首页> 外国专利> Continuous process and equipment to produce gas oxidizing with 39 and 61 of N2, O2 and N2 content by weight with purity of between 95 and 98

Continuous process and equipment to produce gas oxidizing with 39 and 61 of N2, O2 and N2 content by weight with purity of between 95 and 98

机译:连续工艺和设备生产的气体氧化的N2,O2和N2含量为39%至61%(重量),纯度在95%至98%之间

摘要

Continuous process and equipment to produce gas oxidizing with 39% and 61% of N2, O2 and N2 content by weight with purity of between 95% and 98%.The object of this patent has as objective the production of gas fuel, with 39% and 61% of N2, O2 and N2 with weight content of purity between 95% and 98%.Where the water to be di airing is pre aerated at temperatures from ambient to 0 u00b0 C at pressures between 20.6 and 31 ATM.Which is just sufficient to dissolve all the volume of O2 contained in the volume of the compressed air about her, along with part of the N2 from air, whose capture is inseparable from the process; after that,Part of this air is recovered at the top of the tank deaeration, in the form of gas fuel, with 39% O2 and 61% N2, by weight,With the N2 which was part of the compressed air and which was not solubilized in the water is collected at the top of the aeration tank or gasification.In the levels of purity between 95% and 98%; 2, unlike the current state of the art by which is essential to the elevation of the temperature of the water to its boiling point.The degassing of the process object of this patent can be carried out by the preferential version of its equipment only by reducing the pressure gasification.It is reduced in the tank degassing, a little less than atmospheric, to obtain the same gas oxidizer, and water that circulates in the process.After degassing has about 20 mg per litre of water air dissolved therein, and can not be used as the water completely Di airing.
机译:以39%和61%的重量比生产纯度为95%至98%的N2,O2和N2的气体氧化的连续工艺和设备。该专利的目的是生产39%的气体燃料以及61%的N2,O2和N2的重量含量在95%到98%之间,其中要进行除水处理的温度是在20.6到31 ATM的压力下从环境温度到0摄氏度进行充气的。足以溶解她周围压缩空气中所含的所有O2以及空气中的一部分N2,而该气体的捕集与该过程是分不开的;之后,部分空气以气体燃料的形式在罐式脱气的顶部以气体燃料的形式被回收,其中O2和N2的重量比为39%,其中N2是压缩空气的一部分,而并非压缩空气。溶解在水中的气体收集在曝气池或气化炉的顶部。纯度在95%到98%之间;如图2所示,不同于当前的技术水平,这对于将水的温度升高至其沸点是必不可少的。该专利的工艺对象的脱气只能通过其设备的优先版本通过降低温度来实现。在罐内脱气时要减少压力,使其比大气少一点,以获得相同的气体氧化剂和过程中循环的水。脱气后每升水中溶解约20 mg空气,不能完全当水用作迪风。

著录项

  • 公开/公告号BR102017002528A2

    专利类型

  • 公开/公告日2018-09-25

    原文格式PDF

  • 申请/专利权人 FRANCISCO JOSÉ DUARTE VIEIRA;

    申请/专利号BR20171002528

  • 发明设计人 FRANCISCO JOSÉ DUARTE VIEIRA;

    申请日2017-02-07

  • 分类号B01D19;

  • 国家 BR

  • 入库时间 2022-08-21 12:53:59

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