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Method for chemical loop combustion using pyrolusite as an oxide-reducing mass

机译:以软锰矿为还原性氧化物的化学回路燃烧方法

摘要

The method comprises activating a natural manganese mineral by gradually increasing a temperature under an oxidizing atmosphere to a temperature of = 900[deg] C. The step of gradually increasing the temperature is performed at a rate of 5-100[deg] C/hours. The natural manganese mineral is activated in a chemical looping combustion installation. Particles of the natural manganese mineral are fine particle produced during the extraction and the production of metallurgical grade mineral. The natural manganese mineral is crushed and sieved to obtain an active mass with a particle size. The method comprises activating a natural manganese mineral by gradually increasing a temperature under an oxidizing atmosphere to a temperature of = 900[deg] C. The step of gradually increasing the temperature is performed at a rate of 5-100[deg] C/hours. The natural manganese mineral is activated in a chemical looping combustion installation. Particles of the natural manganese mineral are fine particles produced during the extraction and the production of metallurgical grade mineral. The natural manganese mineral is crushed and sieved to obtain an active mass with a particle size compatible with an implementation in a fluidized bed. The active mass has a particle size such that more than 95% of particles of active mass have a size of 150-300 mm. A flow rate of the active mass measured at an inlet of a chemical loop reduction zone is 30-100 kg/hour of oxygen consumed in the reduction zone. The temperature of the reduction zone is 600-1400[deg] C. The reduction reaction is performed in the presence of water vapor.
机译:该方法包括通过在氧化气氛下逐渐升高温度至≥900℃的温度来活化天然锰矿物。以5-100℃/分钟的速率进行逐渐升高温度的步骤。小时。天然锰矿物质在化学循环燃烧装置中被激活。天然锰矿物的颗粒是在冶金级矿物的提取和生产过程中产生的细颗粒。将天然锰矿物粉碎并过筛,以获得具有粒径的活性物质。该方法包括通过在氧化气氛下逐渐升高温度至≥900℃的温度来活化天然锰矿物。以5-100℃/分钟的速率进行逐渐升高温度的步骤。小时。天然锰矿物质在化学循环燃烧装置中被激活。天然锰矿物的颗粒是在冶金级矿物的提取和生产过程中产生的细颗粒。将天然锰矿物粉碎并过筛,以获得活性物质,其粒径与流化床中的实施方案兼容。活性物质的粒径使得超过95%的活性物质的粒径为150-300mm。在化学回路还原区的入口处测得的活性物质的流速为在还原区中消耗的氧气30-100 kg /小时。还原区的温度为600-1400℃。还原反应在水蒸气存在下进行。

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