浮閥塔 的英文怎麼說

中文拼音 []
浮閥塔 英文
float valve tower floating distillation tower valve tower
  • : Ⅰ動詞1 (漂在液體表面) float; drift 2 [方言] (在水裡游) swim Ⅱ形容詞1 (在表面上的) superfici...
  • : 名詞1 (指在某方面有支配勢力的人物或家族) established house or power group; a powerful person or...
  1. Or, if have the same operation loads, the downcomer size of ctst tray can be designed smaller than the fl valve tray. it was found that ctst plates have bigger operating capabilities than other traditional plates in coping with foaming systems

    總之,在處理兩種物系,尤其是易發泡物系時, ctst與f1等傳統板比較,其降液管操作能力大得多。
  2. In addition, the hf in the downcomer of ctst plate is 110 ~ 150mm lower than that of fl valve plate. it was showed that making a comparison of two plates, the downcomer of ctst tray can cope with more operation loads with the same size downcomers

    這說明相同大小的降液管, ctst板上的降液管可處理的操作負荷比浮閥塔板的要大;即若在相同的操作負荷下,在設計降液管時, ctst板的降液管尺寸可比浮閥塔板的小。
  3. Tower plate of floating valve

    浮閥塔
  4. The company takes advantage of advanced dcs control system, high efficient float valve tray technology, high efficient energy - saving exchange techniques, fcc catalytic cracking double riser, two - generator regeneration process, polypropylene with loop reactor process and refining and blending process of high - number gasoline, etc. to ensure providing the users with high - tech qualified products

    公司採用先進的dcs控制系統,高效的浮閥塔盤技術,高效節能交換技術, fcc催化裂化雙提升管、兩器再生工藝,環管聚丙烯工藝,高排號汽油精製調和工藝等,確保高科技合格產品送至用戶手中。
  5. This watts / flippen float valve product guide features high quality, reliable control assemblies and components that provide make up water for pressure washers, cooling towers, heat transfer units, cattle watering tanks, refrigeration units, and for many other applications where float valves are required

    這種美國瓦茨/ flippen的特點在於其優質、控制可靠的部件,為壓力清洗裝置,冷卻,熱傳送裝置,牲畜水,冷凍裝置,以及其他各種要求的應用提供補給水。
  6. By the adoption of a colunm with highly effective bubblecapplates and float valves and the strict control of demineralized water consumption, the total amount of dilute aqua ammonia from the three sections of earbonation, final purification and synthesis is less than the quantity of dilute aqua ammonia required for the production of ammonium bicarbonate, with zero discharge of the dilute aqua ammonia, thus not only prolecting the environment but also realizing a cestain economic benefit

    通過採用高效泡罩板浮閥塔,嚴格控制軟水用量,使碳化、精煉、合成3個工段所產生的稀氨水總量小於生產碳酸氫銨所需的稀氨水量,達到稀氨水的零排放,不僅保護了環境,而且取得了一定的經濟效益。
  7. The test was made on the compound tray, dual flow tray, sieve tray and valve tray for mass transfer efficiency with in - diameter 300 mm column using ethanoi and water system

    在直徑300mm的精餾內,以乙醇-水為介質,進行了復合板、穿流篩板、篩板和浮閥塔板的傳質效率的研究。
  8. The experiment ' s results show that the total and plat efficiency of the compound tray is over 100 %, the highest efficiency can be up to 122 % within the range of f factor i ~ 2. 5m / s ( kg / m3 ) i / 2, it is far higher than the efficiency of dual flow tray, sieve tray and valve tray

    實驗表明,復合的全效率和單板效率在f因子1 2 . 5m s ( kg m3 ) 」 』范圍內,可超過100 ,最高效率達122 ,遠高於穿流篩板、篩板和浮閥塔板的效率。
  9. The results showed that the gas - liquid interfacial area of grv could be remarkably increased

    通過實驗證明該浮閥塔板的相界面積得到顯著提高。
  10. A mathematical model was proposed to compute the interfacial area on the valve tray

    同時根據湍流液體中氣泡變形與破碎的機理,建立了計算浮閥塔板相界面積的理論模型。
  11. Cross flow cap tray

    錯流式浮閥塔
  12. Abstract : the problem of structure design for valve tower was discussed. some new calculation method and formula was proposed. and simu lating calculation was carried out with practical examples

    文摘:對浮閥塔的結構設計問題進行了討論,提出了一些簡化的計算公式,從而可以利用計算機進行輔助計算,並用實例進行了考核
  13. The effect of gas rates, liquid flow - rates, downcomer width, weir height and the addition of surface active agent on the liquid mean residence time, t, effective diffusion coefficient, de, and froth height, hf were studied. results obtained showed that for two systems, the t in the downcomer of ctst plate is 20 - 50 % smaller than that of fl valve plate, and the de is 40 - 70 % smaller than that of fl valve plate

    通過對氣速、液體流量、降液管寬度、堰高和表面活性劑加入的影響進行分析得出下面結論:在相同的操作條件下,對于兩種物系, ctst板降液管的液體停留時間比f1浮閥塔板的約小20 50 ,有效擴散系數比f1浮閥塔板的小40 70 ,泡沫高度低110 150mm 。
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