipe was studied on a 1 : 1 model . the heat pipe is heated by electricity , and working fluid is distilled water , and it is cooled by air . the experimental results show that , ( 1 ) when charging liquid ratio is 45 % , condensation heat - exchange coefficient reaches to maxium ; ( 2 ) when there is not non - condensing gas , the coeffcient decreases a little with the increase of vapour pressure , and it decreases by 9 . 5 % when the pressure increases from 0 . 16mpa to 0 . 36mpa ; ( 3 ) when there is non - condensing gas , the coefficient decreases a little , but when the gas is discharged by an exhaust value , it can be improved , when the volume content of the gas is 2 . 5 % , it can increased by 22 % ; ( 4 ) the effect of the non - condensing gas on the coefficient decreases with the increase of the pressure , and when the volume content of the gas is 5 % and the pressure increases from 0 . 16mpa to 0 . 36mpa , the coefficient increases by 6 % . the relative curves are given between condensation heat - exchange coefficient and air flowrate , charging liquid ratio and vapour pressure
文摘:建立了空气冷却实验台，热管的加热方式为电加热，工质为蒸馏水.在1 1模型上对分离式热管管内凝结换热特性、不凝性气体对凝结换热的影响及不凝性气体的扩散规律进行了试验，得出分离式热管有一最佳充液率，其值为45 %左右；凝结换热系数随着蒸汽压力的增加略有降低，在实验的压力范围内，降低了9 . 5 % ；不凝性气体对分离式热管的凝结换热仅影响冷凝段下部较小部分，通过排气阀排出不凝性气体可有效地改善冷凝段下部的凝结换热；随着压力的增加，不凝性气体对分离式热管冷凝段的影响减少.这些结论可用于分离式热管换热器的工程设计和控制 - In order to solve this problem , this paper analyzes the fault diagnosis method for chillers using wavelet packet analysis . this paper simulated 9 faults including decreasing of cooling water flow , decreasing of refrigerant and non - condense gas existed and so on . it also analyzed the fault diagnosis technology combined theory and experiments
本论文模拟了冷却水量改变、有不凝性气体、制冷剂流量减小等九个故障,并采用理论分析与实验验证相结合的方法对单螺杆式冷水机组的故障诊断技术进行了研究。