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Treatment of recycle gas for direct thermochemical processing of combustible organic substances of high molecular weight raw materials, and low viscosity liquid fuels

机译:用于直接热化学处理高分子量原料的可燃有机物和低粘度液体燃料的循环气处理

摘要

Process for the direct thermochemical processing of at least one organic reactant high molecular weight organic low molecular weight which are present at room temperature as low viscosity liquids and are combustible, applied as reactant substances and / or mixtures of substances containing carbon macromolecules long chain and / or crosslinked in the form of renewable raw materials as well as residual substances and waste, comprising the steps of: - facilitating reactant fractions less volatile product and at least one reducing gas in a reactor, - sudden heating of reactant in the range of seconds to the reaction temperature of 200 ° C to 600 ° C, - transformation of the reactant to the reaction temperature with use of the reducing action of the gas and / or autocatalytic effects of the fractions of product reaction products in vapor form and gas rEACTION n, - separation of the reaction gas by condensation with products evacuation of condensed reaction gas separate reaction comprising a) if reactants containing oxygen, hydrogen, methane and possibly other hydrocarbons, carbon monoxide and dioxide carbon b) if reactants without oxygen, hydrogen, methane and possibly other hydrocarbons - gas conditioning separate reaction by excluding at least part of the gas mixture and additionally by contribution of hydrogen and / or other substance reducing, in particular in the form of carbon monoxide or tetralin, - renewal of the reaction gas conditioning reactor for the simultaneous generation reducing effect, particularly hydrogenation, for transformation of the reactant and / or a drag effect for product discharge, compressed and preheated reaction gas conditioning before rec onducción the reactor.
机译:用于直接热化学处理至少一种有机反应物高分子量有机低分子量的方法,该有机反应物在室温下以低粘度液体形式存在并且可燃,用作反应物和/或含碳大分子长链的物质的混合物和/或以可再生原料以及残留物质和废物的形式进行交联,包括以下步骤:-在反应器中促进反应物馏分挥发性较小的产品和至少一种还原性气体;-反应物突然加热数秒至反应温度为200°C至600°C,-利用气体的还原作用和/或气相和气体反应形式的产物反应产物馏分的自催化作用将反应物转化为反应温度n, -通过缩合反应气体与产物分离而抽空冷凝的反应气体,分离的反应包括)如果反应物含有氧气,氢气,甲烷和可能的其他碳氢化合物,一氧化碳和二氧化碳b)如果反应物不含氧气,氢气,甲烷和可能的其他碳氢化合物-气体调节通过排除至少一部分气体混合物并另外通过-氢气和/或其他物质的还原,特别是一氧化碳或四氢萘形式的还原的贡献;-反应气体调节反应器的更新,以同时产生还原作用,特别是氢化,以转化反应物和/或阻力作用。用于在反应器重新启动之前对产品进行排出,压缩和预热的反应气调节。

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