首页> 外国专利> CONTINUOUS PROCESS AND EQUIPMENT FOR THE PRODUCTION OF OXIDIZING GAS CONTAINING 39 O2 AND 61 N2 BY WEIGHT, WITH N2 HAVING A PURITY LEVEL BETWEEN 95 AND 98

CONTINUOUS PROCESS AND EQUIPMENT FOR THE PRODUCTION OF OXIDIZING GAS CONTAINING 39 O2 AND 61 N2 BY WEIGHT, WITH N2 HAVING A PURITY LEVEL BETWEEN 95 AND 98

机译:连续生产重量为39%的O2和61%N2的氧化气体的工艺和设备,其中N2的纯度在95%和98%之间

摘要

The object of this patent is aimed at the production of OXIDIZING GAS CONTAINING 39% O2 AND 61% N2 BY WEIGHT, WITH N2 HAVING A PURITY LEVEL BETWEEN 95% AND 98%, whereby the water that will be deaerated is previously aerated at temperatures ranging from ambient down to 0° C., under pressures between 20.6 and 31 atm, only enough to dissolve all the volume of O2 in the air that is compressed upon it, along with the portion of N2 of the air, whose capture cannot be dissociated from the process. Afterwards, part of the air is recovered at the top of the deaeration tank, in the form of oxidizing gas, containing 39% O2 and 61% N2 by weight, with N2, which was originally part of the compressed air and was not solubilized in the water, being collected at the top of the aeration or gasification tank showing a purity level between 95% and 98%.;2nd—unlike the State of the Art, which mandatorily requires high water temperature, up to its boiling point, the process degasification, object of the present invention, may be conducted by the preferred embodiment of its pieces of equipment simply by reducing degasification pressure in the degasification tank down to a little bit less than the atmospheric pressure to obtain the same oxidizing gas, and, following degasification, the process water keeps about 20 mg of air, per liter of water, dissolved in itself and, therefore, cannot be used as totally deaerated water.;3—degasification may also be carried out by equipment as formed in the first construction variant of the object of this patent by reducing pressure and, at the same time, increasing the temperature, or sending it, in both embodiments, to the equipment, pre-existing in certain industries, which is used to fully deaerate water and, in these cases, produce the oxidizing gas and fully deaerated water.
机译:该专利的目的在于以重量计生产包含39%O 2 和61%N 2 的氧化气体,其中N 2 纯度在95%和98%之间,从而将要脱气的水预先在环境温度至0°C的温度下,在20.6至31 atm的压力下充气,仅足以溶解所有体积的O压缩空气中的 2 以及空气中N 2 的一部分,它们的捕获不能与过程分离。之后,部分空气以氧化气体的形式在脱气罐顶部被回收,按重量计包含39%的O 2 和61%的N 2 , N 2 ,最初是压缩空气的一部分,不溶于水,收集在曝气或气化罐顶部,纯度在95%到98%之间。与强制要求高水温直至其沸点的现有技术不同,本发明的第二个目的是通过其设备的优选实施方式简单地通过减少脱气来进行工艺脱气,这是本发明的目的。脱气罐中的压力降低到比大气压低一点,以获得相同的氧化性气体,脱气后,工艺用水保持每升水约20 mg空气溶解在其自身中,因此不能; 3—脱气也可能是完全脱气的水。在这两个实施例中,通过降低压力并同时提高温度或将其发送到在某些行业中已经存在的设备,通过在本专利的目的的第一构造变型中形成的设备来执行该任务,用于完全脱气的水,在这种情况下,会产生氧化性气体和完全脱气的水。

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号