電力冷水器 的英文怎麼說

中文拼音 [diànlěngshuǐ]
電力冷水器 英文
electric water cooler
  • : 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名1 (力量; 能力) power; strength; ability; capacity 2 [物理學] (改變物體運動狀態的作用) forc...
  • : 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...
  • : 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
  • 電力 : [電學] power; electric power電力變阻器 power rheostat; 電力捕魚 electrofishing; 電力潮流 directio...
  1. They also say that the electricity needed to pump the sea water to the condenser can be produced by windmills.

    他們還說,把海抽進所需要的,可用風車發來解決。
  2. The air thermal cnergy water heater creates the new generation hot water cquipments. it makes use of the negative card promise successfully, drieing a hot pump with the elcctrie power. equiping through a hot pump medium of compesing parts evaporate a machine. hot pump, congealed machine and inflate valve, urge the work quality completes evaporationt absorb calories within air continuously compress compress congealed reduce expenses evaporate of the thermody name energy cirenlation proess, transfer the calories in the environment to the water thus in, transfer the in great quantities free calories in the air to the life to use a water in

    空氣節能熱是創新一代熱設備,它成功地運用逆卡諾原理,用能驅動熱泵,通過熱泵裝置中的構成部件-蒸發,熱泵,和膨脹閥,促使工質不斷完成蒸發(吸收空氣中的熱量)壓縮凝節流蒸發的熱循環過程,從而環境的熱量轉移到中,將空氣中大量免費的熱量轉移到生活中
  3. Develop and manufacture large pumped storage units, large tubular turbine units, high - power super - critical thermal power unit, large air - cooled turbine generator, large cfb boilers, high - power nuclear steam turbine and generator, pressure shell of nuclear island, high - pressure evaporator and primary pump

    開發生產大型抽蓄能機組、大型貫流式機組、大功率超臨界火機組、大型空汽輪發機、大型循環硫化床鍋爐、大功率核站汽輪機和發機、核島設備壓殼、高壓蒸發和主泵等核一級設備。
  4. There are five parameters need to be measured. there are five channels for input : the displacement of casting - roller, the rotate speed of casting - roller, the pressure of casting and rolling, the casting temperature and the water - speed of cooling water. they are measured by raster, photoelectric coder, strain pressure sensor, thermocouple and turboflowmeter

    系統需要進行監測的參數有五個,即有五路輸入信號:鑄輥位移、鑄輥轉速、鑄軋壓、澆鑄溫度、流速,分別採用光柵、光編碼、應變式壓傳感、熱偶和渦輪流量計作為檢測元件。
  5. These results show that since the existent defects of combustion device structure and its hypothetical circle of contact, these make a poor primary and secondary wind rigidity in operation and a too big actual circle of contact. in addition, the coal used is extreme prone to burn and reside in boiler. under such a condition, the coal powder ignites earlier in a short time and short distance when it leave the jet - combustioning device, and splashes the water cooler, eventually this results in a burned coal residue in boiler

    針對宏偉熱廠410t / h燃煤鍋爐嚴重結渣問題,對燃煤的結渣性、爐內溫度工況及空氣動工況等進行實驗研究,由於燃燒結構和假想切圓選擇的缺陷,使得鍋爐在正常運行時,一、二次風剛性較差,實際切圓過大,加上目前燃用煤質屬于極易燃、易結渣煤質,致使煤粉在離開噴燃很短的時間、較短的距離內開始著火,並沖刷壁,最終造成爐膛結渣。
  6. The shahe pumped - storage power station with two 50mw reversible units has been in good conditions on general since it was put into operation, but there still were some defects, such as the failure of unit ' s contemporaneous device, the insufficient cooling water discharge and pressure, and the failure of static frequency converter and excitation overcurrent

    摘要沙河抽蓄能站兩臺50mw可逆式機組自投運以來,總體情況良好,但是也出現了一些缺陷,如機組同期裝置故障,機組流量或壓不足,靜止變頻故障,勵磁過流故障等。
  7. Air conditioners, liquid chilling packages and heat pumps with electrically driven compressors. heating mode. part 3 : testing and requirements for marking for sanitary hot water units

    驅動壓縮機的空調,液體卻設備和熱泵.供暖方式.第3部分:衛生用熱裝置的試驗和標記要求
  8. The mathematical and physical dynamic models are given based on the adsorbent theory of porous medium. its running and parameters affecting its performance are numerically studied and the method that control the water content in the absorbent bed is recommended. the improvement on system configuration to recover heat is discussed and the operation scheme is given

    利用多孔介質吸附模型和平衡吸附壓的概念建立了該系統工作過程的物理數學模型,數值模擬的方法模擬了其工作過程和影響因素,提出了控制吸附床含濕量的方案,驗證了改進流程回收能量的可行性並給出了操作方案,提出並分析了用熱回收蒸氣潛熱節約能的方法。
  9. Air conditioners, liquid chilling packages and heat pumps with electrically driven compressors - heating mode - testing and requirements for marking for sanitary hot water units

    動壓縮機的空調.液體製設備和熱泵.加熱方式.衛生間熱裝置的試驗和標記要求
  10. 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

    建立了空氣卻實驗臺,熱管的加熱方式為加熱,工質為蒸餾.在1 1模型上對分離式熱管管內凝結換熱特性、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,得出分離式熱管有一最佳充液率,其值為45 %左右;凝結換熱系數隨著蒸汽壓的增加略有降低,在實驗的壓范圍內,降低了9 . 5 % ;不凝性氣體對分離式熱管的凝結換熱僅影響凝段下部較小部分,通過排氣閥排出不凝性氣體可有效地改善凝段下部的凝結換熱;隨著壓的增加,不凝性氣體對分離式熱管凝段的影響減少.這些結論可用於分離式熱管換熱的工程設計和控制
  11. 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:建立了空氣卻實驗臺,熱管的加熱方式為加熱,工質為蒸餾.在1 1模型上對分離式熱管管內凝結換熱特性、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,得出分離式熱管有一最佳充液率,其值為45 %左右;凝結換熱系數隨著蒸汽壓的增加略有降低,在實驗的壓范圍內,降低了9 . 5 % ;不凝性氣體對分離式熱管的凝結換熱僅影響凝段下部較小部分,通過排氣閥排出不凝性氣體可有效地改善凝段下部的凝結換熱;隨著壓的增加,不凝性氣體對分離式熱管凝段的影響減少.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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