Denitrifying agent for directly removing basic nitrogen compound from shale oil
A shale oil and basic nitrogen technology, applied in the petroleum industry, refined hydrocarbon oil, etc., can solve problems such as troublesome operation, easy swelling, limited exchange capacity, etc., and achieve simple removal process, obvious removal effect, and high sedimentation speed fast effect
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Embodiment 1
[0015] Example 1 with 2.0g CuSO 4 ·5H 2 Dissolve O with 3.4g of water, add 94g of phosphoric acid (85%), mix well and then add 0.5g of demulsifier three-dimensional network maleic acid / olefin copolymer to compound into denitrification agent. Take Daqing shale oil as raw material, the ratio of solvent to oil is 1:100, stir at 65°C for 10 minutes, keep at 65°C and settle for 180 minutes, separate the nitrogen residue settled at the bottom of the flask from the upper shale oil, After refining, the alkali nitrogen content of shale oil drops to 1776ppm, and the alkali nitrogen removal rate is 53.0%. The acidity of shale oil before refining is 77.8mgKOH / 100mL, and the acidity of shale oil after refining is 87.9mgKOH / 100mL.
Embodiment 2
[0016] Example 2 (Comparative Example) The feed ratio and reaction conditions are the same as in Example 1, except that no demulsifier is added. After the same experimental operation as in Example 1, it is found by analysis that the acidity of the refined shale oil is 166.2 mgKOH / 100mL, compared with the acidity of shale oil before refining, the acidity of refined shale oil increased a lot without adding demulsifier, indicating that the residual denitrification agent did not settle down completely in shale oil, and the denitrification agent in the page Emulsified in rock oil, poor settling effect.
Embodiment 3
[0017] Embodiment 3 will 2.0g CuSO 4 ·5H 2 Dissolve O with 3.4g of water, add 94g of phosphoric acid (85%), mix well and then add 0.5g of demulsifier three-dimensional network maleic acid / olefin copolymer to compound into denitrification agent. Take Daqing shale oil as raw material, the ratio of solvent to oil is 1:50, stir at 65°C for 10 minutes, keep at 65°C and settle for 180 minutes, separate the nitrogen residue settled at the bottom of the flask from the upper shale oil, After refining, the alkali nitrogen content of shale oil drops to 506ppm, and the alkali nitrogen removal rate is 86.6%.
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