空氣凝結器 的英文怎麼說

中文拼音 [kōngníngjiē]
空氣凝結器 英文
air condenser
  • : 空Ⅰ形容詞(不包含什麼; 裏面沒有東西或沒有內容; 不切實際的) empty; hollow; void Ⅱ名詞1 (天空) s...
  • : Ⅰ名詞1 (氣體) gas 2 (空氣) air 3 (氣息) breath 4 (自然界冷熱陰晴等現象) weather 5 (氣味...
  • : 動詞1. (凝結) congeal; curdle; coagulate 2. (注意力集中) fix
  • : 結動詞(長出果實或種子) bear (fruit); form (seed)
  • : 名詞1. (器具) implement; utensil; ware 2. (器官) organ 3. (度量; 才能) capacity; talent 4. (姓氏) a surname
  • 空氣 : 1 (大氣) air; atmosphere 2 (氣氛) atmosphere 3 (氣閘) air brake4 pneum ; pneumo ; pneumat ;...
  1. When “ holding ” ( during normal operation ), non condensable, which are coming from air ingress and oxygen content in steam and condensate, must also be extracted normally by main ejectors

    當「建立真」 (正常操作下)時,入口處的不可物和蒸汽中的氧含量以及水必須由主抽汽排出。
  2. Condensate receiver tank ( e1183 ) collect the condensate from acc and drain pot, and the condensate will be pump to deaerate through condensate pump, and the condensate level controled by the level transmeter ( lt450 ) and switch ( ls451, ls452 )

    水回收箱( e1183 )收集及集液箱中的中的水,其中的水由液位變送( lt450 )及液位開關( ls451 , ls452 )對水泵(它方供貨)的電機(它方供貨)進行控制,水被送到除氧
  3. From simulations and data of fire site, most air preheater fire often appear when boiler is started in cool state and standby which fuels of insufficient combustion coagulate and congregate on the parts of air preheater. when the temperature of smoke inpouring air preheater increases, aggregate fuels and sediments will combust in stated temperature conditions. it is called the second combustion of air preheater

    這些起火起因於燃料油的不充分燃燒,其果是未充分燃燒的燃料油和聚集在預熱的部件上,當進入的煙溫度增高時,沉積的燃料油被烘烤,當達到一定溫度條件時,則可點燃這些燃料油污沉積物,造成火災發生,這通常被稱為預熱的二次燃燒。
  4. To improve the performance of ashp, an improved ashp system is presented. different from the original system, the new one can control the refrigerant flow rate by the sub - cooling of condenser and adjust the sup - heating of the compressor inlet vapor by the heater in accumulator. the simulation shows the new system not only has better dynamic characteristic of frost and defrost of ashp, but also has higher coefficient of performance

    為改善源熱泵機組的霜除霜動態性能,提出了一種利用冷過冷度來調節製冷劑流量,在液分離里增加電熱裝置保持壓縮機進口過熱度的改進型系統,果表明這種改進型系統不但可以改善系統的運行性能,同時能改善系統運行的經濟性,為機組的技術升級和產品更新提供了一個新的途徑。
  5. Measurements were made of system pressure, mass flow rate of steam, air, and cooling water, temperatures of condensing flow and cooling flow, and the water level of boiler. the major phenomena observed in the present experiment are similar to those by other investigators. the mass flow rate of steam, the system pressure and air content are the most important factors affecting steam condensation

    實驗果表明,維持二次側冷卻水流量不變,無論對于純凈蒸汽還是含有的蒸汽冷,隨著蒸汽發生加熱功率的增大(即蒸汽流量增大) ,有效冷段長度將加長;當蒸汽中含有少量,有效冷段長度也會明顯加長;提高系統壓力,有效冷段長度將縮短。
  6. Heat exchangers - forced convection air cooled refrigerant condensers and dry coolers - sound measurement ; german version en 13487 : 2003

    熱交換.強制對流冷卻製冷劑和乾式冷卻機
  7. A tropical cyclone is akin to a travelling heat engine. it feeds on an incessant supply of latent heat released from condensation in ascending moist air

    熱帶旋類似一臺會走動的熱能機,它的能量來自濕上升時水汽而釋放的潛熱。
  8. 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

    建立了冷卻實驗臺,熱管的加熱方式為電加熱,工質為蒸餾水.在1 1模型上對分離式熱管管內換熱特性、不體對換熱的影響及不體的擴散規律進行了試驗,得出分離式熱管有一最佳充液率,其值為45 %左右;換熱系數隨著蒸汽壓力的增加略有降低,在實驗的壓力范圍內,降低了9 . 5 % ;不體對分離式熱管的換熱僅影響冷段下部較小部分,通過排閥排出不體可有效地改善冷段下部的換熱;隨著壓力的增加,不體對分離式熱管冷段的影響減少.這些論可用於分離式熱管換熱的工程設計和控制
  9. 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:建立了冷卻實驗臺,熱管的加熱方式為電加熱,工質為蒸餾水.在1 1模型上對分離式熱管管內換熱特性、不體對換熱的影響及不體的擴散規律進行了試驗,得出分離式熱管有一最佳充液率,其值為45 %左右;換熱系數隨著蒸汽壓力的增加略有降低,在實驗的壓力范圍內,降低了9 . 5 % ;不體對分離式熱管的換熱僅影響冷段下部較小部分,通過排閥排出不體可有效地改善冷段下部的換熱;隨著壓力的增加,不體對分離式熱管冷段的影響減少.這些論可用於分離式熱管換熱的工程設計和控制
  10. Heat exchangers - forced convection air cooled refrigerant condensors - test procedure for establishing performance

    熱交換.強制對流冷卻製冷劑.性能確定的試驗程序
  11. Heat exchangers - forced convection air cooled refrigerant condensors - test procedure for establishing performance includes amendment a1 : 2002 ; german version en 327 : 2000 a1 : 2002

    熱交換.強制對流冷卻製冷劑.規定性能的
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