A processing system and method for petrochemical alkali slag
A treatment method and technology of a treatment system, applied in the field of petrochemical alkali residue waste liquid treatment, can solve the problems of high energy consumption, complex treatment method, poor economy, etc., and achieve the effect of reducing environmental pollution and saving investment.
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Embodiment 1
[0079] The liquid hydrocarbon alkali slag of a petrochemical enterprise, in which the COD is 4.13×10 5 mg / L, 0.1wt% volatile phenols, 3.6wt% sodium methyl mercaptide, Na 2 S is 0.2wt%, and the pH value is 11.67.
[0080] Using the present invention figure 1 According to the method shown, the liquid hydrocarbon alkali slag to be treated is added to the reaction tank, the flue gas of the sintering machine is passed into the reaction tank, and the temperature of the alkali residue in the first reactor (reaction tank) is adjusted by controlling the flue gas flow rate The temperature is 85°C, and the acidification reaction time is controlled to be 100min. During the acidification process, sodium naphthenate, sodium phenolate, and sodium sulfide in the alkali slag are converted into sodium carbonate, naphthenic acid, and phenol, and hydrogen sulfide is oxidized to generate SO 2 The gas enters the sintering flue gas treatment device. Add sintered desulfurization ash to the acidifi...
Embodiment 2
[0083] The liquid hydrocarbon alkali slag of a petrochemical enterprise, in which the COD is 4.13×10 5 mg / L, 0.1wt% volatile phenols, 3.6wt% sodium methyl mercaptide, Na 2 S is 0.2wt%, and the pH value is 11.67.
[0084] Using the present invention figure 1 According to the method shown, the liquid hydrocarbon alkali slag to be treated is added to the reaction tank, the flue gas of the sintering machine is passed into the first reactor (reaction tank), and the temperature of the alkali residue in the reaction tank is adjusted by controlling the flue gas flow rate The temperature is 90°C, and the acidification reaction time is controlled to be 110min. During the acidification process, sodium naphthenate, sodium phenate, and sodium sulfide in the alkali slag are converted into sodium carbonate, naphthenic acid, and phenol, and hydrogen sulfide is oxidized to generate SO 2 The gas enters the sintering flue gas treatment device. Add sintered desulfurization ash to the acidified...
Embodiment 3
[0087] The liquid hydrocarbon alkali slag of a petrochemical enterprise, in which the COD is 4.13×10 5 mg / L, 0.1wt% volatile phenols, 3.6wt% sodium methyl mercaptide, Na 2 S is 0.2wt%, and the pH value is 11.67.
[0088] Using the present invention figure 1 According to the method shown, the liquid hydrocarbon alkali slag to be treated is added to the first reactor (reaction tank), the flue gas of the sintering machine is passed into the reaction tank, and the temperature of the alkali residue in the reaction tank is adjusted by controlling the flue gas flow rate The temperature is 95°C, and the acidification reaction time is controlled to be 120min. During the acidification process, sodium naphthenate, sodium phenate, and sodium sulfide in the alkali slag are converted into sodium carbonate, naphthenic acid, and phenol, and hydrogen sulfide is oxidized to generate SO 2 The gas enters the sintering flue gas treatment device. Add sintered desulfurization ash to the acidified...
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