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Calcination of hydrated alumina in a rotary kiln - has kiln fired by stoichiometric mixt. of natural gas and oxygen@ burner, provides alumina for electrical insulators

机译:回转窑中水合氧化铝的煅烧-采用化学计量混合法烧成的窑。天然气和氧气@燃烧器,为电绝缘子提供氧化铝

摘要

Process for the calcination of hydrated alumina in a kiln at a mean temp. of 1000-1700 deg.C, opt. in the presence of calcination aid, operates kiln using a burner supplied with mixt. of oxygen and natural gas. The oxygen-natural gas mixt. is stoichiometric, the kiln is a rotary kiln, and the hydrated alumina which is calcined, has a sodium oxide content of 0.07-0.6 wt.% and a water content of 0.5 to 35 wt.%, based on the hydrated alumina. Pref., 0.1-3 wt.% of a calcination aid is added. USE/ADVANTAGE - Used in the mfr. of high grade alumina for electrical insulators. The disadvantages of previous processes, viz. a high level of entrainment of alumina dust in the off-gas and the discharge of nitrogen oxides, are prevented and the process is economical to operate. In an example, hydrated alumina (throughput: 165 kg/hour) with a average grain size of 80 microns, a water content of 2 wt.%, a specific surface of 150 m2/g, and a sodium oxide content of 0.25 wt.%, was mixed with a small amt. of boric acid (throughput: 850 g/hour) as a calcination aid and calcined in a rotary kiln for 18 minutes at a average temp. of 1450 deg.C. The kiln burner was fed with 14 Nm3/hour natural gas and 28 Nm3/hour oxygen. The amt. of dust produced was 3.8 wt.%, and the nitrogen oxides content of the off-gas was less than 0.02 g/rai
机译:在平均温度下在窑炉中煅烧水合氧化铝的方法。选择1000-1700摄氏度在煅烧助剂的存在下,使用配有混合料的燃烧器运行窑炉。氧气和天然气。氧气-天然气混合物。如果是化学计量的,则该窑是回转窑,并且基于水合氧化铝,煅烧的水合氧化铝的氧化钠含量为0.07-0.6重量%,水含量为0.5至35重量%。优选添加0.1-3重量%的煅烧助剂。使用/优势-在mfr中使用。用于绝缘子的高级氧化铝。先前过程的缺点,即。防止了废气中高水平的夹带氧化铝粉尘和氮氧化物的排放,并且该方法操作经济。在一个实例中,水合氧化铝(产量:165kg /小时)具有80微米的平均粒度,2重量%的水含量,150m2 / g的比表面积和0.25重量%的氧化钠含量。 %,与少量amt混合。硼酸(处理量:850克/小时)作为煅烧助剂,并在回转窑中以平均温度煅烧18分钟。 1450摄氏度窑炉中的天然气为14 Nm3 /小时,氧气为28 Nm3 /小时。 AMT。产生的粉尘为3.8 wt。%,废气中的氮氧化物含量小于0.02 g / rai

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