Slurry bed loop reactor and application thereof
A loop reactor, slurry bed technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems of complex equipment structure, unsuitable for large-scale continuous production, and wear of solid catalyst particles.
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Embodiment 1
[0051] Example 1 illustrates the effect of the slurry bed loop reactor and its application method provided by the present invention.
[0052] The diameter ratio of the air bubble removal zone and the downcomer separation zone of the slurry bed loop reactor is 1.5:1. The filter component used in the downcomer is a sintered porous metal filter tube, and the slurry inlet of the filter component has an inverted cone structure. The cone angle is 45°, the filter tube has an outer diameter of 50 mm, a length of 1000 mm, and an average pore diameter of 1 μm. The particle size range of the catalyst used is 1-100 μm. During this process, the synthesis gas enters the bed layer in the form of bubbling from the bottom of the riser through the double-loop gas distributor, and generates liquid hydrocarbons under operating conditions. When the slurry rises and enters the bubble removal zone 13 on the upper part of the downcomer, the unreacted synthesis gas and gas products are completely sepa...
Embodiment 2
[0056] Example 2 illustrates the effect of the slurry bed loop reactor provided by the present invention on Fischer-Tropsch synthesis with a cobalt-based catalyst.
[0057] with H 2 / CO molar ratio is the syngas of 2 as raw material, and Fischer-Tropsch synthesis produces liquid hydrocarbons. The slurry bed loop reactor and other equipment and experimental steps adopted in Example 2 are the same as in Example 1, except that cobalt-based Catalyst (commercial brand is RFT-410), wherein the mass fraction of cobalt is 20-30wt%, and the pore volume is 0.2-0.45m 3 / g, specific surface area 80-180m 2 / g, the bulk density is 1.2-1.4g / cm 3 , particle size range 40-70μm.
[0058] The operating conditions of the slurry bed reaction zone are as follows: the reaction temperature is 220° C., the absolute pressure is 3.0 MPa, the space velocity is 1.0 NL / g-cat / h, and the catalyst loading is 16% (volume percentage). Under these operating conditions, the one-way conversion rate of CO in the ...
Embodiment 3
[0060] Example 3 illustrates the effect of the slurry bed loop reactor provided by the present invention on the Fischer-Tropsch synthesis of iron-based catalysts.
[0061] with H 2 Syngas with a / CO molar ratio of 0.67 is the raw material for Fischer-Tropsch synthesis to produce liquid hydrocarbons. The slurry bed loop reactor and other equipment and experimental steps used in Example 3 are the same as in Example 1, except that the quenching framework is used. Iron (RQFe-Mn-K) catalyst, the mass fraction of iron is 80wt%, specific surface area is 47m 2 / g, the pore volume is 0.13m 3 / g, the bulk density is 1.05g / cm 3 , particle size range (35-50) μm.
[0062] The operating conditions of the slurry bed reaction zone are as follows: the reaction temperature is 280° C., the pressure is 2.1 MPa, the space velocity is 2.1 NL / g-cat / h, and the catalyst loading is 10% (volume percentage). Under these operating conditions, the one-way conversion rate of CO in the synthesis gas reac...
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Abstract
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