片语

reached the adsorption equilibrium达到吸附平衡

gas adsorption equilibrium气体吸附平衡

adsorption equilibrium co tant吸附平衡常数

adsorption desorption equilibrium吸附脱附平衡

adsorption equilibrium pressure吸附平衡压力

adsorption equilibrium equation吸附方程

adsorption equilibrium constant吸附平衡常数

adsorption reached equilibrium达到吸附平衡

reaching adsorption equilibrium达到吸附平衡

adsorption equilibrium constants吸附平衡常数

英汉例句

• the adsorption equilibrium and adsorption kinetic and thermodynamics of methylene blue on the adsorbent were studied.

  研究了该种吸附剂对亚甲基蓝的吸附过程，并对其吸附平衡、吸附动力学和热力学进行了研究。

• adsorption equilibrium on quaternary ammonium resin in uranyl sulphate solution, which is similar to composition used in uranium hydrometallurgy, was studied by chemical equivalent method.

  本文采用化学当量法研究了季铵树脂在组成接近铀水冶条件的硫酸铀酰-硫酸钠溶液中的吸附平衡。

• the silicagel column has showed an irreversible adsorption equilibrium for epirubicin and its analogues with slightly acidic or neutral mobile phases in hydrophilic interaction chromatography (hilic).

  亲水作用色谱分离表阿霉素时，在中性及弱酸性条件下，样品在硅胶柱上呈现不可逆吸附平衡过程。

• the adsorption equilibrium constant of germanium in lignite was determined.

  测定了煤对锗的吸附平衡常数。

• some parameters can be obtained from the fitting results, such as adsorption equilibrium constants of additives.

  由拟合结果可得到一些参数值，如吸附平衡常数等。

• the adsorption rate of acf was more rapid than that of gac in adsorbing methylene blue, so the adsorption equilibrium of acf can be easily reached within a short time.

  与颗粒状活性炭（gac）相比，活性炭纤维吸附脱色亚甲基蓝的速度快，在短时间内，就能达到吸附平衡。

• the lower the initial sdbs concentration, the faster the adsorption rate and the shorter the time reaching adsorption equilibrium necessary were.

  溶液的初始浓度对吸附速率产生明显影响，浓度越低吸附速率越快，达到吸附平衡所需的时间越短。

• adsorption equilibrium on quaternary ammonium resin in uranyl sulphate solution, which is similar to composition used in uranium hydrometal1urgy, was studied by chemical equivalent method.

  本文采用化学当量法研究了季铵树脂在组成接近铀水冶条件的硫酸铀酰-硫酸钠溶液中的吸附平衡。

• the adsorption equilibrium equation deduced through the theory of volume filling of micro-pore was used to fit the adsorption isotherms (obtained, ) and corresponding adsorption heat was calculated.

  采用由微孔填充理论导出的吸附平衡方程对所测得的等温线进行了拟合，计算相应的吸附热；

• here the comparison between the adsorption equilibrium constants obtained with single parameter model and five parameter model has also been made.

  文中还对单参数模型和五参数模型求取的吸附平衡常数作了比较。

• based on the adsorption equilibrium theory, this paper predicts the theoretical performance of adsorption refrigeration cycles of several new adsorbent-refrigerant pairs.

  应用吸附平衡基本理论对几种可能的吸附式致冷新工质对的性能进行了预测。

• the adsorption capacity of sediment particles which had reached adsorption equilibrium on n2 has decreased under the different system of concentration of phosphorus.

  在不同磷浓度体系下达到吸附平衡后的沉积颗粒物对n2的吸附量均有所降低；

• adsorption equilibrium constant has thermodynamic properties. the integral adsorption heat can be acquired from the adsorption equilibrium constants at different temperatures.

  吸附平衡常数具有热力学性质，从不同温度的吸附平衡常数可以得到积分吸附热。

• it is found that the adsorption equilibrium constant on the naked surface(k1) is larger than that on the adsorbed reductant(k2).

  添加剂在基体上的吸附平衡常数（k1）大于已吸附了还原剂的表面上的吸附平衡常数（k2）。

• the adsorption equilibrium time shortens and the adsorption capacity and ratio decrease with temperature.

  初始溶液浓度越高，沸石对磷素的吸附量越大，吸附平衡时间越长。

• the adsorption equilibrium constants decreased with the temperature, while the diffusivity increased with temperature.

  烃分子的吸附平衡常数随温度的升高而降低，而扩散系数随温度的升高而增大。

• the adsorption equilibrium constants are given here also.

  也给出了该吸附过程的吸附平衡常数。

• adsorptive capacity is one of the basic data in adsorption equilibrium experiment.

  吸附量是吸附平衡实验的基本数据之一。

• with the increase of temperature the adsorption equilibrium constants decrease while the effective diffusivity increases.

  实验结果表明，有效扩散系数随温度升高而增大，吸咐平衡常数则正好相反。

• the adsorption equilibrium data of six binary solution systems on ky zeolite at 90℃ and 175℃ were determined.

  测定了碳八芳烃异构体组成的六种二元溶液于90℃和175℃下在ky分子筛上的吸附平衡数据。

• adsorption equilibrium for the single and binary systems of co2 and ch4 on a ddr membrane was studied.

  研究了co2和ch4作为单一组分和混合组分在ddr膜中的吸附平衡。

• the adsorption of binary hydrocarbon liquid mixtures has adsorption equilibrium point, in the equilibrium point, the adsorption capacity of two constituents are both 0.

  ⑤二元烃类液体混合物吸附存在吸附平衡点，在吸附平衡点，两个组分的吸附量均为0。