首页> 外文会议>International Technical Conference on Clean Coal and Fuel Systems;Clearwater Clean Coal Conference >PARAMETRIC AND DYNAMIC STUDIES OF AN IRON-BASED 25 KWTH COAL DIRECT CHEMICAL LOOPING UNIT USING SUB-BITUMINOUS COAL
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PARAMETRIC AND DYNAMIC STUDIES OF AN IRON-BASED 25 KWTH COAL DIRECT CHEMICAL LOOPING UNIT USING SUB-BITUMINOUS COAL

机译:利用亚沥青煤的铁基25夸酚直接化学循环单元的参数和动态研究

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The iron-based Coal-Direct Chemical Looping (CDCL) combustion process is an alternative to conventional oxy-combustion technologies, where the oxygen used for fuel conversion in the CDCL process is provided by an iron-oxide oxygen carrier instead of an air separation unit. The iron oxide is reduced using coal in the reducer reactor, producing highly-pure CO_2 in the flue gas, and the reduced iron oxide is regenerated in a separate combustor reactor using air. The CDCL process at Ohio State has been developed and demonstrated in a 25-kWth sub-pilot unit, and it is the first chemical looping demonstration unit with a circulating moving bed reactor for solid fuel conversion. To date, the CDCL sub-pilot unit at OSU has been operated for more than 680 hours, with a 200-hour continuous operation, providing important data on long term operability as well as parametric optimization. The feasibility of the sub-pilot unit with various types of solid fuels including metallurgical coke fines, biomass, bituminous coal, sub-bituminous coal and lignite coal has been tested. This paper discusses recent parametric operational experience with sub-bituminous coal as the fuel, where dynamic changes in variables were performed to observe the effects on the unit itself. Measurements include temperature, pressure, and gas concentrations from the reducer and combustor. Furthermore, effects of different variables, such as flue gas recycle ratios (enhancer gas flow rates), feed port injection, and temperature, are observed. Tests confirmed high coal conversions with high purity of CO_2 achieved in the flue gas. Overall, the moving bed design of the reducer results in nearly full coal conversion with a high purity of CO_2, eliminating the need for additional down-stream fuel polishing and/or separation units. The combustor gas contained lean oxygen concentrations with minute amounts of carbonaceous gases (CO_2, CO and CH_4) detected, indicating proper regeneration of the oxygen carrier as well as good gas sealing between the reducer and combustor.
机译:铁煤基直接化学链(CDCL)燃烧过程是常规的氧燃烧的技术,其中,用于在CDCL过程燃料转化的氧被铁氧化物氧载体,而不是空气分离单元提供了一种替代的。氧化铁使用在还原剂反应器的煤,产生的烟道气中高纯度CO_2减小,并且还原铁氧化物,使用空气在一个单独的燃烧器反应器再生。在俄亥俄州的CDCL过程已经开发并在25 kWth子导频单元表明,它是所述第一化学环路示范单元与循环移动床反应器,用于固体燃料转化率。迄今为止,在OSU的CDCL子导频单元已经被操作为680多小时,用200小时的连续运转,在长期操作性以及参数优化提供重要的数据。子导频单元的与各种类型的固体燃料,包括冶金焦炭粉,生物质,烟煤,次烟煤和褐煤的可行性已通过测试。本文讨论了亚烟煤为燃料,其中变量的动态变化进行观察单元本身的影响最近参数的操作体验。测量包括温度,压力,和从所述减速器和燃烧器气体的浓度。此外,不同的变量,例如烟道气的循环比(增强剂气体流速),进料口注入,和温度的效应,观察到。试验证实高的煤转化与CO_2的高纯度的烟气中实现。总体而言,移动床设计在接近满煤转化与CO_2的高纯度的减速结果,消除了对额外下游燃料抛光和/或分离单元的需要。燃烧器气体含有含碳气体(CO_2,CO和CH_4)的微量贫氧浓度检测,表明氧载体的适当的再生以及减速和燃烧器之间的良好气封。

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