Desalination and dehydration method and device of oily waste
A dewatering device and waste technology, applied in separation methods, grease/oily substance/float removal devices, mining wastewater treatment, etc., can solve the problems of desalination and dehydration easily affected by the properties of raw materials, short settling time, poor desalination effect, etc. , to achieve the effect of stable treatment effect, strong safety and compact device
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Embodiment 1
[0072] This example is used to illustrate the method for desalting and dehydrating oily waste of the present invention.
[0073] use figure 1 The shown device pumps dirty oil (water content is 37% by weight, salt content is 453mg NaCl / L, mechanical impurity is 3.3% by weight, and the balance is oil content) from inlet 9 to dehydration tank 1, through The U-shaped flow channel provided at the inlet 9 enters the main body of the dehydration tank 1, and then the pressure reducing valve 8 is closed to keep the dehydration tank 1 in a closed state, and the microwave reactor 2 is opened to carry out microwave heating to the dirty oil in the dehydration tank 1 ( The radiation frequency is 2450MHz, the power is 1200W), and when the temperature of the dirty oil is stabilized to 130°C, stop heating, and after the pressure in the dehydration tank is stabilized, the pressure relief valve 8 is opened to reduce the pressure in the dehydration tank 1 to normal pressure (approximately 101.3k...
Embodiment 2
[0076] This example is used to illustrate the method for desalting and dehydrating oily waste of the present invention.
[0077] According to the method described in embodiment 1, the difference is:
[0078] The treated oily waste is oil tank bottom sludge with a water content of 40.17% by weight, a salt content of 714mg NaCl / L, and mechanical impurities of 14.8% by weight;
[0079] The conditions of microwave heating include: the radiation frequency is 2450MHz, and the power is 1500W;
[0080] Microwave heating until the temperature of the oil sludge is 120°C, the condensed water collected in the light component reflux tank 6 after pressure relief accounts for 6% by weight of the water in the waste oil;
[0081] The moment the pressure is released, the temperature of the residual material in the dehydration tank 1 reaches 70° C., and it is kept at 70° C. for 30 minutes.
[0082] Wherein, the water content of the obtained purified oil was 0.9% by weight, and the dehydration ra...
Embodiment 3
[0084] This example is used to illustrate the method for desalting and dehydrating oily waste of the present invention.
[0085] According to the method described in embodiment 1, the difference is that microwave heating to the temperature of the dirty oil is 100° C., and the condensed water collected in the light component reflux tank 6 after pressure relief accounts for 2% by weight of the water in the dirty oil.
[0086] Thus, the water content of the obtained purified oil was 13.1% by weight, and the dehydration rate was 64.6%; the salt content was 194 mg NaCl / L, and the desalination rate was 57.2%.
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