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Based on the physical meaning of each term in the linear parameter log I (a constant correlating the affinity of solut e t o stationary phase) of stoichiometric displacement model for retention o f solute, the thermodynamic characteristics of log I of solute in revers ed-phase liquid chromatography were investigated theoretically. This poi nt was tested by experimental data with two linear relationships:(1) plot of log I vs 1/T with apolar, polar small solut es and proteins;(2) plot of log I vs log Po/w (partition co effi cient of solute between n-octanol and water) with apolar and polar smal l solutes.

依据液相色谱中溶质计量置换保留模型及线性参数log I(与1 mol溶质对固定相的亲和势大小有关的常数),通过作图得知非极性和极性小分子溶质及生物大分子的log I与绝对温度的倒数1/T,以及小分子溶质的log I与其在正辛醇-水中分配系数的对数log Po/w呈线性关系,从两方面进一步证明了log I具有热力学平衡常数的性质。

The initial apparent rate constant, reaction order in term of Ru(superscript 3+)+ or (superscript 3+) concentration, equilibrium constant for the reaction of bipyridyl and Ru(superscript 3+) or (superscript 3+) in the presence of hydroxylamine hydrogenchloride were determined.

在盐酸羟胺存在下,测定了Ru(上标 3+)和(上标 3+)与bipy的反应表观速率常数、浓度级次及反应平衡常数

Gas phase synthesis of hydrogen iodide was taken for example.The example showed how to calculate extent of reaction from equilibrium constant and to calculate the heat capacities at constant pressure and constant volume.

以碘化氢气相合成反应为例,说明如何由化学反应的平衡常数计算平衡反应进度,进而计算定压热容和定容热容。

Equilibrium constant of salts for (liquid +solid) equilibrium at 288 K were evaluated with Pitzer"s model. The solubilities of quaternary and quinary system were calculated by Pitzer "s equations. The prediction results were in agreement with the experimental results essentially.

用288K时二元及三元体系的溶解度数据,运用多元线性回归的方法拟合了PitZer方程中288K时该五元体系所涉及各盐的单盐参数及混合参数;计算出了各盐288K时溶解平衡常数,运用PitZer方程对四元及五元稳定体系相平衡进行了理论模拟,计算结果基本令人满意。

In the sorption equilibrium experiments, the results showed that the equilibrium sorption coefficients for VOCs sorption on clay and organoclays decreased with increasing relative humidity, which proved that the existence and amount of water indeed suppressed the sorption capacities for clay and organoclays to sorb VOCs.

在平衡实验部分,挥发性有机化合物在黏粒或有机黏粒的吸附平衡常数皆随著相对湿度的增加而减小,证实水分的存在及多寡确实会抑制黏粒及有机黏粒对於有机化合物的吸附能力。

The stability of the ternary complexes in relation to their binary parent complexes is characterized by the equilibrium constant (△logK〓=logK〓-logK〓) corresponding to the equilibrium M (ATP 〓+ML〓=M L〓+M〓.

三元混配配合物相对于二元配合物的稳定性用相应于平衡ML〓+M〓=ML〓+M〓的平衡常数△logK〓=logK〓-logK〓表示。

The effects of ,, and temperature on the distribution ratio have been investigated. The composition of the extracted species is determined by the methods of slope ratio, continuous variation,extraction isotherm curves and their chemical analyses. The extraction is found to proceed according to the reaction:AuCl_4 ~-+DEOTA_(0)TAuCl3 .DEOTA_...

着重研究了盐酸浓度、氯离子浓度、氢离子浓度和温度诸因素对萃取的影响;对有机相中金的反萃行为也进行了初探;通过斜率法、等摩尔系列法、萃取等温线法确定了配合物的组成;推定了DEOTA在盐酸体系中萃取金的机理为配位取代反应;计算了萃取反应的表观平衡常数和配合物的稳定常数。

In this paper,the rate constant and equilibrium constant of the crack reaction of methyl silicane were obtained with the transition state theory and quantum chemistry calculation.

本文采用过渡态理论和量子化学计算方法,首次计算得到了甲硅烷裂解反应的速率常数和平衡常数,并对结果进行了讨论。

The dissociation constants and the reaction rate constants of inclusion complexes formed between α、β—cyclodextrin and several naphthyl esters (α—naphthyl acetate,β—naphthyl acetate,β—naphthyl caproate) were obtained by kinetics of hydrolyses of naphthyl esters.

通过几种脂肪酸萘酯(乙酸-α-萘酯、乙酸-β-萘酯、己酸-β-萘酯)的环糊精催化水解研究得到了它们同环糊精所形成的包接络合物的分解平衡常数和反应速度常数,进而提出了它们同环糊精所形成的包接络合物的结构模型。

Based on the traditional mechanical model the buble point method of three diagonal matrix, an neural network model of gas-liquid equilibrium computation for liquid air, which makes system presure P and equilibrium component of liquid phrase x1,x2,x3 as input nodes makes system temperature T, equilibrium component of gas nitrogen y1, equilibrium constant of argon and oxygen k2, k3 as output nodes, insteads of the buble point computation of the three diagonal matrix , thus a improved distillation model is built.

在传统的机理模型三对角矩阵法中的泡点法基础上,将体系压力P,平衡液相组成x1, x2, x3 为输入节点体系温度T ,平衡汽相氮组成y1 及氩、氧的相平衡常数k2, k3 为输出节点的神经网络液体空气汽液平衡计算模型,取代三对角矩阵法中泡点计算,从而建立改进的精馏塔模型改进模型用于空分塔的模拟计算,不仅计算速度快,计算结果与机理模型结果非常接近,且符合设计要求,对实现产品质量的在线监控具有一定的指导意义

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