A diisopropyl ether-based high-concentration phenol-containing wastewater extractant and extraction method
A diisopropyl ether, high-concentration technology, applied in chemical instruments and methods, extraction water/sewage treatment, water pollutants, etc., to achieve the effect of large operating flexibility range, low solubility, and easy control
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Embodiment 1
[0030] The high concentrated coal chemical simulation of the deductions of wastewater, with a total ghetin content of 6500 mg / L, a cell phenol content of 4000 mg / L, polyphenol content 2500 mg / L. The 3-stage countercurrent extraction was performed using an extraction crop experimental method, wherein the extractant is a synergist (a volume fraction of 50% of the diisopropyl ether + volume fraction of 50% is mixed for 90 min, and stands for 120 min. The extraction temperature was 60 ° C, the extraction pH is 7, the volume ratio of the extractant and the phenolic wastewater is 1: 5.5.
[0031] The total phenol content of the phenol after extraction is less than 200 mg / L, wherein the unit phenol is less than 0 mg / L, and the polyphenols are less than 200 mg / L; total phenol, phenol and polyphenol deletion reach 96.9%, 100%, 92.0%, respectively. .
Embodiment 2
[0033] High concentrated coal chemical simulation of wastewater to be treated, with a total gyne content of 6000 mg / L, a phenol content of 2000 mg / L, and a polyphenol content of 4000 mg / L. The 5-stage countercurrent extraction was performed using an extraction cascade experiment method, wherein the extractant is a synergist (a volume fraction of 10%) of a diisopropyl ether + volume fraction of 90% orthopentyl alcohol. The mixture is stirred for 30 min, and stands for 90 min. The extraction temperature was 60 ° C, the extraction pH is 5, the volume ratio of the extractant and the phenolic wastewater is 1: 2.
[0034] The phenolic glyph content of the phenol was 0 mg / L after extraction, wherein the cell phenol 0mg / L, polyphenols 0 mg / L; total phenol, phenol and polyphenol removal rate reached 100%, 100%, 100%, respectively.
Embodiment 3
[0036] High concentrated coal chemical simulation of wastewater treatment, with a total ghenol content of 12,000 mg / L, a phenol content of 6000 mg / L, and a polyphenol content of 6000 mg / L. 6-stage countercurrent extraction was carried out by a collateral experiment method, wherein the extractant is a synergist (a volume fraction of 40% diisopropyl ether + volume fraction of 60% n-and-pentanol), mixed with stirring for 50 min, standing for 50 min, The extraction temperature was 60 ° C, the extraction pH is 6, and the volume ratio of the extractant and the phenolic wastewater is 1: 6.
[0037] The total phenolic gap level after extraction was less than 60 mg / L, wherein the cell phenol 0 mg / L, polyphenols were less than 60 mg / L; total phenol, cell phenol, and polyphenol removal rates reached 99.5%, 100%, 99.0%, respectively.
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