Mölder Erik, Mashirin Alelxei, Tenno Toomas
Institute of Physical Chemistry, University of Tartu, Jakobi 2, 51014 Tartu, Estonia.
Environ Sci Pollut Res Int. 2005;12(2):66-70. doi: 10.1065/espr2004.11.223.
GOAL, SCOPE AND BACKGROUND: Gas mass transfer through the liquid-gas interface has enormous importance in various natural and industrial processes. Surfactants or insoluble compounds adsorbed onto an interface will inhibit the gas mass transfer through the liquid-gas surface. This study presents a technique for measuring the oxygen mass transfer through the air-water interface. Experimental data obtained with the measuring device were incorporated into a novel mathematical model, which allowed one to calculate diffusion conduction of liquid surface layer and oxygen mass transfer coefficient in the liquid surface layer.
A special measurement cell was constructed. The most important part of the measurement cell is a chamber containing the electrochemical oxygen sensor inside it. Gas exchange between the volume of the chamber and the external environment takes place only through the investigated surface layer. Investigated liquid was deoxygenated, which triggers the oxygen mass transfer from the chamber through the liquid-air interface into the liquid phase. The decrease of oxygen concentration in the cell during time was measured. By using this data it is possible to calculate diffusional parameters of the water surface layer.
Diffusion conduction of oxygen through the air-water surface layer of selected wastewaters was measured. The diffusion conduction of different wastewaters was about 3 to 6 times less than in the unpolluted water surface. It was observed that the dilution of wastewater does not have a significant impact on the oxygen diffusion conduction through the wastewater surface layer. This fact can be explained with the presence of the compounds with high surface activity in the wastewater. Surfactants achieved a maximum adsorption and, accordingly, the maximum decrease of oxygen permeability already at a very low concentration of surfactants in the solution. Oxygen mass transfer coefficient of the surface layer of the water is found to be Ds/ls = 0.13 x 10(-3) x cm/s.
A simple technique for measuring oxygen diffusion parameters through the air-water solution surface has been developed. Derived equations enable the calculation of diffusion parameters of the surface layer at current conditions. These values of the parameters permit one to compare the resistances of the gas-liquid interface to oxygen mass transfer in the case of adsorption of different substances on the surface layer.
This simple technique may be used for a determination of oxygen permeability of different water-solution surface layers. It enables one to measure the resistance to the oxygen permeability of all inflowing wastewater surface layers in the wastewater treatment plant, and to initiate a preliminary cleaning of this wastewater if required. Similarly, we can measure oxygen permeability of natural waterbodies. Especially in the case of pollution, it is important to know to what extent the oxygen permeability of the water surface layer has been decreased. Based on the tehnique presented in this research, fieldwork equipment will be developed.
目标、范围与背景:气体通过液 - 气界面的传质在各种自然和工业过程中具有极其重要的意义。吸附在界面上的表面活性剂或不溶性化合物会抑制气体通过液 - 气表面的传质。本研究提出了一种测量氧气通过气 - 水界面传质的技术。用该测量装置获得的实验数据被纳入一个新的数学模型,该模型可用于计算液体表面层的扩散传导以及液体表面层中的氧气传质系数。
构建了一个特殊的测量池。测量池最重要的部分是一个内部装有电化学氧气传感器的腔室。腔室内部与外部环境之间的气体交换仅通过所研究的表面层进行。将所研究的液体脱氧,这会引发氧气从腔室通过液 - 气界面进入液相。测量了细胞内氧气浓度随时间的降低情况。利用这些数据可以计算水面层的扩散参数。
测量了选定废水中氧气通过气 - 水表面层的扩散传导。不同废水的扩散传导比未受污染的水面低约3至6倍。观察到废水的稀释对通过废水表面层的氧气扩散传导没有显著影响。这一事实可以用废水中存在高表面活性的化合物来解释。表面活性剂在溶液中浓度很低时就达到了最大吸附量,相应地,氧气渗透率也达到了最大降低值。发现水表面层的氧气传质系数为Ds/ls = 0.13×10⁻³×cm/s。
开发了一种简单的测量氧气通过气 - 水溶液表面扩散参数的技术。推导的方程能够计算当前条件下表面层的扩散参数。这些参数值可用于比较在表面层吸附不同物质的情况下气 - 液界面到氧气传质的阻力。
这种简单的技术可用于测定不同水溶液表面层的氧气渗透率。它能够测量污水处理厂中所有流入废水表面层的氧气渗透阻力,并在需要时对该废水进行初步净化。同样,我们可以测量天然水体的氧气渗透率。特别是在污染的情况下,了解水表面层的氧气渗透率降低到何种程度非常重要。基于本研究提出的技术,将开发现场工作设备。