首页> 外国专利> Granular iron ore direct redn. in blast furnace using natural gas - with high ethane content as source of methane for producing carbon mon:oxide and hydrogen@

Granular iron ore direct redn. in blast furnace using natural gas - with high ethane content as source of methane for producing carbon mon:oxide and hydrogen@

机译:粒状铁矿石直接还原。在使用天然气的高炉中-乙烷含量高的乙烷作为甲烷源,用于产生一氧化碳和氢@

摘要

Direct redn. of granular Fe ore is carried out in a blast furnace with a redn. gas contg. H2 and CO, produced from a CH4-rich gas (I) on an indirectly heated catalyst (II) at 800-1200 deg.C, the top gas from the blast furnace being used (partly) as fuel for indirect heating of (II). The novel features are as follows. Natural gas (III), contg. 50-80 (vol.)% CH4 and 20-45% C2H6 and propane and higher hydrocarbons is compressed to 20-40 bar, cooled to -40 to -80 deg.C in a heat exchange zone and passed to a first separator. A first condensate (IV) contg. C2H6 is discharged from the first separator, partly expanded by a pressure difference of 2-20 bar and passed to a second separator. A CH4 fraction (V) is discharged from the first separator and partly expanded by cooling. (I), contg. at least 75% CH4 and 5-20% C2H6 and having a temp. of -75 to -100 deg.C, is discharged from the second separator. (I) is heated in a heat exchange zone, then heated further and passed over (II). A second condensate (VI) contg. C2H6 is discharged from the second separator and vapourised in the heat exchange zone. ADVANTAGE - The process permits the use (III) with a high C2H6 content and minimis soot formation on (II).
机译:直接重做。粒状铁矿石在高炉中进行氧化还原处理。气续H2和CO,是在800-1200℃的间接加热的催化剂(II)上由富含CH4的气体(I)产生的,高炉炉顶的气体被(部分)用作间接加热(II)的燃料)。新颖特征如下。天然气(续),续将50-80(体积)%的CH 4和20-45%的C 2 H 6以及丙烷和高级烃压缩至20-40bar,在热交换区中冷却至-40至-80℃,并传送至第一分离器。第一冷凝物(IV)续。 C2H6从第一分离器中排出,通过2-20 bar的压差而部分膨胀,并通入第二分离器。 CH4馏分(V)从第一分离器排出,并通过冷却部分膨胀。 (I),续至少75%的CH4和5-20%的C2H6并具有温度-75至-100℃的温度从第二分离器排出。 (I)在热交换区中加热,然后进一步加热并通过(II)。第二冷凝物(VI)续。 C2H6从第二个分离器中排出,并在热交换区中汽化。优点-该方法允许使用具有高C2H6含量且在(II)上形成最小烟灰的(III)。

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