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Have you seen the differences? 712-HOUR GAS

机译:你看到差异了吗? 712小时燃气

摘要

Case 72-9818+ Canada Process for separating SO2 from a current of gas, with production of sulphuric acid by the nitric oxide process A process for separating SO2 from a current of gas, with production of sulphuric acid by the nitric oxide process in a tower system is described, in which the SO2-containing gas is introduced into a denitration zone and, after passing through the latter at a nitric oxide concentration of at least 1 % by volume in the gas phase,onward into an SO2-processing zone comprising at least one packed tower, in which it is brought into intimate contact with sulphuric acid containing less than 70 % by weight of H2SO4 (dilute acid, the acid being used to absorb the nitrogen oxides in the towers downstream from the SO2-processing zone having a concentration of between 70 and 85 % by weight of H2SO4 (absorption acid): this process is improved bya) heating the nitrose-containing acid intended for the denitration zone which, relative to the direction of gas flow, is located upstream from the first tower, trickle-fed with dilute acid, of the SO2-processing zone, by indirect heat exchange to above 60.degree.C before it comes into contact with the gas stream which leaves the denitration zone, andb) holding the sojourn time of the gas between leaving the denitration zone and entering the first tower of the nitric oxide absorption zone, at concentrations of at least S % by volume o SO2 and at least 10 V/o by volume of .degree.2 in the gas entering the denitration zone, at less than 30 seconds, and, at lower SO2 contents or lower O2 contents in the said entry gas, limiting the residence time to a maximum length calculated from the equation in which formula Zmax is the sojourn time in seconds, ¢SO2! denotes the SO2 content in the gas entering the denitration zone, in % by volume, and ¢O2! denotes the oxygen content in the same entry gas, in % by volume.
机译:案例72-9818 + Canada从一股气流中分离SO2的过程,通过一氧化氮过程生产硫酸从一股天然气中分离出SO2的过程,通过塔中的一氧化氮过程生产硫酸描述了一种系统,其中将含SO 2的气体引入脱硝区,并且在以至少一体积%的一氧化氮浓度在气相中通过脱硝区之后,再进入包含至少一个脱硝区的SO 2处理区。至少一个填充塔,其中它与含少于70%(重量)H2SO4的硫酸(稀酸)紧密接触,稀酸用于吸收SO2处理区下游塔中氮氧化物,该硫酸具有浓度为70%至85%(重量)的H2SO4(吸收性酸):通过以下方法可以改善此过程:a)加热用于脱硝区的含硝酸的硝酸,相对于气流方向为1在间接接触到离开脱硝区的气流之前,通过间接热交换至高于60°C的方式,在SO2处理区的第一塔上游滴入稀酸,并用稀酸进料,并且b)保持气体从脱硝区到进入一氧化氮吸收区的第一塔之间的停留时间,SO2浓度至少为S%(体积),o2的体积至少为10V / o。气体进入脱硝区的时间少于30秒,并且在上述进入气体中的SO2含量较低或O2含量较低时,将停留时间限制为最大长度,该方程式中公式Zmax为停留时间(以秒为单位) ,¢SO2!表示进入脱硝区的气体中的SO2含量(以体积%计)和¢O2!表示相同进入气体中的氧气含量,以体积%计。

著录项

  • 公开/公告号SE7602528L

    专利类型

  • 公开/公告日1976-09-13

    原文格式PDF

  • 申请/专利权人 CIBA-GEIGY AG;

    申请/专利号SE19760002528

  • 发明设计人 FATTINGER V;

    申请日1976-02-26

  • 分类号C01B17/82;

  • 国家 SE

  • 入库时间 2022-08-23 02:41:06

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