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High-phenol concentration waste water treatment method

A treatment method and technology for phenol wastewater are applied to the treatment of phenol-containing wastewater and the treatment of high-concentration volatile phenol-containing wastewater, which can solve the problems of solvent loss, weak extraction ability of the extractant, high solubility, etc. Excellent extraction effect, low solubility effect

Active Publication Date: 2016-05-04
GUANGDONG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the solubility of methyl isobutyl ketone in water is 2%, and the residual amount and organic residue amount in waste water are relatively high, which is easy to cause solvent loss and secondary pollution. Solvent regeneration has an important impact on economy and technology
[0005] Chinese patent 20121014513.7 discloses the use of isopropyl ether, isopropyl butyl ketone, and methyl tert-amyl ether as extractants for extraction and dephenolization. First, acid gas is used to saturate the wastewater to reduce the pH value, and then the dephenol extraction agent is used Carry out dephenolization treatment, and finally use single-tower pressurized stripping to carry out deacidification, deamination and solution stripping. The disadvantages of this method are: the extraction ability of the extractant is weak, the energy consumption is too high, the price is high, and the process is complicated, which directly leads to the treatment of waste water. Inefficient and cost prohibitive
[0006] To sum up, in the current prior art, when using extractant to extract and dephenolize volatile phenols, the extraction and dephenolization rate is low; while using high-efficiency extractant, the solubility of the solvent in water is large, the energy consumption of solvent recovery is high, and the loss Large, increasing operating costs

Method used

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Experimental program
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Effect test

Embodiment 1

[0038] The phenol-containing wastewater with a concentration of 5000mg / L is first passed through the grid to remove impurities, and then the eucalyptol and phenol-containing wastewater are placed in the extraction vessel at a volume ratio of 1:1. Stir for 5 minutes, and separate layers in a constant temperature tank at a temperature of 10°C. After standing still for 60 minutes, separate the raffinate phase in the lower layer. The content of phenol in the raffinate phase is measured by gas chromatography. The extraction dephenolization rate is 96.2%.

Embodiment 2

[0040] Put the phenol-containing wastewater with a concentration of 20,000 mg / L first through the grid to remove impurities, and then put the eucalyptol and phenol-containing wastewater in the extraction vessel at a volume ratio of 1:4, and place them on a magnetic stirrer at 25°C Stir for 10 minutes, and separate layers in a constant temperature bath at 25°C. After standing still for 30 minutes, separate the lower raffinate phase. The phenol content in the raffinate phase is measured by gas chromatography. The dephenolization rate is 94.7%.

Embodiment 3

[0042] The phenol-containing wastewater with a concentration of 40000mg / L was first passed through the grid to remove impurities, and then the eucalyptol and phenol-containing wastewater were placed in the extraction vessel at a volume ratio of 1:8. Stir for 15 minutes, and separate layers in a constant temperature tank at a temperature of 40°C. After standing for 15 minutes, separate the raffinate phase in the lower layer. The content of phenol in the raffinate phase is measured by gas chromatography. The extraction dephenolization rate is 91.1%.

[0043] For specific chromatograms, see figure 1 It is the gas chromatogram before the extraction of 40000ppm phenol-containing wastewater; wherein, 1.42min is the ethanol peak (internal standard), and 4.54min is the phenol peak; figure 2 Be that concentration is the gas chromatogram after 40000ppm phenol-containing waste water is extracted with eucalyptus alcohol, explanation: 1.45min is ethanol peak (internal standard), 4.4min i...

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Abstract

The invention discloses a high-phenol concentration waste water treatment method. The high efficiency and economic phenol-containing waste water extraction method comprises 1, removing impurities of high-phenol concentration waste water, 2, putting eudesmol and the high-phenol concentration waste water treated through the step 1 into an extraction container according to a volume ratio of 1: 1-10, carrying out fast stirring at a temperature of 10-50 DEG C for 5-20min and carrying out standing for 15-80min, 3, separating a raffinate phase in the lower layer and an extract phase in the upper layer from the stood solution through gravity flows, and analyzing phenol content of the raffinate phase through a gas chromatography method, 4, carrying out rectification on the extract phase obtained through the step 3 to obtain a phenol removal extraction agent and a crude phenol product and recycling the phenol removal extraction agent for extraction of high-phenol concentration waste water, and 5, carrying out rectification on the raffinate phase obtained through the step 3 to obtain the residual phenol removal extraction agent and the phenol-free waste water. The high-phenol concentration waste water treatment method belongs to the technical field of water treatment.

Description

technical field [0001] The invention relates to a treatment method for phenol-containing wastewater, in particular to a treatment method for high-concentration volatile phenol-containing wastewater, belonging to the technical field of water treatment. Background technique [0002] Eucalyptol, also known as eucalyptol, is a colorless or light yellow oily transparent liquid. Has a camphor scent and a cooling herbal scent. Boiling point 176°C, melting point 1-1.5°C, freezing point 1°C, flash point 47-48°C, soluble in ethanol, ether, chloroform, glacial acetic acid, propylene glycol, glycerin and most non-volatile oils, slightly soluble in water. Eucalyptus oil is obtained from eucalyptus leaves, and the production of eucalyptus oil both at home and abroad adopts a steam distillation process. my country is very rich in eucalyptus oil resources. my country has introduced eucalyptus for more than 100 years, and about 300 species of eucalyptus have been introduced. Up to now, mor...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/10
CPCC02F1/001C02F1/04C02F1/26C02F9/00C02F2101/345
Inventor 万力李珩德方岩雄蔡晓兰谭伟
Owner GUANGDONG UNIV OF TECH
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