liquid liquid equilibrium 中文意思是什麼

liquid liquid equilibrium 解釋
液-液平衡
  • 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. Vapour liquid equilibrium of ethanol - cyclohexane - water system

    水汽液平衡數據的測定與關聯
  2. The result shows that all these system are simple eutectic, at the same time, the entropy of phase change of every system in the eutectic point is determined by using differential scanning calorimetry ( dsc ) on the basis of experimental research, through the improved one - parameter margules equation by introducing a new variable temperature, the improved equation was designed to compute solid - liquid equilibrium

    測定結果表明，這幾組體系均為簡單低共熔體系；同時利用差熱掃描量熱法（ dsc ）對上面各組體系低共熔點處的相變焓進行了測定。在實驗研究的基礎上，通過改進單參數margules方程並引入新的變量溫度，達到了將此方程用於固液平衡計算的目的。
  3. This article choosed out organic phase change materials, and, the solid - liquid - equilibrium of eleven binary system including fatty alcohol / fatty acid, n - octadecane / fatty acid, n - octadecane / fatty alcohol system were determined by cooling curve, and, t - x phase diagrams of these systems were drawn. the result shows that all these systems are simple eutectic, at the same time, the entropy of phase change of every system in the eutectic point is determined by using differential scanning calorimetry ( dsc ). and n - octadecane / fatty acid systems were calculated theoretically

    本文初選出部分有機相變貯能材料，採用步冷曲線法測定了12醇-羧酸系列、 18烷-羧酸系列、 18烷- 12醇體系共11組體系的二元固液相平衡關系，繪制了這11組體系的t - x相圖，測定結果表明，這幾組體系均為簡單低共熔體系；同時利用差熱掃描量熱法（ dsc ）對上面各組體系低共熔點處的相變焓進行了測定；並對18烷-羧酸系列進行了熱力學理論預測。
  4. Study on isobaric vapor - liquid equilibrium of methanol - propionic acid - h2o multisystems

    水多元系汽液平衡研究
  5. 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
  6. Vapor liquid equilibrium of acrylonitrile o -, m - or p - xylene

    丙烯腈體系的汽液平衡
  7. 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。
  8. The optimum results are gotten by simulation of changing the value of some variable such as feed position, theoretical tray. the optimum value can be used to guide industrial design. both isopropyl acetate and butyl acetate as azeotropic agent are contrast to each other according to operational data. besides, liquid - liquid equilibrium still is designed by onself, and its credibility is checked by the experimental data of the system acetic acid water - isopropyl acetate at 24

    對乙酸-水-乙酸異丙酯體系和乙酸-水-乙酸丁酯體系，分別進行了進料板位置、理論板數的優化計算，得到的優化結果可用於指導工業過程的設計；對採用乙酸正丁酯和乙酸異丙酯作夾帶劑時的操作進行了綜合比較。
  9. 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
  10. 4 if liquid reaches equilibrium within the scrubbing media, it cannot absorb additional gas

    如果溶劑在吸附材料表面的達到平衡，溶劑就不能再吸附多餘氣體。
  11. 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。
  12. 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
  13. 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
  14. The liquid - liquid equilibrium data of ternary dem - ethanol - glycerin system have been determined at atmospheric pressure and different temperatures of 20, 40 and 60 ? c, the conjugate phase compositions and thereout the contribution curves of this ternary liquid - liquid equilibrium system have been obtained

    摘要在常壓， 20 、 40 、 60下，測定了二乙氧基甲烷乙醇丙三醇三元體系的液液平衡數據，得到了三元液液平衡體系的共扼相組成並由此繪得相平衡曲線。
  15. Liquid - liquid equilibrium for the isopropanol - benzene - water - potassium fluoride system

    氟化鉀體系液液平衡
  16. This article studied solid - liquid - equilibrium ( s - l - e ) of organic compound system, measured solid - liquid phase diagram, latent heat of phase change and energy conservation effect in order to supply a sort of simple, feasible means to choose solid - liquid pcms

    本文對有機固液相平衡進行了探討和分析，並且對固液平衡相圖、相變潛熱和節能效果進行測定，目的在於為固液相變材料的篩選提供一種簡單、可行的研究方法。
  17. 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。
  18. 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 。
  19. 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。
  20. 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
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