Slurry reactor reaction system and method for Fischer-Tropsch synthesis reaction
A reaction system, Fischer-Tropsch synthesis technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, chemical/physical processes, etc., can solve problems such as test failure, increase in proportion, and decrease in yield of target products to ensure Yield, improved heat transfer efficiency, improved safety effects
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[0042] According to a preferred embodiment of the present invention, 20-70% of the heat exchange tubes of the internal heat exchange unit are provided with baffles.
[0043] According to a preferred embodiment of the present invention, the internal heat exchange unit includes a lower heat exchange unit 2, a middle heat exchange unit 3 and an upper heat exchange unit 4 arranged inside the slurry bed reactor 1;
[0044] The lower heat exchange unit 2, the middle heat exchange unit 3 and the upper heat exchange unit 4 each independently comprise more than two heat exchange tubes connected in parallel, and part or Baffles are arranged in all the heat exchange tubes, and the baffles are used to prolong the residence time of the heat exchange medium in the internal heat exchange unit;
[0045] The lower heat exchange unit 2 , the middle heat exchange unit 3 and the upper heat exchange unit 4 are connected in series and / or in parallel.
[0046] With the above settings, the system ca...
Embodiment 1
[0100] This example is used to illustrate the slurry bed reaction system and the Fischer-Tropsch synthesis reaction method of the present invention.
[0101] use figure 1 In the slurry bed reaction system shown, the Fischer-Tropsch synthesis feed gas (synthesis gas) is introduced from the lower part of the slurry bed reactor 1, and then reacts on the surface of the catalyst in the environment of liquid wax, and the gas produced after the reaction is released from the slurry state. The top of the bed reactor flows out to the downstream for separation, and the heater 7 makes the temperature rise rate of the flowing water 20°C / h; when the temperature in the slurry bed reactor 1 reaches 120°C, the heater 7 is set so that the flowing water The temperature rise rate is 10°C / h; when the temperature in the slurry bed reactor 1 reaches 200°C, set the heater 7 so that the temperature rise rate of the water passing through is 5°C / h; When it reaches 250°C, it is deemed to have reached th...
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