Shunt down method of fixed bed Fischer-Tropsch synthesis process
A Fischer-Tropsch synthesis, fixed-bed technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, petroleum industry, etc., can solve the problems of catalyst damage and difficult replacement of heavy hydrocarbons, and achieves reduction of temperature runaway, reduced temperature Adverse influence, effect of smooth shutdown
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Embodiment 1
[0024] In this example, a tubular fixed-bed reactor is used, and cobalt loaded with metal oxide is used as a Fischer-Tropsch synthesis catalyst. The Fischer-Tropsch synthesis reaction conditions are: reaction pressure 3.0MPa, catalyst bed average temperature 215°C, H 2 The molar ratio of feed to CO and CO is 2, and the hourly space velocity of syngas is 750h -1 , The ratio of recycle gas to fresh feed gas (cycle ratio) is 4.
[0025] When the reactor needs to be shut down, keep the average temperature of the catalyst bed at 215°C, cut in nitrogen (oxygen volume fraction less than 0.5%), cut out the raw material gas, and keep the gas hourly space velocity at 750h -1 , the cycle ratio is kept at 4. After 12 hours of replacement, the liquid level of the high-pressure separator has no obvious change, and the combustible gas (H 2 +CO) volume fraction is less than 0.1%, the cycle compressor is stopped, and the liquid level of the high and low pressure separators drops to a low le...
Embodiment 2
[0027] In this embodiment, a tubular fixed-bed reactor is used, and cobalt loaded with metal oxide is used as a Fischer-Tropsch synthesis catalyst, and part of the light synthetic oil is recycled back to the reactor inlet. The Fischer-Tropsch synthesis reaction conditions are: reaction pressure 3.0MPa, catalyst bed average temperature 210°C, H 2 The molar ratio of feed to CO is 2, and the hourly space velocity of syngas is 700h -1 , The space velocity of light synthetic oil entering the reactor is 0.5h -1 , The ratio of recycle gas to fresh feed gas (cycle ratio) is 3.
[0028] When the reactor needs to be shut down, keep the average temperature of the catalyst bed at 210°C, cut in nitrogen (oxygen volume fraction less than 0.5%), cut out the raw material gas, and keep the gas hourly space velocity at 700h -1 , to maintain the space velocity of light synthetic oil entering the reactor at 0.5h -1 , the cycle ratio is kept at 3. Subtract 0.25h per hour after replacement for ...
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