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PRODUCTION OF TAR FROM BRIQUETTE COKING

机译:用焦糖炼焦油生产焦油

摘要

1383988 Coke briquettes FMC CORP 14 Sept 1972 [15 Sept 1971] 42652/72 Heading C5E Coke briquettes are made from coal by (a) reacting coal particles with oxygen at above 250‹ F., shock heating the resulting particles to tardistilling temperatures to produce a char and a tar distillate, further heating the char to produce a calcinate having a non-condensible volatiles content of up to 3% and containing at least 1% hydrogen and cooling the calcinate; (b) treating the tar with oxygen to produce an oxygenated pitch; (c) briquetting the calcinate with the oxygenated pitch and heating the green briquettes in the presence of oxygen to induce an exothermic reaction and cure the briquettes; and (d) coking the cured briquettes at 1400- 1600‹ F. while recirculating the volatiles driven off and producing additional tar which is separately blown with air at a temperature above the boiling point of water to produce a pitch having a softening point above 120‹ F. and blending this pitch with the mixture to be briquetted in step (c). As shown cured briquettes from step (c) are heated in zone 12 of a kiln 10 by hot gases from the zone 14, the briquettes then pass through the hot zone 14 and through the cooling zone 16. Heat for the hot zone 14 is provided by a burner 18 fed with air 20, gas 22 and recycle gas 40. The volatiles from the heating are passed through a dry cyclone 28, a scrubber 30 and a wet cyclone 32 from which a tar 34 is recovered. The tar 34 is blown with air at 250-300‹ F. before being incorporated in the briquettes.
机译:1383988焦炭压块FMC CORP 1972年9月14日[1971年9月15日] 425/72标题C5E焦炭压块由煤制成,方法是:(a)使煤颗粒与氧气在250°F以上的温度反应,将所得颗粒骤热加热至焦油蒸馏温度,以生产焦炭和焦油馏出物,进一步加热焦炭,以生产出不凝性挥发物含量最高为3%且含有至少1%氢的煅烧产物,并冷却该煅烧产物; (b)用氧气处理焦油以产生氧化沥青; (c)以氧化沥青将煅烧物压块,并在氧气存在下加热生坯,以引起放热反应并固化该坯块; (d)在1400-1600°F下使固化的团块焦化,同时再循环除去的挥发物,并产生另外的焦油,在空气中以高于水沸点的温度分别吹入焦油,以产生软化点高于120的沥青。 ‹F。并将该沥青与步骤(c)中待压块的混合物混合。如图所示,来自步骤(c)的固化的团块在窑10的区12中被来自区14的热气体加热,然后,团块通过热区14和冷却区16。为热区14提供热量。通过加热到燃烧器18的空气20,气体22和再循环气体40。来自加热的挥发物通过干燥的旋风分离器28,洗涤器30和湿旋风分离器32,从中回收焦油34。在掺入团块之前,将焦油34在250-300°F下吹入空气。

著录项

  • 公开/公告号AU457987B2

    专利类型

  • 公开/公告日1975-02-13

    原文格式PDF

  • 申请/专利权人

    申请/专利号AU19720046128

  • 发明设计人

    申请日1972-08-30

  • 分类号C10B49/02;C10C3/04;C10L5/16;

  • 国家 AU

  • 入库时间 2022-08-23 04:17:25

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