首页> 外国专利> Magnesium bi:sulphite recovery from waste gas leaving lye boiler - esp. in cellulose mfr., by absorbing sulphur di:oxide in magnesium hydroxide soln. (OE 15.4.78)

Magnesium bi:sulphite recovery from waste gas leaving lye boiler - esp. in cellulose mfr., by absorbing sulphur di:oxide in magnesium hydroxide soln. (OE 15.4.78)

机译:从离开碱液锅炉的废气中回收硫酸镁:亚硫酸盐-esp。通过吸收氢氧化镁溶液中的二氧化硫制成纤维素。 (OE 15.4.78)

摘要

The absorption of SO2 in the gas occurs in at least one magnesium sulphite (MS) stage and at least one magnesium bisulphite (MBS) stage. More MS is made than is required for the prodn. of bisulphite, and the excess (E) is removed as MS from the MBS system. Excess (E) corresponds with the difference of the amt. of S in the thick lye and the total bonded S in the tower acid. The MS removed is pref. employed for mfg. H2SO4; or is cracked by heating to obtain MgO recycled to the MBS stage and SO2 fed into the purified bisulphite soln. The MS is pref. cracked at 500-900 degrees C., possibly using some heat from the lye boiler. The MS is pref. dried before craking, which pref. occurs in a stream of SO2, and the resulting SO2 is pref. liquefied. Used in the prodn. of cellulose, using a completely closed circuit for the chemicals, and to produce a digestion acid contg. any desired amt. of SO2 in soln.
机译:气体中SO2的吸收发生在至少一个亚硫酸镁(MS)阶段和至少一个亚硫酸氢镁(MBS)阶段。生成的MS数量超过产品所需的数量。的亚硫酸氢盐,多余的(E)作为MS从MBS系统中除去。过量(E)对应于amt的差异。浓碱液中的S和塔酸中的总键合S。已删除的MS为首选。用于制造。硫酸;或通过加热裂化以获得再循环到MBS阶段的MgO和将SO 2进料到纯化的亚硫酸氢盐溶液中。 MS是首选。可能是使用了碱液锅炉的一些热量在500-900摄氏度下破裂。 MS是首选。干燥后再开裂,这是首选。发生在SO2的流中,并且生成的SO2是优选的。液化的。在产品中使用。使用完全封闭的化学药品回路制造纤维素,并产生消化酸(续)。任何所需的amt。溶液中的二氧化硫含量。

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