精餾塔 的英文怎麼說

中文拼音 [jīngliù]
精餾塔 英文
finestiller
  • : Ⅰ形容詞1 (經過提煉或挑選的) refined; picked; choice 2 (完美;最好) perfect; excellent 3 (細)...
  • : 餾動詞(蒸熱熟食) heat up; reheat
  1. Simplified model for distillation tower of air separation unit in igcc plant by comparting method

    電站空分系統精餾塔的分段簡化模型
  2. The neural network inferential control strategy for distillation column

    精餾塔神經元網路推斷控制
  3. Optimizing control of distillation column based on rbf neural network

    基於徑向基函數神經網路的精餾塔優化控制
  4. Rbf neural networks applied in soft - measuring of distillation columns

    徑向基函數神經網路在精餾塔軟測量中的應用
  5. Application of advanced control scheme based on soft - sensor in distillation column

    基於軟測量技術的先進控制在精餾塔上的應用
  6. About 40 dividing wall columns ( dwc ) have been applied industrially

    其中的分隔壁精餾塔已有40座以上工業化。
  7. 2 sets of fractionating towers produced for canadian customer, which are attached with export labels for delivery after inspected by customers

    為加拿大客商生產製作的2臺精餾塔,經客商驗收貼上出口標簽,準備發運。
  8. Cracking unit fractionator

    裂化裝置的精餾塔
  9. But the temperature difference at the vertical direction in combustion chamber in lead column, that is said by operator, is over 60 ?. ( 2 ) according to the experiences in the practice, the second layer air and the second layer gas had a little effect of support burning, and the third air has little effect for combustion, and the power to drawing exhaust gas can only be adjusted in limited range. the problems, it is said above, restricted more advance of some kinds of technology and economy target in spelter refining in new jersey furnace

    由於鋅爐產量提高,一些問題開始暴露出來: ( 1 )燃燒室?舶要求溫度差不超過10 ,而從現場反映的情況來看,燃燒室上、中、下部溫度差已超過60 ; ( 2 )在生產實踐中,發現燃燒室第二層空氣、第二層煤氣作用甚小,第三層空氣失去助燃作用,廢氣出口的抽力可調范圍有限;以上這些問題在客觀上制約了精餾塔在鋅煉中各項技術經濟指標的進一步提高。
  10. In the second place, based on the asu of buggenum igcc plant in netherlands, both static and dynamical model for distillation tower of the asu are created and some valuable conclusions are gained as well. finally, a compartmental simplified model is created for distillation tower of the asu, in order to reduce the simulation time and increase the simulation efficiency. the new model will be helpful to the further simulation and on - line optimal control for the asu of the igcc plant

    其次,本文以荷蘭buggenum電站的空分系統為原型,基於matlab建立了空分系統精餾塔的半圖形化動、靜態數學模型,並通過模擬,得出了一些有價值的結論:當空分系統的壓力變化時,氧氣產品濃度的響應時間常數為兩小時左右,說明空分系統是igcc電站最大延遲環節;而且雖然氧氣濃度最後會穩定在igcc電站所要求的范圍之內,但在過渡過程中會超出限制,這些都為igcc電站的安全運行及控制系統設計提供了有價值的信息。
  11. Abstract : the safety of extended service for butadiene extraction and rectification tower , after design life and with corrosion in rubber plant, qilu petro - chemical industry company is evaluated according to the safety assessment rules of pressure vessels containing defects in service

    文摘:根據在役含缺陷壓力容器安全評估規程,對運行已達到設計壽命並存在一定腐蝕的齊魯石化公司橡膠廠丁二烯萃取精餾塔的超期股役安全性進行了分析與評定。
  12. Gc ms analysis of datong raw and oxidized coal extract using methanol tetrahydrofuran mixed solvent

    含水四氫呋喃萃取精餾塔的動態模擬
  13. 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的精餾塔內,以乙醇-水為介質,進行了復合板、穿流篩板、篩板和浮閥板的傳質效率的研究。
  14. The first part comprises industrial pta oxidation process modeling, residual fluid catalytic cracking process modeling, complex distillation modeling and analysis, the application of pta oxidation process soft - sensor technology. in the second one, the infeasibility degree based genetic algorithm is proposed to handle constrained optimization problem in engineering cases and the neighborhood and archive based genetic algorithm and its variant are proposed to treat the multi - objective optimization problem. with that, the pta oxidation process is regarded as a benchmark for the application of the proposed multi - objective optimization genetic algorithm

    論文內容分為兩部分,第一部分對包括三個典型的工業過程, pta氧化反應器、渣油催化裂化反應系統和復合式精餾塔進行分析、建模以及pta氧化過程的軟測量工程實施;第二部分分別提出了基於進化演算法解決工業過程中普遍存在的約束優化問題和多目標優化問題的過程優化演算法? ?基於不可行度選擇遺傳演算法和基於鄰域和存檔操作遺傳演算法,並利用該演算法對工業pta氧化過程操作進行多目標優化研究。
  15. Construction technology of rectifying tower of air separation plant

    空分裝置精餾塔安裝技術
  16. One ring own alcohol rectifying tower of phenol

    苯酚一環己醇精餾塔
  17. Model for distillation tower of air separation system of igcc plant

    電站空分系統精餾塔的建模
  18. The simulation of air distillation tower by using improved model of distillation tower

    改進精餾塔模型用於空分模擬計算
  19. The results indicate that the position of sensitive plates is located at the section of middle or upper in tower but not near by feeding plate, and the smaller reflux ratio, the closer overhead of distillation tower. accurate calculation for flash is solved using matlab, and the result is correct and reasonable. complicated multi - components distillation and crude distillation are simulated using chemcad, and results are reasonable about profiles of flow for vapor and liquid as well as temperature in the tower

    數值分析的結果表明精餾塔靈敏板位置並不在進料板附近,而是位於段的中上部,且迴流比愈小,愈靠近頂;利用matlab實現了蒸過程的嚴格計算,與參考值比較,結果正確、合理;藉助于chemcad進行常減壓的穩態模擬計算,得出了流量和溫度在內的分佈,經過理論分析,結果合理,可為實際生產提供參考。
  20. A typical continuous fractionating column equipped with the necessary auxiliaries and containing rectifying and stripping sections is shown in fig. 21. 7

    圖21 . 7所示的是一個典型的連續操作精餾塔。它配備有必要的輔助設施,包括段與提段兩部分。
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