水管式冷卻器 的英文怎麼說

中文拼音 [shuǐguǎnshìlěngquè]
水管式冷卻器 英文
water-tube type cooler
  • : 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...
  • : 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;...
  • : 名詞1 (樣式) type; style 2 (格式) pattern; form 3 (儀式; 典禮) ceremony; ritual 4 (自然科...
  • : 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...
  • : Ⅰ動詞1 (後退) step back 2 (使退卻) drive back; repulse 3 (推辭; 拒絕) decline; refuse; reje...
  • : 名詞1. (器具) implement; utensil; ware 2. (器官) organ 3. (度量; 才能) capacity; talent 4. (姓氏) a surname
  • 水管 : waterpipe; water carrier; aqueduct; water conduit; water pipe; syphon; siphon (消防) 水管車 hos...
  1. Centralized piped supply system for condenser cooling, centralized piped supply system for cooling towers and district cooling scheme

    集中道供應系統集中道供應塔用系統及區域性系統
  2. Other types of cooling systems include : fresh water cooling towers, air - cooled system, water - cooled air conditioning system centralized piped supply system for condenser cooling, centralised piped supply system for cooling towers and district cooling scheme

    -其他種類的系統包括:淡塔氣系統系統集中道供應系統集中道供應塔用系統及區域性系統。
  3. Abstract : this article presents the reason and mechanism of waterside corrosion of condenser ' s tube, which is related to water quality and water speed, pipe material and treatment of cooling water and additional protection and cleaning method

    文摘:介紹了凝汽側腐蝕原因和機理,與質和速有關,還與材和處理諸因素有關,也和附加保護及清洗方有關。
  4. Theoretical and experimental study of ellipse tube type indirect evaporative cooler wrapped with absorbing water materials

    包覆吸性材料橢圓間接蒸發的理論與實驗研究
  5. At hot end of beat pipe, several measures were taken to eliminate heat, namely ( 1 ) traditional sensible heat elimination ; ( 2 ) exhaust air is processed by air washer, then passes through hot end ; ( 3 ) exhaust air is handled by wet film, then passes through hot end ; ( 4 ) sprays water at the top of hot end, respectively

    第一級採用熱間接蒸發,熱端布置4種散熱方: ( 1 )傳統類型的顯熱散熱; ( 2 )排風經過噴室降溫后進入熱端; ( 3 )排風經過填料直接蒸發降溫后進入熱端; ( 4 )直接在熱端頂部淋
  6. This equipment is mainly composed of braising apparatus 、 condenser 、 balanced water tank 、 material pump 、 circulating pump of cooling water 、 double water - ring vaccum pump 、 connecting pipeline and electrical control box

    本設備主要由閃蒸、平衡箱、出料泵、循環泵、雙級真空泵、聯接道及電控制櫃等組成。
  7. The cooler designed is a pipe - shell type cooler and the water pump driven by direct current servo motor is an away center type pump

    設計的泵採用直流伺服電動機帶動的離心泵。
  8. It specifies the process of the design, simulation and experiment of liquid cooling system. main contents of the thesis are as follows : description of the present usage of liquid cooling system, presentation of a new type of liquid cooling system and description of its work principles ; design of the liquid cooling system, which mainly deals with the design and collating calculating of serpentine condenser and heat exchangers adopted in this system. meanwhile, the model chosen calculating of compressor 、 thermal expansion valve 、 plate evaporator 、 water pump and the like equipment used in the system are also carried out

    本文的主要內容如下:對液源使用現狀進行了描述,提出了一種新型液源系統並對其工作原理進行了闡述;對系統進行了設計,主要對系統中所採用的側空/液換熱進行了設計和校核計算,同時對系統中所用到的壓縮機、熱力膨脹閥、板蒸發泵等配套設備進行了選型計算;分別對製系統和液循環系統進行了數學建模。
  9. The heat transfer and flow resistance performance of petal - shaped finned tube oil - cooler with helical baffles was studied, and compared the total heat transfer coefficient of petal - shaped fimed tube oil - cooler with helical baffles with that of smooth tube oil - cooler with segmental baffles

    摘要研究了螺旋隔板花瓣的傳熱和流阻性能,並與弓形隔板光滑進行了性能對比。
  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

    建立了空氣實驗臺,熱的加熱方為電加熱,工質為蒸餾.在1 1模型上對分離內凝結換熱特性、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;隨著壓力的增加,不凝性氣體對分離凝段的影響減少.這些結論可用於分離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:建立了空氣實驗臺,熱的加熱方為電加熱,工質為蒸餾.在1 1模型上對分離內凝結換熱特性、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;隨著壓力的增加,不凝性氣體對分離凝段的影響減少.這些結論可用於分離換熱的工程設計和控制
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