電熱蒸餾水器 的英文怎麼說

中文拼音 [diànzhēngliùshuǐ]
電熱蒸餾水器 英文
electrical distiller
  • : Ⅰ名詞1 (有電荷存在和電荷變化的現象) electricity 2 (電報) telegram; cable Ⅱ動詞1 (觸電) give...
  • : Ⅰ動詞1. (蒸發) evaporate2. (利用水蒸氣的熱力使食物熟或熱) steam Ⅱ名詞[中醫] (將藥物隔水蒸熟) steaming
  • : 餾動詞(蒸熱熟食) heat up; reheat
  • : 名詞1 (由兩個氫原子和一個氧原子結合而成的液體) water 2 (河流) river 3 (指江、河、湖、海、洋...
  • : 名詞1. (器具) implement; utensil; ware 2. (器官) organ 3. (度量; 才能) capacity; talent 4. (姓氏) a surname
  • 蒸餾 : [化學] [物理學] distillation; distill
  1. This series apparatus takes tap water as source water to producer pure water by mode of electric heating distilling with reasonable structures, easy operation, stable water - quality, & safe - durable use, it ' s ideal for clinicccs, hospitals, laboratories, electroplating, etc

    本系列不銹鋼斷自控電熱蒸餾水器,以自來作為源,用方法制取純,供醫療衛生、藥、鍍及實驗室等部門使用,本產品結構合理,使用方便,操作簡單,出量大,安全可靠,質穩定,經久耐用。
  2. 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,管的加方式為,工質為.在1 1模型上對分離式管管內凝結換特性、不凝性氣體對凝結換的影響及不凝性氣體的擴散規律進行了試驗,得出分離式管有一最佳充液率,其值為45 %左右;凝結換系數隨著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管的凝結換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;隨著壓力的增加,不凝性氣體對分離式管冷凝段的影響減少.這些結論可用於分離式管換的工程設計和控制
  3. 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,管的加方式為,工質為.在1 1模型上對分離式管管內凝結換特性、不凝性氣體對凝結換的影響及不凝性氣體的擴散規律進行了試驗,得出分離式管有一最佳充液率,其值為45 %左右;凝結換系數隨著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管的凝結換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;隨著壓力的增加,不凝性氣體對分離式管冷凝段的影響減少.這些結論可用於分離式管換的工程設計和控制
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