Polymer-containing oil sludge treatment device and method based on supercritical water gasification process
A supercritical water gasification and treatment device technology, which is applied in water/sludge/sewage treatment, sludge treatment, chemical instruments and methods, etc., can solve the problem that the cohesive state cannot achieve high-efficiency gasification of oil-containing sludge
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Embodiment 1
[0033] Step 1, the raw material containing poly-oil sludge is fed into the continuous stirring tank 3 through the screw feeding device 1, the feed mass ratio of poly-oil-containing sludge to subcritical water is 1:1, and the raw material and subcritical water 2 are subjected to subcritical Water liquefaction reaction, liquefying the difficult-to-flow raw material into an easy-flowing liquid to obtain a mixture A; the control of the continuous stirring tank 3 is 13Mpa, the temperature is 150°C, and the high-torque magnetic drive stirring speed is 1000rpm;
[0034] Step 2, the mixture A enters the supercritical water gasification device 4, the feed mass ratio of the mixture A to the supercritical water is 1:1, and the mixture A and the supercritical water 5 are subjected to supercritical water vaporization in the supercritical water gasification device 4. Gasification reaction, so as to achieve high-efficiency gasification of oil-containing sludge, and obtain mixture B; the tempe...
Embodiment 2
[0037] Step 1, the raw material containing oily sludge is fed into the continuous stirring tank 3 through the screw feeding device 1, the feed mass ratio of oily sludge containing oily polymer and subcritical water is 1:3, and the raw material is subcritically mixed with subcritical water 2 in it. Water liquefaction reaction, liquefying the difficult-to-flow raw material into an easy-flowing liquid to obtain a mixture A; the control of the continuous stirring tank 3 is 15Mpa, the temperature is 250°C, and the high-torque magnetic drive stirring speed is 1500rpm;
[0038] Step 2, the mixture A enters the supercritical water gasification device 4, the feed mass ratio of the mixture A to the supercritical water is 1:3, and the mixture A and the supercritical water 5 are subjected to supercritical water vaporization in the supercritical water gasification device 4. Gasification reaction, so as to achieve high-efficiency gasification of oil-containing sludge, and obtain mixture B; t...
Embodiment 3
[0041] Step 1, the raw material containing poly-oil sludge is sent into the continuous stirring tank 3 through the screw feeding device 1, the feed mass ratio of poly-oil-containing sludge to subcritical water is 1:5, and the raw material is subcritically mixed with subcritical water 2 in it. Water liquefaction reaction, liquefying the difficult-to-flow raw material into an easy-flowing liquid to obtain a mixture A; the control of the continuous stirring tank 3 is 20Mpa, the temperature is 370°C, and the high-torque magnetic drive stirring speed is 1800rpm;
[0042]Step 2, the mixture A enters the supercritical water gasification device 4, the feed mass ratio of the mixture A to the supercritical water is 1:5, and the mixture A and the supercritical water 5 are subjected to supercritical water vaporization in the supercritical water gasification device 4 and supercritical water 5 Gasification reaction, so as to achieve high-efficiency gasification of oil-containing sludge, and ...
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