流化固定床分离烟草粉尘与砂粒杂质的工艺研究

Arief Rahmatulloh, S. Santosa, Anang Takwanto, Atika Nabilla
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引用次数: 0

摘要

烟草粉尘是卷烟厂的副产品。烟草粉尘上以铁砂(磁铁矿)和二氧化硅形式存在的杂质约占10 - 20% (wt%),使烟草粉尘属于有害物质。烟草粉尘中砂杂质浓度阈值小于5% (wt%)。流化固定床分离是降低烟草粉尘杂质含量的方法之一。采用重量法对流态化前后的烟草粉尘进行了分析,探讨了分离工艺对烟砂杂质浓度的影响。烟灰原料砂杂质浓度为28.47;32.38;35.32% (wt%)。流化床固定床分离的最佳气流速度为0.61 m/s。该速度在120分钟的时间内产生的烟草粉尘中,砂杂质最小,为4% (wt%)。分离过程后(497 cm ~ 493 cm和939 cm ~ 925 cm)的FTIR波数相减表示砂杂质浓度的减量。此外,Fe-O-Si相互作用的损失表明,从烟草粉尘中成功地降低了沙杂质浓度。Keywords-Tobacco尘埃;磁铁矿;二氧化硅;分离;流化床固定。
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Separation Process of Tobacco Dust from Sand Impurities by Fluidized Fixed Bed
Tobacco dust is by-product of cigarette factory. The existence of impurities on tobacco dust in the form of iron sand (magnetite) and silica for about 10 – 20% (wt%) makes tobacco dust belong to hazardous material. The threshold of sand impurities concentration on Tobacco dust is less than 5% (wt%). One of the methods able to reduce the impurities of tobacco dust is separation process using fluidized fixed bed. Tobacco dusts before and after fluidized were analyzed with gravimetric method to find out the effect of separation process on the sand impurities concentration. The sand impurities concentrations on raw material of tobacco dusts are 28.47; 32.38; and 35.32% (wt%). Further, the optimum gas flow velocity for separation process using fluidized fixed bed was achieved at 0.61 m/s. That velocity generated tobacco dust with the smallest sand impurities at 4% (wt%) in 120 minutes time operation. The subtraction of FTIR wavenumber after separation process (497 cm to 493 cm and 939 cm to 925 cm ) was denoted as the decrement of sand impurities concentration. Moreover, the loss of Fe-O-Si interaction indicated that the sand impurities concentration was successful to be reduced from the tobacco dust. Keywords—Tobacco dust; Magnetite; Silica; Separation; Fluidized bed fixed.
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