Method for removing phenoxy compounds in solvent oil
A technology for removing solvents and compounds, applied in the direction of refining with an alkaline aqueous solution, can solve the problems of harsh process conditions, high equipment requirements, high construction investment and production costs, and achieve simple process flow, high activity, and low production costs. Effect
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Embodiment 1
[0026] Embodiment 1. The method of the present invention is used to remove phenolic oxygen compounds from solvent oil whose distillation range is 120° C. to 150° C. and whose content of phenolic oxygen compounds is 87 ppm. The schematic diagram of the process flow is as attached figure 2 As shown, 6 is a baffled tubular oil-alkali mixing reactor with oblique corrugated plates inside; 7 is a pre-dephenolization reactor with wire mesh packing on the upper layer and oblique corrugated packing on the lower layer, and the height ratio of the upper and lower layers of packing is 1:1.2. And the oil-water settling tank, the specification model is φ1500×5000; 8 is the hydrocyclone, the specification model is φ1600×4000; 9 is the coalescence high-efficiency dehydrator, the model is 4AQL1650CH19P3-CC7027; 10 is the fixed bed reactor, the specification model It is φ1000×6000, filled with high-efficiency adsorbent. The active component of the adsorbent is the ionic salts of certain metals...
Embodiment 2
[0030] Embodiment 2, for the solvent oil whose distillation range range is 120~150°C and phenolic oxygen compound content is 68ppm, the processing capacity is 15t / h, the reaction temperature is 50°C, and the reaction pressure is 0.4MPa, and other conditions are the same as in Example 1. The phenolic oxygen compound content of the product solvent oil obtained at the distillation outlet of the refined dephenolization fixed-bed reactor (10) is below 3.8ppm, and the product is colorless and odorless. It is tested according to the method of GB / T 3555, and the characteristic number of Saibo is not less than + 30.
Embodiment 3
[0031] Embodiment 3, for the solvent oil whose distillation range range is 120~150°C and phenolic oxygen compound content is 64ppm, the processing capacity is 13t / h, the reaction temperature is 40°C, the reaction pressure is 0.2MPa, the alkali concentration is 5%, add The amount is 30%, and other conditions are the same as embodiment 1, and the phenolic oxygen compound content of the product solvent oil obtained at the distillation outlet of the fine dephenolization fixed-bed reactor (10) is below 1.0ppm, and the product is colorless and tasteless, according to GB / T 3555 Method for detection, Saibo characteristic number is not less than +30.
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