Combined Fischer-Tropsch synthesis wastewater treatment system and method thereof
A technology for Fischer-Tropsch synthesis wastewater and wastewater treatment system, which is applied in hydrogen/synthesis gas production, chemical instruments and methods, inorganic chemistry, etc. consumption and cost effects
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[0034] In another embodiment of the present invention, the Fischer-Tropsch synthetic wastewater enters the Fischer-Tropsch synthetic wastewater treatment reactor from the Fischer-Tropsch synthetic wastewater feed port arranged at the bottom of the Fischer-Tropsch synthetic wastewater treatment reactor, and the Fischer-Tropsch synthetic wastewater treatment reaction In the device, the liquid phase flows upwards and reacts in contact with the water-phase reforming catalyst in the second reaction zone. The reaction effluent I is waste water after treatment, which is exported from the middle outlet of the Fischer-Tropsch synthesis wastewater treatment reactor, and the outlet is arranged at Between the two reaction zones; in the Fischer-Tropsch synthetic wastewater treatment reactor, the generated gas phase flows upwards and contacts with the shift catalyst in the first reaction zone to react, and the reaction effluent II flows from the top of the Fischer-Tropsch synthetic wastewater...
Embodiment 1
[0050] This embodiment adopts figure 1 A combined Fischer-Tropsch synthetic wastewater treatment system. In the Fischer-Tropsch synthesis wastewater treatment reactor, the diameter ratio of the first reaction zone and the second reaction zone is 1:2, and the volume ratio of the loaded catalyst is 1:2. The first reaction zone is filled with a Cu-Zn system shift catalyst, and the second reaction zone is filled with a Pt system water phase reforming catalyst.
[0051] The Cu-Zn series shift catalyst is prepared by co-precipitation method, and its chemical composition is CuO:ZnO:Al 2 o 3 The ratio is 33:47:20. After precipitation, aging, washing, drying, and roasting, the catalyst is finally shaped into flake-shaped particles of 3mm×3mm.
[0052] The preparation method of the Pt series water phase reforming catalyst is as follows: the first step is to prepare the carrier, get 100 grams of pseudo-boehmite, mix with 1.5 gram of nitric acid (concentration 65%), 2 gram of carbon bl...
Embodiment 2
[0056] This embodiment adopts figure 2 A combined Fischer-Tropsch synthetic wastewater treatment system. In the Fischer-Tropsch synthesis wastewater treatment reactor, the diameter ratio of the first reaction zone and the second reaction zone is 2:3, and the volume ratio of the loaded catalyst is 1:2. The first reaction zone is filled with a Cu-Zn system shift catalyst, and the second reaction zone is filled with a Pd system water phase reforming catalyst.
[0057] The Cu-Zn series shift catalyst is prepared by co-precipitation method, and its chemical composition is CuO:ZnO:Al 2 o 3The ratio is 33:47:20. After precipitation, aging, washing, drying, and roasting, the catalyst is finally shaped into flake-shaped particles of 3mm×3mm.
[0058] The preparation method of the Pd series water phase reforming catalyst is as follows: the first step is to prepare the carrier, dissolve 3 grams of nitric acid, 96 grams of aluminum nitrate, and 80 grams of sodium metasilicate in 2 lit...
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