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2 FT System for preparation of synthetic fuel with slurry bubble column reactor operating in two or more FT modes

机译:2 FT系统,用于以两种或更多种FT模式运行的浆液鼓泡塔反应器来制备合成燃料

摘要

The present invention is a synthetic fuel production apparatus having a slurry bubble column reactor operating in two or more modes; And its use. The slurry bubble column reactor operating in at least two modes (a) Fe: Cu: K : SiO 2 = 100: 1 ~ 10: 1 ~ 20: 10 ~ 50 weight ratio of the Fischer having-Tropsch iron-based catalyst, or for the synthesis (b ) Fischer-Tropsch synthesis iron-based catalyst with 10 to 100% of iron atoms in the phase fraction of ferrihydrite and 0 to 90% of iron atoms in the phase fraction of hematite with respect to 100% of the number of iron atoms, 250℃ ~ 280 Operate in low temperature FT mode at ℃ to produce synthetic fuel containing C 19+ as the first wax amount, and operate in high temperature FT mode at 290 ℃ ~ 350 ℃ to make C 19+ a second wax smaller than the first wax amount. While producing synthetic fuel contained in a large amount, the off-gas emission is greater than that of the low-temperature FT mode, and the synthetic fuel production device is operated in conjunction with the slurry bubble column reactor when operating in the high-temperature FT mode. It is equipped with a combustor, a heat exchanger, a power generator, or a generator that uses gas of high calorific value discharged during operation in the high-temperature FT mode.
机译:本发明是一种具有以两种或更多种模式运行的淤浆鼓泡塔反应器的合成燃料生产设备。及其用途。淤浆鼓泡塔反应器以至少两种模式运行(a)Fe:Cu:K:SiO 2 = 100:1〜10:1〜20:10〜50重量比的具有Tropsch铁基催化剂的Fischer,或合成(b)费-托合成铁基催化剂,相对于铁氧体数量的100%,亚铁酸盐的相分数为10至100%的铁原子,赤铁矿的相分数为0至90%的铁原子250℃〜280的铁原子数在℃下以低温FT模式运行,生产出以C 19 + 为第一蜡含量的合成燃料,并在290℃〜350℃以高温FT模式运行使C 19 + 小于第二蜡的第二蜡。在生产大量包含的合成燃料的同时,废气排放量要比低温FT模式的排放量大,并且当在高温下运行时,合成燃料生产设备与浆料鼓泡塔反应器一起运行FT模式。它配备有燃烧器,热交换器,发电机或使用在高温FT模式下运行时排放的高热值气体的发电机。

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