Deep treatment process of oily wastewater
A technology of advanced treatment and process method, applied in the fields of adsorption water/sewage treatment, petroleum industry, separation method, etc., can solve the problems of difficulty in regeneration and application limitation, and achieve the effect of stable treatment effect, low production and operation cost, and energy saving.
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Embodiment 1
[0026] 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.
[0027] A kind of advanced treatment process of oily wastewater, the process is described as follows:
[0028] The main water quality indicators of the oily wastewater discharged 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 air flotation effluent passes through the activated carbon adsorption tower with two columns connected in series, the bottom enters and the top exits, the adsorption residence time is 15min, the oil content of the effluent is controlled to be less than 1mg / L, and the wastewater can be treated up to 429BV. After continuing to adsorb, the oil content in the effluent is higher than 1mg / L, indicating that the adsorption s...
Embodiment 2
[0034] Taking the advanced treatment of oily wastewater in an oil production plant as an example, the specific implementation process of the present invention is described.
[0035] 1) Using self-made modified fly ash as the adsorbent, the fly ash and modifier solution (V 盐酸 :V 硫 酸 = 1:3) mix uniformly with gray water mass volume ratio of 1:1, carry out stirring reaction for 3 hours under the action of ultrasonic waves, 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 adsorb, the oil content in the effluent is higher than 1mg / L, indicating that the adsorption site of the restructured adsorption to...
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 rubber powder particles larger than 20 mesh in a ratio of 8:1, and pack the column by dry method, and put 3cm thick glass fiber on the upper and lower ends of the adsorption tower.
[0045] 2) The air flotation effluent passes through the expanded graphite-rubber powder adsorption tower with two columns connected in series, the bottom enters and the top exits, th...
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