Denitrification method for aromatics raffinate oil
A raffinate oil and denitrification technology, which is applied in the field of aromatic raffinate oil and aromatic raffinate oil denitrification, can solve the problems of increased cost of aromatic raffinate oil denitrification, loss of adsorption activity of activated clay, and environmental pollution.
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Embodiment (1~10
[0015] Nitrogen removal of aromatic raffinate in a size of carried out in a stainless steel tubular fixed-bed reactor. 100 g of sulfonic acid-based cation exchange resin is filled in the reactor, and the particle size of the resin is 0.40-1.25 mm. The outside of the reactor is equipped with an electric heating temperature control system, and temperature measuring platinum resistors are respectively installed on the upper, middle and lower parts of the resin bed. The amount of reaction feed is controlled by a feed pump, and the system pressure is regulated by a back pressure valve. The total nitrogen content in the aromatic raffinate oil used as the raw material is 10 mg / kg, and the neutral test is alkaline; the total nitrogen content in the aromatic raffinate oil after denitrification is ≤0.5 mg / kg, and the neutral test is qualified. The indicators of the catalyst are shown in Table 1, and the conditions and results of each embodiment are shown in Table 2.
Embodiment 11
[0023] The resin saturated with adsorbed morpholine is soaked in sulfuric acid solution with 3 times the volume concentration of 4-5 wt% for 2 hours, then washed with deionized water until pH = 7, and then dried. The regenerated strongly acidic cation exchange resin is then subjected to denitrification reaction. The conditions and results are shown in Table 3. The regenerated mass exchange capacity is the same as that of the fresh one.
[0024] table 3
[0025]
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