Method for oxidative degradation of material containing organic substances with circulating water
A technology of organic matter and materials, applied in the field of efficient supercritical water oxidation reaction, can solve problems such as time-consuming and laborious exploration, and achieve the effect of large selection, reducing harsh requirements and reducing corrosion
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Embodiment 1
[0074] refer to figure 1 . The initial stream 1 was a suspension with a cellulose concentration of 1.0 wt. % before the secondary stream 2 was produced. The initial material flow 1 enters the equipment, and after being preheated to 200°C, it is supplied at a flow rate of 2 g / s. The oxidant material stream 4 without preheating is a 16.32wt% hydrogen peroxide solution with a flow rate of 0.5 g / s. The non-preheated oxidant stream 4 is heated to 180° C. to form the preheated oxidant stream 5 . The heated initial stream 1 and the oxidant stream 5 are mixed to form the feed stream 6 . Thus, the concentration of cellulose in feed material 6 is 0.72% by mass and the oxidizer stream provides twice the amount of oxygen required to fully oxidize the carbon in the organics. The temperature of the reactor is 380°C, the pressure is 25 MPa, and the volume is 166 milliliters. The residence time of the material in the reactor is 30 seconds. The temperature of the exchanger is lowered to 5...
Embodiment 2 to 12
[0078] Except for the contents shown in Table 1 below, it was carried out in substantially the same manner as in Example 1.
[0079] Table 1
[0080]
[0081] The percentage of the amount of organic matter converted into carbon dioxide per unit time to the amount of feed organic matter; "X" means that the substance cannot be recycled under this condition.
Embodiment 13
[0083] The method is basically the same as in Example 1, except that the organic matter in the initial material stream 1 is acetic acid with the same concentration as in Example 1, and the removal efficiency is 100%.
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