首页> 外国专利> PROCESS FOR OBTAINING SODIUM CARBONATE FROM CARBON DIOXIDE RESULTING FROM THE AIR AND COMBUSTION GASES BY MEANS OF ABSORPTION WITH A SODIUM HYDROXIDE SOLUTION FOR ACQUIRING CARBON CREDITS.

PROCESS FOR OBTAINING SODIUM CARBONATE FROM CARBON DIOXIDE RESULTING FROM THE AIR AND COMBUSTION GASES BY MEANS OF ABSORPTION WITH A SODIUM HYDROXIDE SOLUTION FOR ACQUIRING CARBON CREDITS.

机译:通过用氢氧化钠溶液吸收来获得碳信用而从空气和燃烧气体中获得的二氧化碳中的碳酸钠的方法。

摘要

The present invention consists in a process for obtaining sodium carbonate from carbon dioxide resulting from the air and combustion gases from burners and inner combustion engines that use fossil fuels; the process uses an absorption by a chemical reaction with sodium hydroxide in order to acquire carbon credits according to the Kyoto Protocol related to the climate change and the byproduct marketing. The process is performed in an horizontal pulveriser absorber including coupling sections of 1 m and dispersion nozzles of ¼" for the absorption liquid which is an hydroxide sodium solution at 8%. The absorber has an affordable minimum industrial size, with a diameter of 0.85% m and three rows of nozzles, one in the upper portion and the remaining two rows located at the side portions in order to form a 90° angle with regard to the first row. Each row has 5 nozzles separated 20 cm one from each other, 15 nozzles per section. The sodium carbonate of the absorbing solution is concentrated up to the saturation point by means of flowing the same back to the deposit of the absorption liquid and restoring the consumed sodium hydroxide. Once the sodium carbonate is concentrated, it is heated in a heat exchanger and then crystallised in a basket crystalliser for separating the crystals, these latter elements being washed with water and dried with hot air for finally being milled down to the desired commercial size.
机译:本发明在于一种方法,该方法用于从由使用化石燃料的燃烧器和内燃机的空气和燃烧气体产生的二氧化碳中获得碳酸钠。该过程使用与氢氧化钠的化学反应进行吸收,以根据与气候变化和副产品销售有关的《京都议定书》获得碳信用额。该过程在卧式粉碎机吸收器中进行,该吸收器包括1 m的耦合段和1/4“的分散喷嘴,用于8%的氢氧化钠溶液的吸收液。该吸收器的最小工业尺寸可承受,直径为0.85% m和三排喷嘴,其中一个位于上部,其余两排位于侧面,以便与第一排形成90°角,每排有5个喷嘴,彼此间隔20厘米,每节15个喷嘴,吸收液的碳酸钠通过流回吸收液的沉淀并恢复消耗的氢氧化钠的方式浓缩至饱和点,将碳酸钠浓缩后加热在换热器中,然后在篮式结晶器中结晶以分离出晶体,随后的这些元素用水洗涤并用热空气干燥,最后研磨成粗粉。商业规模。

著录项

  • 公开/公告号MX2010010186A

    专利类型

  • 公开/公告日2012-03-20

    原文格式PDF

  • 申请/专利权人 ROBERTO TOMAS MIKLOS ILKOVICS;

    申请/专利号MX20100010186

  • 发明设计人 ROBERTO TOMAS MIKLOS ILKOVICS;

    申请日2010-09-20

  • 分类号C07C69/96;

  • 国家 MX

  • 入库时间 2022-08-21 17:23:52

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