首页> 外国专利> Process for converting synthesis gas to liquid hydrocarbons in the presence of a Fischer Tropsch Catalyst, with Improvement of the mass and Energy Transfer in the mixing zone with high Shear stress

Process for converting synthesis gas to liquid hydrocarbons in the presence of a Fischer Tropsch Catalyst, with Improvement of the mass and Energy Transfer in the mixing zone with high Shear stress

机译:在费-托催化剂存在下将合成气转化为液态烃的方法,改善了高剪切应力混合区的质量和能量传递

摘要

1.A process for the conversion of synthesis gas to hydrocarbons, characterized in that it comprises contacting the synthesis gas with high temperature and pressure with a catalyst comprising a suspension of Solid Particles Suspended in a liquid medium.Contact that occurs in a system comprising at least one area of high Shear Mixing and reaction Vessel such that the volume of suspension present in the area (S) with high Shear mixing is substantially reduced the volume of suspension P Present in the Reaction vessel.The suspension was mixed with synthesis gas in the area (S) with high Shear mixing.The resulting mixture of the suspension and the synthesis gas is discharged from the area (S) with high Shear mixing in the Reaction vessel and such that Kinetic Energy is dissipated to the suspension present in the area (S) of blended with a high shear rate po R at least 0.5 kW / m3 for the total volume of suspension present in the system.
机译:1,一种将合成气转化为碳氢化合物的方法,其特征在于,它包括使高温和高压下的合成气与包含悬浮在液体介质中的固体颗粒悬浮液的催化剂接触。高剪切混合和反应容器的至少一个区域,以使存在于高剪切混合的区域(S)中的悬浮液体积大大减少反应容器中存在的悬浮液P的体积。在高剪切混合下,将悬浮液和合成气的混合物从区域(S)排出,并将动能耗散到存在于该区域(S)的悬浮液中。 S)以高剪切速率po R混合,对于系统中存在的悬浮液总体积至少为0.5 kW / m3。

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