排氣冷凝器 的英文怎麼說

中文拼音 [bèilěngníng]
排氣冷凝器 英文
vent condenser
  • : 排構詞成分。
  • : 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...
  • : Ⅰ形容詞1 (溫度低; 感覺溫度低) cold:冷水 coldwater; 你冷不冷? do you feel cold?; are you feeling...
  • : 動詞1. (凝結) congeal; curdle; coagulate 2. (注意力集中) fix
  • : 名詞1. (器具) implement; utensil; ware 2. (器官) organ 3. (度量; 才能) capacity; talent 4. (姓氏) a surname
  • 排氣 : [機械工程] exhaust; aerofluxus; air out; exit gas; ventilate; atmosphere; vent排氣泵 exhaust pump...
  1. As to simple turbine, steam discards directly into atmosphere, or into condensator for cooling, then goes back to boiler for use

    在簡單的渦輪機中,蒸汽被入大,或進入成水后流回鍋爐。
  2. The condenser should be hot enough to allow venting of some of the volatiles carried in the steam.

    的熱度,應足以使蒸中的一些揮發物質出。
  3. Fini air treatment, recommended for the most demanding professional uses, is composed of refrigerating dryers, filters for separating impurities, condensate drain cocks, water - oil separators, tanks, and all other components necessary for optimising compressor operation

    Fini空處理系統,由藏乾燥組成,用過濾分開雜質,立式出管,水油分離罐和其他空壓機必須的零部件組成,建議使用在大多數要求苛刻的專業用途。
  4. The air - cooled steam condenser ( acc ) condenses the turbine exhaust steam or the de - superheated steam from the turbine bypass by rejecting the heat to the atmosphere

    ( acc )通過向大釋放熱量對汽機汽或汽機旁路的減溫過熱蒸汽進行
  5. The dried material is put into the middle of shell, mixing by the rake teeth and the material shaft works back and forth. the indirect heating, equal agitation of rake teeth and grinding of breaking stick makes water in material evaporation. under the effect of vacuum system, the water in the dried material and apparent water are discharged and the vapor water is discharged from outlet of vacuum pump passing dry dust collector, wet dust collector and condenser

    被乾燥物料從殼體上方正中間加入,在不斷正反轉動的耙的攪拌下,物料軸向來回走動,與殼體內壁接觸的表面不斷更新,受到蒸汽的間接加熱,耙的均勻攪拌,粉碎棒的粉碎,使物料內的水份化,在真空系統的作用下,使被乾燥物料內部水份和表面水份更有利的出,化的水份經乾式除塵濕式除塵,從真空泵出口處放空。
  6. It has been shown that this updated sampling and measurement method, which can measure the content of tar and dust individually, appears much more precise and credible, particularly aiming at the characteristic of heavy tar and dust content in biomass gas. this clarification system that adopts two - level shell and tube condensers and one tar removal filter, has the advantages of high removal efficiency ( 97 % ~ 98 % ) and low operating cost. besides, it has been made more environmentally friendly considering that wastewater from condensers has measured up to related effluent state standards after being disposed in tar clarifier - tank

    多次試驗表明:針對生物質浙江大學碩士學位論文含焦油灰塵量大的特點,改進的生物質焦油取樣測量法可實現焦油和灰塵的分離,有較高準確性和可靠性;採用二級管殼式與一級乾式過濾結合的燃凈化系統不但凈化效率高( 97 98 ) 、運行費用低,而且含焦油廢水二經過澄清池澄清處理后可達到國家相關污水放標準,避兔了濕式凈化系統的水污染;兼顧凈化效果、經濟性和減少污染考慮,採用以半焦為吸附材料的于式凈化系統可以達到炊用燃對焦油含量的要求。
  7. 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結換熱特性、不體對結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;結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結換熱僅影響段下部較小部分,通過出不體可有效地改善段下部的結換熱;隨著壓力的增加,不體對分離式熱管段的影響減少.這些結論可用於分離式熱管換熱的工程設計和控制
  8. 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結換熱特性、不體對結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;結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結換熱僅影響段下部較小部分,通過出不體可有效地改善段下部的結換熱;隨著壓力的增加,不體對分離式熱管段的影響減少.這些結論可用於分離式熱管換熱的工程設計和控制
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