Method for preventing sedimentation of catalyst in slurry bed reactor and slurry bed reaction device
A reaction device and slurry bed technology, applied in the field of Fischer-Tropsch synthesis, can solve problems such as increased distributor resistance, inability to increase production load, distributor blockage, etc.
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[0055] Under normal circumstances, both the main cycle compressor and the auxiliary cycle compressor are operating normally. The main cycle compressor enters synthetic gas (2.88MPa, 35°C), which is compressed and boosted by the main cycle gas compressor to 3.35MPa, 68°C, and the auxiliary cycle compresses The decarbonized gas at the inlet of the machine is 2.75MPa, 40°C, and after being compressed by the auxiliary cycle compressor, the pressure is boosted to 3.35MPa, 68°C. The synthetic gas compressed by the main cycle gas compressor is heated to 205°C through the heat exchanger, and the pressure is 3.2MPa. The raw material gas from the purification unit at 3.2MPa, 220°C, and total sulfur content <0.05ppm is mixed with the circulating synthesis gas at 3.2MPa, 205°C, and enters the distributor at the bottom of the reactor. The synthesis gas entering the slurry bed reactor (R-6101) passes through the slurry bed layer containing the catalyst in the form of bubbling to carry out t...
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