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Process intensification of liquid phase and gas-liquid precipitation of calcium carbonate in narrow channel reactors

机译:窄通道反应器中液相的过程强化和碳酸钙的气液沉淀

摘要

A fundamental study of liquid phase and gas-liquid precipitation of calcium carbonate in narrow channel reactors is presented. Precipitation is strongly dependent on transport rates, as the final product properties are determined by local values of the concentrations during the reaction. The high transport rates available in narrow channels provided the intensification of a precipitation process in this type of equipment. Liquid phase precipitation of calcium carbonate was studied in two square cross section reactors with diagonal lines of I and 2 mm. Flow rates ranging between 0.15 and I CM3/S were used. Mixing efficiency in the narrow channels was characterized with the iodide-iodate reaction scheme. The results showed that mixing efficiency increased with Reynolds number. The mean particle size of calcium carbonate precipitate was found to range between 3 um and 8 um approximately. The narrow channels allowed production of particles similar or smaller in size than in a well stirred batch reactor. Liquid phase precipitation was ftirther characterized by monitoring the change in electrical conductivity, during precipitation, in a narrow channel reactor with embedded electrodes. This system allowed a preliminary study of precipitation rate and limited data on scaling by solid deposits were also obtained. Gas-liquid precipitation of calcium carbonate was studied in a square cross section 2 mm diagonal line narrow channel reactor. The carbonation reaction between a calcium hydroxide solution or suspension andC02 gas was considered. Liquid flow rates between 0.35 and 1.48 CM3/s and carbon dioxide flow rates between I and 8.22 CM3/S were used. Flow patterns for the water-carbon dioxide system were visually characterized. The experimental volumetric mass transfer coefficients for precipitation from a calcium hydroxide solution were found to vary between 0.33 and 0.8 s-1. Particle size and morphology were characterized on selected calcium carbonate samples obtained in both cases from a calcium hydroxide solution and suspension.
机译:提出了对窄通道反应器中碳酸钙的液相和气液沉淀的基础研究。由于最终产物的性质取决于反应过程中浓度的局部值,因此沉淀在很大程度上取决于传输速率。狭窄通道中的高运输速率使这种设备的沉淀过程更加激烈。在两个对角线为I和2 mm的正方形横截面反应器中研究了碳酸钙的液相沉淀。使用的流量在0.15和1 CM3 / S之间。窄通道中的混合效率通过碘化物-碘酸盐反应方案来表征。结果表明,混合效率随雷诺数的增加而增加。发现碳酸钙沉淀物的平均粒度约为3μm至8μm。狭窄的通道允许产生与充分搅拌的间歇反应器中尺寸相似或更小的颗粒。通过在具有嵌入式电极的窄通道反应器中监测沉淀过程中电导率的变化,进一步表征了液相沉淀。该系统允许对降水速率进行初步研究,并且还获得了有关固体沉积物结垢的有限数据。在正方形横截面2 mm对角线窄通道反应器中研究了碳酸钙的气液沉淀。考虑了氢氧化钙溶液或悬浮液与CO 2气体之间的碳酸化反应。使用的液体流速在0.35-1.48 CM3 / s之间,而二氧化碳流速在I-8.22 CM3 / S之间。在视觉上表征了水-二氧化碳系统的流动模式。发现从氢氧化钙溶液沉淀的实验体积传质系数在0.33和0.8 s-1之间变化。对在两种情况下均从氢氧化钙溶液和悬浮液中获得的选定碳酸钙样品进行了粒径和形貌表征。

著录项

  • 作者

    Trippa Giuliana;

  • 作者单位
  • 年度 2006
  • 总页数
  • 原文格式 PDF
  • 正文语种 English
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