Deep treatment process of oily wastewater
A technology of advanced treatment and process method, which is applied in biological water/sewage treatment, microorganism-based methods, adsorbed water/sewage treatment, etc. It can solve problems such as regeneration difficulties and application limitations, and achieve stable treatment effects and low production and operation costs. , the effect of reducing damage
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Embodiment 1
[0026] The specific implementation process of the present invention is described below by taking the secondary air flotation effluent of an oil refinery as an example.
[0027] A kind of advanced treatment technology of oily wastewater, the technological process is described as follows:
[0028] The main water quality indicators of oily wastewater from air flotation are as follows:
[0029] category
CODcr
Volatile phenol
pH
Content (mg / L)
378.1-720.7
37.5-43.9
3.4
37.6-51.2
[0030] 1) The flotation effluent passes through the double-column series-connected activated carbon adsorption tower, and the bottom enters and the top exits. The adsorption residence time is 15min. After continuing the adsorption, the oil content in the effluent is higher than 1 mg / L, indicating that the adsorption site of the reorganized adsorption tower is occupied and needs to be regenerated. The tower is switched to an adsor...
Embodiment 2
[0034] Taking the advanced treatment of oily wastewater in an oil extraction plant as an example, the specific implementation process of the present invention is described.
[0035] 1) Select self-made modified fly ash as adsorbent, mix fly ash and modifier solution (V 盐酸 : V 硫 酸 = 1:3) Mix uniformly in a ratio of grey water mass to volume ratio of 1:1, carry out stirring reaction under the action of ultrasonic waves for 3 hours, and obtain modified fly ash adsorbent after drying.
[0036]2) The oily wastewater passes through the modified fly ash adsorption tower with two columns connected in series, the bottom enters and the top exits, the adsorption residence time is 10min, the oil content of the influent is (35.7-42.9mg / L), and the oil content of the effluent is controlled <1mg / L L, up to the standard treatment of wastewater 217BV. After continuing to absorb, the oil content in the effluent is higher than 1mg / L, indicating that the adsorption site of the restructured ads...
Embodiment 3
[0040] The specific implementation process of the present invention will be described below by taking the secondary air flotation effluent of an oil refinery as an example.
[0041] A kind of advanced treatment process of oily wastewater, the process is described as follows:
[0042] The main water quality indicators of the oily wastewater discharged from air flotation are as follows:
[0043] category
CODcr
Volatile phenol
pH
oil content
Content (mg / L)
378.1-720.7
37.5-43.9
3.4
37.6-51.2
[0044] 1) Mix the expanded graphite obtained by puffing at 900°C with the rubber powder particles larger than 20 mesh in the ratio of 8:1, and use the dry method to pack the column. The upper and lower ends of the adsorption tower are covered with 3cm thick glass fibers.
[0045] 2) The air flotation effluent passes through the expanded graphite-rubber powder adsorption tower with two columns connected in series, the bottom ent...
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Abstract
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