首页> 外国专利> METHOD OF PRODUCTION OF GRANULATED OXYGEN-CONTAINING BLEACHING AGENT ON BASE OF PEROXOSOLVATE OF SODIUM CARBONATE AND DEVICE FOR REALIZATION OF THIS METHOD

METHOD OF PRODUCTION OF GRANULATED OXYGEN-CONTAINING BLEACHING AGENT ON BASE OF PEROXOSOLVATE OF SODIUM CARBONATE AND DEVICE FOR REALIZATION OF THIS METHOD

机译:基于碳酸钠过氧溶剂的粒状含氧漂白剂的生产方法及实现该方法的装置

摘要

FIELD: chemical industry.;SUBSTANCE: proposed method includes delivery of aqueous solution of hydrogen peroxide and soda from reservoirs of 1 and 2 to reactor 3. Reaction mass thus obtained is delivered to double-screw mixer 6 communicated with drier 7. Part of dried granules is returned from drier 7 to mixer 6 and other part is directed to classifier 8; fraction at size of particles from 0.1 to 1.00 mm is directed from intermediate part of said classifier to storage reservoir 9 for target fraction granules. Then, granules are fed to vacuum drier in the scope of no more than 50% of its inner volume. Solution preparation unit 37 is used for preparation of aqueous solution of stabilizing agent- sodium, sodium sulfate, sodium carbonate, sodium silicate or their mixtures. Concentration of stabilizing agent solution is 5-15 mass-% and volume is 0.215-0.235 of volume of granules. Vacuum drier 11 and measuring reservoir 10 are evacuated simultaneously to residual pressure not exceeding 13.33 kPa. Granules are evacuated at heating to 55°C and are mixed with stabilizing agent solution first in vacuum followed by jumpwise rise of pressure to atmospheric level or to excessive pressure of 10 kPa; procedure is continued for 0.5-1.0 min. Then vacuum drying is performed at constant or periodic mixing. Moisture content of finished product doe not exceed 1.05% at stability of 59.93-65.74%.;EFFECT: enhanced efficiency.;12 cl, 1 dwg, 1 tbl
机译:领域:拟议的方法包括将过氧化氢和苏打水溶液从1和2的储罐中输送到反应器3中。如此获得的反应物料输送到与干燥机7连通的双螺杆混合器6中。颗粒从干燥器7返回混合器6,另一部分直接进入分级器8。从所述分级机的中间部分将粒度为0.1至1.00mm的颗粒从所述分级器的中间部分引导至用于目标部分颗粒的储存器9。然后,将颗粒以不超过其内部容积的50%的范围进料到真空干燥器中。溶液制备单元37用于制备稳定剂-钠,硫酸钠,碳酸钠,硅酸钠或其混合物的水溶液。稳定剂溶液的浓度为5-15质量%,体积为颗粒体积的0.215-0.235。同时将真空干燥器11和测量容器10抽空至残余压力不超过13.33 kPa。将颗粒在加热至55℃时抽真空,并首先在真空中与稳定剂溶液混合,然后将压力突然升高至大气压或超过10 kPa;继续进行0.5-1.0分钟。然后在恒定或周期性混合下进行真空干燥。成品的水分含量不超过1.05%,稳定性为59.93-65.74%。;效果:提高了效率; 12 cl,1 dwg,1 tbl

著录项

  • 公开/公告号RU2264977C2

    专利类型

  • 公开/公告日2005-11-27

    原文格式PDF

  • 申请/专利权人

    申请/专利号RU20040101648

  • 申请日2004-01-20

  • 分类号C01B15/10;B01J8/18;F26B5/04;F26B19/00;

  • 国家 RU

  • 入库时间 2022-08-21 21:21:50

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