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Gasification of solid carbonaceous fuels - slurried in liquid carbon dioxide, by continuous partial oxidation

机译:固体碳质燃料的气化-通过连续部分氧化在液态二氧化碳中制浆

摘要

Synthesis or fuel gas mixts. (constituents CO, CO2, H2, H2O, CH4, H2S, COS, N2, A) are produced by (a) mixing liquid CO2 and a solid particulate carbonaceous fuel at between -69 and +80 degrees F and at a pressure between above the triple point pressure of the CO2 and 1000 psig to produce an H2O-free slurry, (b) introducing the slurry at between-69 and + 1200 degrees F and at 76-4500 psia simultaneously with an O2-contg. (21 mole % O2) gas at 80-500 degrees F and 76-4500 psia into a free-flow noncatalytic gas generator and (c) carrying out partial oxidation of the mixt. at an autogenous temp. of 1200-3000 degrees F and 30-4400 psia. The liquid CO2 serves both as slurrying agent and temp. moderator. The process utilises low cost high-sulphur solid fuel feeds, reduces heat load and consequently oxygen requirements of the gas generator, eliminates heat exchanger fouling, avoids excessive duty and temp. degradation of recoverable heat when using a waste heat boiler, and reduces single-pass carbon waste.
机译:合成或燃气混合物。 (成分CO,CO2,H2,H2O,CH4,H2S,COS,N2,A)通过以下方式生产:(a)在-69至+80华氏度之间且在上述压力之间的压力下混合液态CO2和固体颗粒碳质燃料CO2的三点压力和1000 psig压力产生无H2O的浆料,(b)在-69至+ 1200华氏度和76-4500 psia的压力下将浆料同时引入O2浓度。在80-500华氏度和76-4500 psia下的(> 21摩尔%O2)气体进入自由流动的非催化气体发生器,并且(c)对混合物进行部分氧化。在自然温度下1200-3000华氏度和30-4400 psia。液态CO2既可以用作制浆剂,又可以用作温度。主持人。该方法利用了低成本的高硫固体燃料进料,减少了热负荷,从而降低了气体发生器的氧气需求,消除了热交换器的结垢,避免了过度的负荷和温度。使用废热锅炉时可回收热量的降低,并减少单程碳浪费。

著录项

  • 公开/公告号FR2359891B1

    专利类型

  • 公开/公告日1981-05-22

    原文格式PDF

  • 申请/专利权人 TEXACO DEVELOPMENT CORP;

    申请/专利号FR19760022956

  • 发明设计人

    申请日1976-07-28

  • 分类号C10J3/16;

  • 国家 FR

  • 入库时间 2022-08-22 15:06:57

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