Separation method for phenol compounds in oil
A technology for separation of phenolic compounds and separation methods, applied in the separation of aromatic hydrocarbon mixtures, in the field of phenols, can solve the problems of complex post-treatment process, consumption of large acid-base solution, pollution of the environment, etc., achieve low separation cost and prevent phenol-containing wastewater , the effect of avoiding environmental pollution
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Embodiment 1
[0033] This example illustrates the great advantages of the new method over industrial methods.
[0034] The industrial sodium hydroxide solution elution method uses a sodium hydroxide solution with a mass fraction of 10% to 15% for washing, and 40ml of a 15% sodium hydroxide solution is added to 20ml of simulated oil (97.67g / L toluene solution with phenol ), stirring for 20min. After the lower water phase was evaporated to remove oil for 30 minutes, 10 ml of sulfuric acid solution with a mass fraction of 60% was added to acidify, the recovery rate of phenol was 95%, sodium hydroxide, sulfuric acid solution was not recyclable, and 38 ml of phenol-containing wastewater was produced.
[0035] The process conditions illustrated in this embodiment are: phenol is dissolved in toluene to prepare a simulated oil solution, the concentration is 97.67g / L, and the quaternary ammonium salt is choline chloride (HOEt(Me) 3 NCl), the molar ratio of choline chloride to phenol in the tolu...
Embodiment 2
[0041] The process conditions illustrated in this embodiment are: phenol is dissolved in toluene to prepare a simulated oil solution, the concentration is 97.67g / L, the quaternary ammonium salt is choline chloride, the molar ratio of phenol in choline chloride to toluene solution is 0.8, and the separation temperature The temperature is 50°C, and the stirring time is 15 minutes.
[0042] At 50°C, 2.893g of choline chloride was added to 20ml of oil solution, stirred for 15 minutes and then allowed to stand for 5 minutes. The volume and phenol content of the upper oil phase were measured, and the removal rate of phenol was 89.0%.
[0043] The upper oil phase was removed, and the lower eutectic phase was vacuum-dried at 80°C for 1 h. After cooling, 20 ml of ether was added, stirred for 15 min, then allowed to stand for 5 min, and choline chloride was recovered after centrifugation and drying.
[0044]
Embodiment 3
[0046] The process conditions described in this embodiment are: phenol is dissolved in toluene to prepare a simulated oil solution, the concentration is 97.67g / L, the quaternary ammonium salt is choline chloride, the molar ratio of phenol in the choline chloride to toluene solution is 1, the separation temperature 0°C, stirring time 15min.
[0047] At 0°C, 2.893g of choline chloride was added to 20ml of oil solution, stirred for 15 minutes and then allowed to stand for 5 minutes. The volume and phenol content of the upper oil phase were measured, and the removal rate of phenol was 86.0%.
[0048]The upper oil phase was removed, and the lower eutectic phase was vacuum-dried at 80°C for 1 h. After cooling, 20 ml of ether was added, stirred for 15 min, then allowed to stand for 5 min, and choline chloride was recovered after centrifugation and drying.
[0049]
PUM
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