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Sintering Characteristic in Catalytic Gasification of China Inner Mongolia Bituminous Coal Ash

机译:内蒙古烟煤催化气化的烧结特性。

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摘要

To determine the ash characteristics, catalysts transformation and the sintering mechanism during catalytic coal gasification, the investigation of the effect of ashing temperature, K2CO3 and CaO catalysts addition on the ash sintering behavior of bituminous coal was conducted under catalytic gasification conditions. The ash sintering temperature was determined at 3.5 MPa using a pressure-drop sintering device with H2O, H-2, CO inlets. The ash morphology was analyzed using a scanning electron microscope-energy dispersive X-ray spectrometer (SEM-EDS). An X-ray diffractometer (XRD) in combination with FactSage were used to predict the reactions occurring between minerals as well as the mineral transformation and slag formation. The results showed that different ashing temperature affected both ash transformation reactions and volatilization amount of added catalyst, which influenced the ash fusion temperatures and the sintering temperature. The ash-550 degrees C was chosen to investigate the sintering behavior. The ash fusion temperatures and the sintering temperature both dropped markedly to a limit value as the concentration of K2CO3 increased and increased again. Besides, the morphology changes from SEM-EDS validated the trend of the sintering temperature, and the molten degree of the tested C-K-S sample was more serious. The sintering happened at several hundred Celsius below the initial deformation temperature; it is more accurate using FactSage to predict slagging compared with the fusion temperatures in catalytic coal gasification process. Furthermore, the FactSage and XRD results revealed that the existence of massive kaliophilite was the main cause of the greatly decreased sintering temperature, the K bearing aluminosilicate could react with Fe, Ca-containing aluminosilicates to form eutectic mixtures, which led to a dramatic drop of the sintering temperature. In addition, the effect of the CaO addition on the slagging property depends on the amount of CaO, reaction condition (pressure, reaction atmosphere) and raw coal property, especially to high iron coal. The existing Fe(II) components easily reacted with the Ca-bearing feldspar minerals to produce low-temperature eutectics and formed the liquid phases, which accelerated the sintering and agglomeration. At last, from the view of K, Ca-containing catalysts transformation using XRD and FactSage calculation, the additional catalyst partly transformed into silica, aluminosilicates and entered into cofusions during sintering, which led to the decreasing catalytic activity and increasing difficulty of catalyst recovery in catalytic coal gasification process.
机译:为了确定催化煤气化过程中的灰分特性,催化剂的转变和烧结机理,在催化气化条件下,研究了灰化温度,K2CO3和CaO催化剂的添加对烟煤灰分烧结行为的影响。使用带有H2O,H-2,CO入口的压降烧结装置,将灰分烧结温度确定为3.5 MPa。使用扫描电子显微镜-能量色散X射线光谱仪(SEM-EDS)分析灰的形态。 X射线衍射仪(XRD)与FactSage结合使用可预测矿物之间发生的反应以及矿物转化和炉渣形成。结果表明,不同的灰化温度对灰分转化反应和添加的催化剂挥发量都有影响,从而影响灰分熔融温度和烧结温度。选择灰分550℃来研究烧结行为。随着K 2 CO 3浓度的增加和增加,灰烬熔化温度和烧结温度均显着下降至极限值。此外,SEM-EDS的形貌变化证实了烧结温度的趋势,并且测试的C-K-S样品的熔融度更加严重。烧结发生在低于初始变形温度几百摄氏度的条件下。与催化煤气化过程中的熔融温度相比,使用FactSage预测结渣更为准确。此外,FactSage和XRD结果表明,块状钾铝辉石的存在是烧结温度大大降低的主要原因,含K的硅铝酸盐可以与含Ca的Fe,Ca铝硅酸盐反应形成共晶混合物,从而导致共晶混合物的急剧下降。烧结温度。另外,CaO的添加对结渣性能的影响取决于CaO的量,反应条件(压力,反应气氛)和原煤性能,特别是对于高铁煤。现有的Fe(II)组分容易与含Ca的长石矿物发生反应,产生低温共晶并形成液相,从而加速了烧结和团聚。最后,从X射线衍射和FactSage计算得出含K,Ca的催化剂转化过程中,额外的催化剂部分转化为二氧化硅,硅铝酸盐,并在烧结过程中发生凝集,导致催化剂活性降低,催化剂回收难度增加。催化煤气化过程。

著录项

  • 来源
    《Energy & fuels》 |2016年第5期|3975-3985|共11页
  • 作者单位

    Enn Technol & Dev Co Ltd, State Key Lab Coal Based Low Carbon Energy, Huaxiang Rd, Langfang 065001, Peoples R China|Tianjin Univ, Sch Chem Engn & Technol, Weijin Rd, Tianjin 300072, Peoples R China;

    Enn Technol & Dev Co Ltd, State Key Lab Coal Based Low Carbon Energy, Huaxiang Rd, Langfang 065001, Peoples R China;

    Enn Technol & Dev Co Ltd, State Key Lab Coal Based Low Carbon Energy, Huaxiang Rd, Langfang 065001, Peoples R China;

    Enn Technol & Dev Co Ltd, State Key Lab Coal Based Low Carbon Energy, Huaxiang Rd, Langfang 065001, Peoples R China|Chinese Acad Sci, Inst Coal Chem, State Key Lab Coal Convers, Taoyuan Rd, Taiyuan 030001, Peoples R China;

    Enn Technol & Dev Co Ltd, State Key Lab Coal Based Low Carbon Energy, Huaxiang Rd, Langfang 065001, Peoples R China;

    Tianjin Univ, Sch Chem Engn & Technol, Weijin Rd, Tianjin 300072, Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
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  • 正文语种 eng
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  • 入库时间 2022-08-18 00:39:57

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