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FLASHCHAIN Theory for Rapid Coal Devolatilization Kinetics. 11. Tar Hydroconversion during Hydrogasification of Any Coal

机译:FLASHCHAIN快速脱挥发分动力学理论。 11.任何煤的加氢气化过程中的焦油加氢转化

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This paper introduces a FLASHCHAIN-based reaction mechanism for oils production during tar hydroconversion with any coal for any hydrogasification conditions. Oils are generated by the hydrogenation of tar monomers in two stages. In the first stage, the tar monomers released as primary tars are rapidly hydrogenated into oils at the monomer hydrogenation rate. Since elevated pressures always shift primary tar molecular weight distributions toward lighter species, monomers constitute substantial fractions of primary tar, and as much as one-half the ultimate oils yield is produced soon after the onset of tar hydroconversion. In the second stage, additional tar monomers are gradually released by hydrocracking of larger tar molecules and then hydrogenated into oils, while control of the oils production rate shifts from monomer hydrogenation to hydrocracking. Oil yields are uniform with H-2 pressures higher than 1 MPa because rates of monomer hydrogenation and hydrocracking accelerate for progressively higher H2 pressures to compensate for diminishing primary tar yields. Predicted oil yields grow for progressively hotter temperatures. The analysis shows that aliphatic tar components must be incorporated into oils along with their aromatic nuclei during monomer hydrogenation and constitute one-half or more of the oils yield at the highest H2 pressures. Primary tar composition and, especially, their structural components determine the maximum oil yields from different coals. The sample-to-sample variability in primary tar yields is apparent in their associated oil yields. In combination, the mechanisms for hydropyrolysis, tar hydroconversion, and char hydrogasification accurately interpreted a database representing coals of rank from lignite to anthracite, heating rates from 1 to 10(4) degrees C/s, temperatures from 475 to 900 degrees C, coal contact times from 1 to 900 s, gas contact times from 2 to 42 s, and H2 pressures from 0.3 to 15 MPa.
机译:本文介绍了一种基于FLASHCHAIN的反应机理,用于在任何加氢气化条件下与任何煤进行焦油加氢转化过程中的石油生产。油是通过两个阶段的焦油单体加氢生成的。在第一步中,作为初级焦油释放的焦油单体以单体氢化速率迅速氢化为油。由于升高的压力总是使伯油的分子量分布向较轻的物质移动,因此单体占伯油的主要部分,并且在焦油加氢转化后不久就产生了最终油产量的一半。在第二阶段,通过将较大的焦油分子加氢裂化逐渐释放出更多的焦油单体,然后将其氢化成油,而对油的生产速率的控制则从单体加氢转变为加氢裂化。 H-2压力高于1 MPa时,油的产量是均匀的,因为单体加氢和加氢裂化的速率会随着H2压力的逐渐升高而加速,以补偿初级焦油产量的降低。随着温度的逐渐升高,预计的石油产量会增加。分析表明,脂肪族焦油组分必须在单体加氢过程中连同其芳族核一起掺入油中,并在最高H2压力下占油产量的一半或更多。焦油的主要成分,尤其是其结构成分决定了不同煤的最大含油量。初级焦油产率的样品间差异在其相关的油产率中很明显。结合起来,加氢热解,焦油加氢转化和焦化气化的机理可以准确地解释一个数据库,该数据库代表了褐煤至无烟煤的等级煤,升温速率为1至10(4)℃/ s,温度为475至900℃,煤接触时间为1到900 s,气体接触时间为2到42 s,H2压力为0.3到15 MPa。

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  • 来源
    《Energy & fuels》 |2018年第7期|7569-7584|共16页
  • 作者

    Niksa Stephen;

  • 作者单位

    Niksa Energy Associates Ltd Liabil Co, 1745 Terrace Dr, Belmont, CA 94002 USA;

  • 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);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-18 00:39:10

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