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Site hydroisomerization of synthetic hydrocarbon liquid in Tropsch reactor - slurry Fischer

机译:Tropsch反应器中合成烃液体的现场加氢异构化-费休浆液

摘要

In hydrocarbon synthesis reactor, in a slurry Fischer-Tropsch hydrocarbon synthesis process for synthesizing the liquid hydrocarbons from synthesis gas, in the downcomer reactor in one or more immersed in the slurry body in the synthesis reactor, It also performs the hydroisomerization of synthetic hydrocarbon liquid containing slurry liquid. Preferably, the monolithic catalyst is used in the hydroisomerization. At least some circulation of slurry from the slurry body down around through the downcomer reactor is achieved by density difference driving liquid pressure. The density difference driving liquid pressure is effected by removing from the slurry sent to the down tube, the gas bubbles. Preferably, before the slurry is in contact with the catalyst, I do also removal of the catalyst particles. hydroisomerization occurs without synthesis reactor while continuing to produce a hydrocarbon, to inhibit the hydrocarbon synthesis reaction. [Selection] Figure Figure 1
机译:在烃合成反应器中,在用于从合成气中合成液态烃的费托烃合成法的浆液中,在降液管反应器中将一或多个浸入合成反应器的浆体中,还进行合成烃液的加氢异构化含有浆液。优选地,整体催化剂用于加氢异构化中。通过密度差驱动液体压力实现了至少一部分浆料从浆料主体向下通过降液管反应器的循环。通过从送入下管的浆料中除去气泡来实现密度差驱动液体压力。优选地,在淤浆与催化剂接触之前,我也要除去催化剂颗粒。加氢异构化在没有合成反应器的情况下发生,同时继续产生烃,以抑制烃合成反应。 [选择]图图1

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