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%O 2 和61%N 2 且N 2 纯度的氧化气体的工艺和设备95%和98%之间的水平

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,仅足以溶解全部体积的水。压缩空气中的O 2 以及空气中N2的一部分,其捕获不能从过程中分离出来。之后,部分空气以氧化气体的形式从脱气罐的顶部回收,其中含有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。第二,不同于强制性地要求高水温直到其沸点的现有技术,本发明的工艺脱气可以通过其设备的优选实施方式简单地通过降低设备中的脱气压力来进行。将脱气罐的压力降至大气压以下,以获得相同的氧化性气体。脱气后,工艺用水会保持溶解于每升水中约20 mg的空气,每升水本身溶解,因此不能使用作为完全脱气的水。 3-脱气也可以通过在本专利的目的的第一构造变型中形成的设备通过降低压力并且同时增加温度,或者在两个实施例中将其预先传送到设备中来进行。 -在某些行业中存在,通常用于对水进行完全脱气,在这种情况下,会产生氧化性气体和完全脱气的水。

著录项

  • 公开/公告号WO2018145177A4

    专利类型

  • 公开/公告日2018-10-18

    原文格式PDF

  • 申请/专利权人 JOSÉ DUARTE VIEIRA FRANCISCO;

    申请/专利号WO2017BR50029

  • 发明设计人 JOSÉ DUARTE VIEIRA FRANCISCO;

    申请日2017-02-10

  • 分类号C01B13;B01D19;

  • 国家 WO

  • 入库时间 2022-08-21 12:43:08

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