Method for extracting biphenyl and indole from recycling washing oil of coal oil
A technology for coal tar and oil washing, which is applied in the field of purification of biphenyl and indole, can solve problems such as not seen, and achieve the effects of low production cost, high product yield, and improved reuse value.
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Embodiment 1
[0026] The raw material is rectified under the condition of vacuum degree of 74Kpa, theoretical plate number of rectification column of 40, and reflux ratio of 8 to enrich the indole biphenyl fraction, and obtain a biphenyl content of 27.3% and an indole content of 6.42%. indole biphenyl fraction. Then by indole biphenyl fraction: triethylene glycol: the mass ratio of n-heptane is 1: 0.5: 1 to carry out extraction, indole content is 20.53% in the indole extraction liquid after three-stage cross-flow extraction, and indole extraction rate 85.6% %. The indole extract is carried out rectification and purification under the condition that the vacuum degree is 74Kpa, the theoretical plate number of the rectification column is 40, and the reflux ratio is 8, and the indole product with a purity of 95.2% is obtained, and its single-pass yield is 85.6%. The triethylene glycol content is 98%, and the recovery rate is 95%. The biphenyl raffinate after extraction recovers n-heptane thro...
Embodiment 2
[0028] The indole biphenyl fraction enriched by rectification in Example 1 was extracted according to the mass ratio of indole biphenyl fraction:ethanolamine:n-hexane of 1:1:1. After the three-stage cross-flow extraction, the indole content in the indole extract was 21.63%, and the indole extraction rate was 89.6%. With regard to the indole extract, the rectification and purification are carried out under the conditions that the vacuum degree is 74Kpa, the theoretical plate number of the rectification column is 40, and the reflux ratio is 8, and the indole product with a purity of 95.4% is obtained, and its single-pass yield is 88.6%. The solvent ethanolamine content is 98%, and the recovery rate is 96%. The extracted biphenyl raffinate is simply distilled to recover n-hexane, with a purity of 99.5% and a recovery rate of 97%, for recycling; continue to operate under the conditions of a vacuum of 75KPa, a theoretical plate number of the rectification column of 40, and a reflux...
Embodiment 3
[0030] The raw material is rectified and enriched indole biphenyl fraction at a vacuum degree of 80Kpa, the theoretical plate number of the rectification tower is 40, and the reflux ratio is 6, and the indole biphenyl fraction with a biphenyl content of 27.07% and an indole content of 4.01% is obtained. Benzene fraction. Then carry out the six-stage countercurrent extraction process according to the mass ratio of indole biphenyl fraction: triethylene glycol: n-heptane in the ratio of 1:0.5:1. After extraction, the indole content is 17.98%, and the indole extraction rate is 98.2%. The indole extract is subjected to rectification and purification under the condition that the vacuum degree is 74Kpa, the theoretical plate number of the rectification column is 40, and the reflux ratio is 10, and the indole product with a purity of 95.2% is obtained, and its single-pass yield is 78.6%. The triethylene glycol content is 98%, and the recovery rate is 95%. The biphenyl raffinate recov...
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