Method for purifying materials containing metal impurities
A technology for metal impurities and materials, applied in the field of heteroatom purification, can solve the problems of improved iron removal effect, increased bed pressure drop, and too fast pressure drop of catalyst bed, etc.
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Embodiment 1
[0022] Gasoline fraction iron removal process.
[0023]During the processing process, the gasoline fraction is polluted by iron impurities, the content of which is 32 μg / g in terms of iron element, the flash gas (low fraction gas) of the low-pressure separator is the low fraction gas of the catalytic cracking gasoline hydrotreating unit, and the volume content of hydrogen sulfide is 3.4%, the pressure is 0.7MPa. Experimental schemes 1-1 and 1-2 use a catalyst, which is the residual oil hydrogenation protection agent FZC-102 (Raschig ring, diameter 5mm) developed and produced by Fushun Petrochemical Research Institute. Embodiments 1-3 use alumina particles (Raschig ring, outer diameter 5mm, inner diameter 2.5mm, height 6mm, diameter of the most probable pore of alumina is 15nm). Experimental schemes 1-4 are the same alumina particles as schemes 1-3, and the alumina particles contain 2wt% potassium oxide. Adopt the inventive method to process, specifically according to the att...
Embodiment 2
[0027] Diesel fraction iron removal process.
[0028] Diesel fractions contain iron impurities and are contaminated by iron impurities during processing. The iron content is 85 μg / g. The flash gas (low fraction gas) of the low-pressure separator is the low fraction gas and hydrogen sulfide of the catalytic cracking diesel hydrotreating unit. The volume content is 6.5%, the pressure is 1.0MPa, and the catalyst adopts residual oil hydrogenation protection agent FZC-101 (seven-hole ring, outer diameter 16mm), FZC-102 (Raschig ring, diameter 5mm) developed and produced by Fushun Petrochemical Research Institute. ), the volume ratio is 1:2, packed in layers, the diesel raw material is first contacted with FZC-101, then with FZC-102, and processed by the method of the present invention, specifically according to the attached figure 1 Process operation. In the comparative example, the operating conditions are the same as those of the experimental mode 2-1, except that instead of usi...
Embodiment 3
[0032] Demetallization process of vacuum distillate oil (distillation range 379~540℃).
[0033] The content of various impurities is 12 μg / g of iron, 25 μg / g of calcium, and 22 μg / g of sodium. The flash gas (low fraction gas) of the low-pressure separator is the low fraction gas of the vacuum distillate oil hydrocracking unit, and the volume content of hydrogen sulfide is 5.1%, the pressure is 1.5MPa, the catalyst adopts residual oil hydrogenation protection agent FZC-100 (seven-hole ball, outer diameter 16mm), FZC-101 (seven-hole ring, outer diameter 16mm) developed and produced by Fushun Petrochemical Research Institute, FZC-102 (Raschig ring, diameter 5mm), the volume ratio is 1:2:2, packed in layers, the diesel raw material is firstly contacted with FZC-100, and then with FZC-101 and FZC-102, using the method of the present invention processing, according to the attached figure 2 Process operation. The specific conditions and results are shown in Table 3.
[0034] Tabl...
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