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Experimental Determination And New Correlations For Multi-Component Solid Solubilities In Supercritical Carbon Dioxide

机译:超临界二氧化碳中多组分固体溶解度的实验测定和新关联

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摘要

The fluids that are operated above their critical temperature and pressure areknown as supercritical fluids (SCFs). SCFs replaces the conventional organic solventsin the chemical processes due to their attractive properties such as liquid likedensities, gas like diffusivities, negligible surface tension, lower viscosity and high compressibility. Carbon dioxide, being non-toxic, non-flammable with ambientcritical temperature and moderate critical pressure, is the most widely used SCF inmany chemical processes. Supercritical carbon dioxide (SCCO2) finds applications inindustrial processes such as extraction and separation processes. The feasibility of asupercritical process can be determined from the solubility of solute in SCF. For theefficient design of a SCF process, the effects of temperature and pressure on thesolubility of a solid should be examined thoroughly. In general, the solute of interest is not present alone; it is present along with many other components in the compound. The solute has to be extracted or separated from matrix of components. Therefore, it is important to determine the mixture solubilities in SCCO2. The mixture solubility of a solute is not same as that of pure component solubility. The presence of the other component alters the solubility of the solute to a greater extent; hence the effects of the other components present along with the solute, temperature and pressure need to be known to understand the mixture behavior of the solute in SCCO2. The solubilities of solid isomers (ortho-, meta-, para-) in SCCO2 vary to a greater extent. This huge difference in the solubilities of isomers is due to interactions between the molecules. The high solubility of an isomer in SCCO2 might be due to the solute-solvent interactions. The interactions between the molecules are significant in the solid mixtures solubilities in SCCO2. This researchwork focuses on experimental determination and modeling of mixture solubilities ofsolids in SCCO2.The solubilities of several pairs of isomers have been experimentally determined at different temperatures and pressures. These include the ternary solubilities of ntrophenols, nitrobenzoic acids and dihydroxy benzene isomers mixtures in SCCO2. The experimental solubilities of nitrophenol (meta- and para-) isomers mixture have been determined. This study includes the effect of temperature, pressure and each isomer on the ternary mixture solubilities of nitrophenol mixtures. The enhancements in the ternary solubilities of nitrophenols over their binary solubilities and the selectivity of SCCO2 for the nitrophenol mixture have been discussed in detail. The solubilities of dihydroxy benzene (ortho-: pyrocatechol, meta- : resorcinol and para-: hydroquinone) isomers in SCCO2 have been determined at various temperatures and pressures. The ternary solubilities of pyrocatechol and resorcinol and quaternary solubilities of pyrocatechol, resorcinol and hydroquinone mixtures in SCCO2 have been investigated. The effect of each isomer on the mixture solubilities of other isomers has been included in this work. Selectivity for dihydroxy benzene isomers and variation of solubilities enhancements with temperature and pressure has been presented in this study. The equilibrium mixture solubilities of nitrobenzoic acid isomers (meta- and para) mixture have been studied. The variation of mixture solubilities and their enhancements with temperature and pressure has been thoroughly analyzed. Selectivity of SCCO2 for this nitrobenzoic acid mixture has been studied in detail.The increase or decrease in the ternary solubilities of the solid mixtures thathave been considered in this study is due to the interactions between the molecules.The ternary solubilities of m-nitrophenol increase whereas they decrease for pnitrophenol for the nitrophenol solid mixture. Quaternary solubilities of dihydroxybenzene isomers (pyrocatechol + resorcinol + hydroquinone) increases compared totheir pure component solubilities. The ternary solubilities of pyrocatechol increases while resorcinol decreases over the pressure range at different temperatures (except 338 K) considered in this study. The mixture solubilities of p-nitrobenzoic acid of nitrobenzoic acid isomers increase to a greater extent. An average of separationefficiency of 70%, 85% and 90% has been observed for ternary solid mixtures ofnitrophenol, nitrobenzoic acid and dihydroxy benzene isomers respectively. Modeling of high pressure multi-component systems is useful to understand the behavior of the mixtures. Moreover, the experimental determination of multicomponent solubilities of solids in SCCO2 is tedious and time consuming; hence the modeling of mixture solubilities is essential. The interactions between the molecules have been incorporated in the association theory and a five parameter equation with two constraints has been derived for binary systems. The new equation correlates the solubilities of m-dinitrobenzene in this study along with 72 other systems available in literature. Seven new model equations have been developed to correlate ternary (2 forcosolvent (solid + cosolvent + SCCO2) systems; 5 for solid mixtures in SCCO2)solubilities of solids in SCCO2. A new model equation for cosolvent ternary systemshas been derived by using the concepts of association of molecules. The model equation contains seven adjustable parameters with three constraints and correlates mixture solubilities in terms of temperature, pressure, density and cosolvent composition. The interactions between the molecules have been included in the association theory then the number of parameters decreased to five with two constraints. The performance of the newly developed equations has been evaluated for 32 ternary systems with various cosolvents along with experimental data of mdinitrobenzene in methanol cosolvent of this study. The same association theory has been extended to ternary (solid mixtures +SCCO2) solubilities of solids in SCCO2 and two new equations have been derived with and without incorporating interactions between the molecules. Both the equations have five adjustable parameters with three constraints for the equation which has been derived from association theory alone and two constraints for the equation which has been derived by considering the interactions between themolecules in the association theory. A new model equation has been derived by combining solution model with Wilson activity coefficient model to account for nonidealities of the solute. This equation has four adjustable parameters and noconstraints on the parameters. The non-idealities of both solutes in the solution model have been included and two more equations with no constraints on the parameters have been developed. One equation uses NRTL activity coefficient model whichresults in three adjustable parameters while the other equation with five parametershas been obtained from Wilson activity coefficient model for solid mixturessolubilities in SCCO2. The performance of the newly developed equations has beenevaluated for the solid mixtures (ternary systems) in SCCO2. The equations withconstraints make them limited for few systems and the equations with no constraintsare able to correlate the solubilities of solids of all the ternary systems that areavailable in literature along with the generated ternary experimental data of this study. The quaternary solubilities of solids have been correlated by using a five parameter model equation which has been derived by combining solution and Wilson activity coefficient models. The equation for the quaternary systems does not have constraints on the parameters; hence can be applied for quaternary systems. The equation correlates the quaternary solubilities of solids in terms of temperature, pressure, density and cosolute compositions. Chapter 1 gives a brief introduction on the solubilities of solid mixtures and their behavior in SCCO2. Chapter 2 presents the experimental setup and the solubilitydata of binary, ternary and quaternary systems determined in this study. Chapter 3focuses on the models that have been derived to correlate the solubilities of solids inSCCO2. Chapter 4 discusses in detail about the results obtained in this research work.Chapter 5 briefly summarizes the work and presents major conclusions. The new equations that have been developed here are first of its kind for the ternary and quaternary systems. These equations give information about the nonidealities of the systems. The nature of the interactions between the molecules can be determined from the parameters of the equations which incorporate interactions between the molecules. The multi-component solubilities of the solids can be correlated by using the semi-empirical equations that have been derived in this research.
机译:在其临界温度和压力之上工作的流体称为超临界流体(SCF)。 SCF由于其吸引人的特性(如液体相似度,气体扩散性,表面张力可忽略不计,较低的粘度和高压缩性)而在化学过程中替代了常规有机溶剂。在环境临界温度和中等临界压力下,无毒,不可燃的二氧化碳是SCF在许多化学过程中使用最广泛的方法。超临界二氧化碳(SCCO2)在工业过程中的应用,例如提取和分离过程。超临界过程的可行性可以通过溶质在SCF中的溶解度来确定。为了高效地设计SCF工艺,应彻底检查温度和压力对固体溶解度的影响。通常,感兴趣的溶质并不单独存在。它与化合物中的许多其他成分一起存在。溶质必须从成分矩阵中提取或分离。因此,确定混合物在SCCO2中的溶解度非常重要。溶质的混合物溶解度与纯组分的溶解度不同。其他组分的存在会在更大程度上改变溶质的溶解度;因此,需要了解其他组分以及溶质,温度和压力的影响,以了解溶质在SCCO2中的混合行为。固体异构体(邻位,间位,对位)在SCCO2中的溶解度变化较大。异构体溶解度的巨大差异是由于分子之间的相互作用。异构体在SCCO2中的高溶解性可能是由于溶质与溶剂的相互作用所致。分子之间的相互作用在固体混合物在SCCO2中的溶解度中很重要。这项研究工作着重于实验确定和模拟固体在SCCO2中的混合物的溶解度。已经在不同的温度和压力下通过实验确定了几对异构体的溶解度。这些包括在SCCO2中的三元酚,硝基苯甲酸和二羟基苯异构体混合物的三元溶解度。已经确定了硝基苯酚(间位和对位)异构体混合物的实验溶解度。这项研究包括温度,压力和每种异构体对硝基苯酚混合物三元混合物溶解度的影响。详细讨论了硝基苯酚的三元溶解度相对于其二元溶解度的提高以及SCCO2对硝基苯酚混合物的选择性。已在各种温度和压力下测定了二羟基苯(邻-:邻苯二酚,间-:间苯二酚和对-:对苯二酚)异构体在SCCO2中的溶解度。研究了邻苯二酚和间苯二酚的三元溶解度以及邻苯二酚,间苯二酚和对苯二酚混合物在SCCO2中的四元溶解度。每种异构体对其他异构体的混合物溶解度的影响已包括在这项工作中。这项研究提出了二羟基苯异构体的选择性以及溶解度随温度和压力的变化。研究了硝基苯甲酸异构体(间位和对位)混合物的平衡混合物溶解度。混合物溶解度的变化及其随温度和压力的增强已经得到了彻底的分析。已经详细研究了SCCO2对这种硝基苯甲酸混合物的选择性。本研究中考虑的固体混合物的三元溶解度的增加或降低是由于分子之间的相互作用所致,间硝基苯酚的三元溶解度增加,而对于硝基苯酚固体混合物,它们的对硝基苯酚含量降低。与纯组分的溶解度相比,二羟基苯异构体(邻苯二酚+间苯二酚+对苯二酚)的季溶解度增加。在此研究中,在不同温度(338 K除外)的压力范围内,邻苯二酚的三元溶解度增加,而间苯二酚的溶解度降低。硝基苯甲酸异构体的对硝基苯甲酸的混合物溶解度更大程度地提高。对于硝基苯酚,硝基苯甲酸和二羟基苯异构体的三元固体混合物,已观察到平均分离效率分别为70%,85%和90%。高压多组分系统的建模有助于理解混合物的行为。此外因此,实验测定SCCO2中固体的多组分溶解度既繁琐又费时;因此,混合物溶解度的建模至关重要。分子之间的相互作用已被结合到缔合理论中,并针对二元系统推导了具有两个约束的五参数方程。新方程将本研究中的间二硝基苯的溶解度与文献中可用的其他72种系统关联起来。已经开发了七个新的模型方程式,以关联三元(2个助溶剂(固体+助溶剂+ SCCO2)系统; 5个用于SCCO2中的固体混合物)的固体在SCCO2中的溶解度。利用分子缔合的概念推导了一种新的共溶剂三元体系模型方程。模型方程式包含具有三个约束条件的七个可调整参数,并根据温度,压力,密度和助溶剂组成关联混合物的溶解度。分子之间的相互作用已包含在缔合理论中,然后参数的数量减少到五个,且有两个约束。这项新开发的方程式的性能已针对32种具有各种助溶剂的三元系统以及本研究的甲醇共溶剂中的二硝基苯的实验数据进行了评估。相同的缔合理论已经扩展到固体在SCCO2中的三元(固体混合物+ SCCO2)溶解度,并且推导了两个新的方程式,其中包含和不包含分子之间的相互作用。这两个方程都有五个可调参数,对方程的三个约束是单独从缔合理论得出的,而对方程的两个约束是通过考虑分子在缔合理论中的相互作用而得出的。通过将溶液模型与Wilson活度系数模型相结合,得出了一个新的模型方程,以说明溶质的非理想性。该方程式具有四个可调参数,并且对参数没有约束。溶液模型中包含了两种溶质的非理想性,并开发了两个不受参数限制的方程。一个方程使用NRTL活度系数模型,得出三个可调参数,而另一个方程则从Wilson活度系数模型获得了五个参数,用于SCCO2中固体混合物的溶解度。对于SCCO2中的固体混合物(三元系统),已经对新开发的方程的性能进行了评估。有约束的方程使它们受限于少数系统,无约束的方程能够将文献中可用的所有三元系统的固溶度与本研究生成的三元实验数据联系起来。通过使用五参数模型方程来关联固体的四元溶解度,该方程是通过结合溶液和Wilson活度系数模型得出的。四元系统的方程对参数没有约束;因此可以应用于四元系统。该方程根据温度,压力,密度和固溶成分将固体的四元溶解度关联起来。第1章简要介绍了固体混合物的溶解度及其在SCCO2中的行为。第2章介绍了本研究确定的二元,三元和四元系统的实验装置和溶解度数据。第三章重点介绍了与固体在SCCO2中的溶解度相关的模型。第4章详细讨论了这项研究工作中获得的结果。第5章简要总结了工作并提出了主要结论。在此开发的新方程式是三元和四元系统的第一类。这些方程式给出了有关系统非理想性的信息。分子之间相互作用的性质可以从结合了分子之间相互作用的方程式的参数中确定。固体的多组分溶解度可以通过使用本研究得出的半​​经验方程式进行关联。

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    Reddy N Siva Mohan;

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  • 年度 2012
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  • 正文语种 en_US
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