vapor-liquid equilibrium 中文意思是什麼

vapor-liquid equilibrium 解釋
氣液平衡
  • vapor : n. 〈美國〉＝ vapour.
  • liquid : n 1 液體。2 【語言學】流音〈如 [l] [r]〉 adj 1 液體的，液態的，流動的。2 清澄的，透明的。3 易變的...
  • equilibrium : n. 1. 平衡，均衡，均勢，相稱。2. （心情的）平靜。3. （判斷的）不偏不倚。
  1. Liquid and vapor phases cannot coexist in equilibrium.

    液相和氣相不能在平衡中共存。
  2. Study on isobaric vapor - liquid equilibrium of methanol - propionic acid - h2o multisystems

    水多元系汽液平衡研究
  3. Study on isobaric vapor - liquid equilibrium for vinyltrichlorosilane vinyltrimethoxysilane binary system

    乙烯基三甲氧基硅烷二元體系等壓汽液平衡研究
  4. Vapor liquid equilibrium of acrylonitrile o -, m - or p - xylene

    丙烯腈體系的汽液平衡
  5. The azeotropic distillation of the system acetic acid - water - azeotropic agent ( isopropyl acetate and butyl acetate ) is simulated. due to the non - ideal behavior, nrtl - hoc and uniquac - hoc model is used to depict vapor - liquid phase equilibrium behavior of this system. concerning the liquid in the decanter, the stability is checked by tangent plane stability analysis, and the initialization of phase splitting calculation is produced. a good estimate of the phase fration is gotten by successive substitution with newton ' s method, and every component of two phase is gotten by mass equilibrium equation. finally, the solution of this equation is produced with successive substitution calcultion. the naphtali - sandholm method is used to simulation of azeotropic distillation. by virtue of this combined calculation method, the simulation is begun with operational data as basical data. the results of simulation accord with the operating data, which proved that the combined calculation method is credible

    該體系具有高度非理想性，氣液相平衡模型採用nrtl - hoc和uniquac - hoc模型，採用切平面判據法對進入分層器中的液相進行液相穩定性測試，提供液液相分離計算的初值，再結合牛頓拉夫森迭代法運算求得相分割系數，根據物料衡算求出各相組成，循環迭代可求得分層各組分數據，共沸精餾模擬計算採用那夫塔列-山德荷姆全變量迭代演算法。
  6. However, te - rich phases and point defects with high concentration were found locally. not only the vapor - solid equilibrium but also the vapor - liquid - solid equilibrium should be considered for the annealing of the crystals with te - rich phases. by analyzing the phase diagrams of cd - te and p - t plot of cd1 - xznxte ( x = 0. 04 ), it was concluded that for the purpose of rem

    本文通過仔細分析cd . te二元相圖和cd卜龍znxte （ x = 0 . 04 ）的p一t相圖，認為為了去除富te相，獲得穩定的電學性能，退火時晶片溫度應小於115ok ，氣氛環境的總壓力應小於pcs （對cdte ， pc洶
  7. The results can be summarized into the following aspects : molecular dynamics study of liquid - vapor interface shows that the planar liquid - vapor interface at macroscopic level is in fact a wavy surface fluctuating with time, and the length scale of the fluctuating region of the wavy surface is the thickness of the liquid - vapor interface. with speckle laser visualized experiment, the fluctuation of the interface can be verified qualitatively. moreover, md simulations indicate that in the liquid - vapor equilibrium system, there exists a local non - equilibrium region near the interface

    主要研究成果歸納如下：對汽液界面進行了分子動力學研究，揭示出宏觀尺度的平界面在分子尺度上是隨時間起伏漲落的曲分界面，分界面的漲落區域就是汽液界面的厚度，相應的激光散斑實驗也定性地證明了界面漲落區的存在；研究還發現在汽液平衡體系中，界面附近存在局域熱非平衡區域，並指出了其可能的原因及影響。
  8. Recent progress in vapor - liquid equilibrium for alcohol - water - salt systems

    含鹽醇水體系汽液平衡研究進展
  9. The effective stockmayer potential model method and vapor - liquid equilibrium simulation of hcfc - r

    勢能模型及汽液平衡分子模擬
  10. With the characteristic time method, we also studied the condensation coefficients of water and argon in liquid - vapor equilibrium system. the simulated condensation coefficient decreases with the increase of temperature for both argon and water, and the condensation coefficient of water is larger than that of argon. though the polarity and the rotation are considered in the simulation of water, the difference between the condensation coefficients of water and argon is not remarkable

    模擬獲得的lennard - jones流體和水在平衡條件下的凝結系數表明：水和氬的凝結系數為溫度的減函數；水的凝結系數略高於氬的凝結系數；雖然在水的模擬中考慮了分子的極性、旋轉等因素，但模擬獲得的水與氬的凝結系數之間的差距並不顯著，具體原因仍有待于進一步的探討。
  11. This article takes the chemical physics experiments " binary liquid - vapor equilibrium phase diagram " for the study, using the computer program to draw the liquid - vapor equilibrium phase diagram conveniently, and can extract composes is 0. 75 time gas phase composition and the boiling point respectively is 0. 5772, 64. 9737

    文章採用計算機程序方便地繪出氣液平衡相圖，並求出了溶液組成為任意值時（以摩爾分數為0 . 75為例）的氣相組成和沸點分別為0 . 5772 ， 64 . 9737 。
  12. On the basis of virial state equation and the corresponding - states principle, a state equation of corresponding - states - virial is proposed to calculate thermodynamics properties of humid air, which is used as working substance in humid air turbine and compressed air energy storage ( caes ) system at high temperature and high pressure. the activity coefficient method and eos method are utilized to calculate the vapor - liquid equilibrium state of humid air. main contents of study listed as following : 1

    用本文提供的計算模型對干空氣、水蒸汽和濕空氣的第二、第三維里系數進行了計算，並與asher提供的維里系數進行比較; 3 .用本文提出的對應態維里方程，計算得到濕空氣的壓縮因子，濕度在0 w 1kg / kg （ a ）的范圍內時，與實驗數據吻合較好。
  13. A thermodynamic model of vapor liquid solid three phase equilibrium and its moleling technique

    氣液瀝青三相相平衡熱力學模型與計算方法
  14. Fuel components in icf targets at vapor - liquid equilibrium phase

    靶丸內燃料的氣液兩相組分組成分析
  15. We reviewed the historical development of j - t refrigeration cycle and its current study at home and abroad. using cubic equation of state, the vapor - liquid equilibrium of cryogenic mixtures containing nitrogen and hydrocarbons and their thermodynamic properties were calculated. based on these calculations, the system and its components were designed

    綜述了混合工質j - t節流製冷循環的發展史及國內外研究現狀，採用立方型狀態方程對含氮混合工質的汽液相平衡和熱力性質進行了計算，並在此基礎上建立了j - t節流製冷系統各部件的物理模型，進行了系統的設計計算； 2
  16. Liquid vapor equilibrium

    液汽平衡
  17. Vle vapor liquid equilibrium app

    Vle氣液平衡裝置
  18. Magnesium has a relatively high vapor pressure ? indeed, one third of an atmosphere of magnesium vapor exists in equilibrium with the liquid metal at 950 degrees c

    鎂的蒸氣壓比較高，在950時與鎂金屬的氣態?液態平衡蒸氣壓高達1 / 3大氣壓。
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