Method for preparing ethylene by hydrogenation of acetylene and reaction tower used in the method
A technology of acetylene hydrogenation and reaction tower, which is applied in the fields of hydrogenation to hydrocarbons, chemical instruments and methods, organic chemistry, etc., and can solve problems such as difficulty in removing heat from overheating reactions, difficulty in uniform mixing of liquid and solid, and easy blockage of gas distributors. , to achieve the effect of solving mercury pollution, expanding the coal chemical industry route, and avoiding the overheating of the fixed bed
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Embodiment 1
[0031] A method for preparing ethylene by hydrogenating acetylene, including the following steps:
[0032] 1) Pack the granular catalyst evenly on the tray, and purge the reaction pipeline and equipment with inert gas. After the oxygen content is qualified, the liquid phase solvent N-methyl-2-pyrrolidone is pumped in from the liquid phase inlet And it moves from top to bottom. When the liquid level at the bottom of the reaction tower reaches 50%, the liquid phase solvent is continuously extracted from the liquid phase outlet, sent to the regeneration or heat exchange unit for processing, and then returned to the liquid phase inlet for recycling.
[0033] Switch the nitrogen to a mixture of hydrogen and acetylene with a volume ratio of 5:1, pressurized by the compressor, enter from the gas phase inlet of the lower part of the reaction tower, distribute through the gas distributor, and move from bottom to top in the reaction tower;
[0034] 2) The gas and liquid phases come into contac...
Embodiment 2
[0040] The invention relates to a reaction tower used in a method for hydrogenating acetylene to produce ethylene. The reaction tower is a gas-liquid-solid three-phase mass transfer device, the diameter of the reaction tower is 600mm, and the total height is 5m. Such as Figure 1-3 As shown, the structure includes tower body 1, liquid phase inlets and outlets 7, 4, gas phase inlets and outlets 3, 8, trays 5, gas distributor 2, gas-liquid separator 9, and downcomer 6;
[0041] Among them, the tray 5 is provided with 10 layers with a distance of 300mm; it includes an overflow port 11, a liquid receiving tray 10 and a reaction unit; the reaction unit is equipped with a plurality of spray devices 12, the spray device includes a gas riser 15 and spray Cover 14, the opening rate of the spray device is 13%. The gas riser 15 is conical, hollow, with a small head facing upwards, and 50mm high; the spray hood 14 has a conical structure, with spray holes evenly opened on the upper part, an...
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