管餾器 的英文怎麼說

中文拼音 [guǎnliù]
管餾器 英文
pipe still
  • : Ⅰ名詞1 (管子) pipe; tube 2 (吹奏的樂器) wind musical instrument 3 (形狀似管的電器件) valve;...
  • : 餾動詞(蒸熱熟食) heat up; reheat
  • : 名詞1. (器具) implement; utensil; ware 2. (器官) organ 3. (度量; 才能) capacity; talent 4. (姓氏) a surname
  1. The plant is mainly engaged in producing medical, foodstuff and exported silicon rubber products including silicon rubber sealing rings for household distillatory, watering trough, water clarifier, shower set, electric cooker, canning of foodstuffs, vacuum flask and other products ; and producing medical silica gel bottle closure, bulb, disinfector, rubber blanket, hose, high temperature resistant silicon rubber sealing rings of every kind and other rubber products

    本廠主要生產醫用級、食品級以及出口硅橡膠製品,用於家用蒸、飲水機、凈水、淋浴、電飯鍋、食品罐、保溫瓶等產品的配套硅膠密封圈;生產醫用硅膠瓶塞、吸球、消毒塊、膠板、膠、各種耐高溫硅橡膠密封圈等橡膠製品。
  2. There have long been question regarding whether or not an fcc main fractionator needs relief valve protection for anything except some smaller events, like steam ? out or fire

    關於是否要fcc標準下主分的的電子來保護除了像蒸汽或爐火等一類的小事件之外的件,已經成為了一個長期爭論的問題。
  3. When the design pressure of the reactor / regenerator is less than or equal to the design pressure of the main fractionator, or there is some absolute mechanical limit to the regenerator pressure ( plus the static head difference between the regenerator and reactor ) that is less than the main fractionator design pressure, the units do not need large relief valves on the main fractionator

    當所設計反應或交流熱換的壓力小於或等於主分,又或者有些機械上無可避免的限制(還有就是兩靜電頭的不同)小於交流熱換的壓力,其時整個部件就不需要大的調劑電子了。
  4. In this way it can prevent from the phenomenon of filler block caused by scrap iron and its life is prolonged. all parts that will contact ethanol in the device such as condensor. buffer tank, cooling snake pipe are made of stainless steel in order to guaran - tee that the finished product, ethanol, is not polluted

    塔體採用不銹鋼製作,從而防止了鐵屑堵塞填料的現象,延長了裝置的使用期限。本裝置中凡接觸酒精的設備部份如冷凝、穩壓罐、冷去口蛇等均採用不銹鋼,以確保成品酒精不被污染。
  5. The laboratory technicians at bicon have placed the aluminum oxide sleeve in an ultrasonic cleaner with distilled water before building up the porcelain

    在拜肯中心技工所技師先將氧化鋁套置入超音波清潔內的蒸水中,之後做成齒冠。
  6. In place of the reboiler, a heating coil may be placed in the bottom of the column to generate vapor from the pool of liquid there

    例如可以在精塔的底部安裝一個加熱盤代替再沸,加熱釜液產生蒸汽。
  7. For the purpose of home brewing in any premises conducted in accordance with the above conditions, you are allowed without a licence to possess in those premises any utensil or apparatus, other than a still or part of a still, for manufacturing the liquor, together with fermenting or fermented materials not exceeding 60 litres

    為按上述條件在任何處所進行家中自釀制酒,你可以在並無領有牌照的情況下在該處所內有用作製造有關酒類的用具或具(但蒸或其任何部分除外) ,以及不超逾60升的發酵中或已發酵的物料。
  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

    建立了空氣冷卻實驗臺,熱的加熱方式為電加熱,工質為蒸水.在1 1模型上對分離式熱內凝結換熱特性、不凝性氣體對凝結換熱的影響及不凝性氣體的擴散規律進行了試驗,得出分離式熱有一最佳充液率,其值為45 %左右;凝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 % ;不凝性氣體對分離式熱的凝結換熱僅影響冷凝段下部較小部分,通過排氣閥排出不凝性氣體可有效地改善冷凝段下部的凝結換熱;隨著壓力的增加,不凝性氣體對分離式熱冷凝段的影響減少.這些結論可用於分離式熱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:建立了空氣冷卻實驗臺,熱的加熱方式為電加熱,工質為蒸水.在1 1模型上對分離式熱內凝結換熱特性、不凝性氣體對凝結換熱的影響及不凝性氣體的擴散規律進行了試驗,得出分離式熱有一最佳充液率,其值為45 %左右;凝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 % ;不凝性氣體對分離式熱的凝結換熱僅影響冷凝段下部較小部分,通過排氣閥排出不凝性氣體可有效地改善冷凝段下部的凝結換熱;隨著壓力的增加,不凝性氣體對分離式熱冷凝段的影響減少.這些結論可用於分離式熱換熱的工程設計和控制
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