Anti-blocking agent and equipment anti-blocking method for supercritical hydrothermal treatment system of high-salt organic waste
A technology of organic waste and supercritical water, which is applied in the fields of chemical industry and environmental protection, can solve problems such as blockage, and achieve the effect of wide application range, low cost and easy realization
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Embodiment 1
[0038] Example 1 supercritical water oxidation treatment of pickled mustard wastewater
[0039] Mustard mustard wastewater: initial chemical oxygen demand (COD), 2984mg / L; salt content (mainly NaCl), 2.8%; anti-blocking agent is 50nm SiO 2 Granules, the addition amount is 0.1%; the additive is 2% starch solution; the oxidant is air, and the peroxygen ratio is selected as 2.0; the temperature of high-temperature supercritical water is 600 ° C, and the flow ratio of mustard mustard wastewater is 3:1.
[0040] Mustard mustard wastewater with 2% starch (2) and 0.1% SiO 2Particles (3) are mixed in the mixing storage tank 4 to form a uniform suspension, which is pressurized to 26 MPa by the booster pump 5, and enters the mixer 6 without any preheating along the way; in the mixer 6, the suspension is mixed with the high temperature super The critical water and air are mixed up to 390°C and enter the reactor 9; in the reactor 9, the organic matter undergoes an oxidation reaction, and...
Embodiment 2
[0041] Example 2 Supercritical water gasification treatment of pharmaceutical wastewater
[0042] Pharmaceutical wastewater: initial COD, 34987mg / L; salt content (Na 2 CO 3 、Na 2 SO 4 Mainly), 5.8%; the anti-blocking agent is 1-10 microns of Fe 2 o 3 Granules, the addition amount is 1%; the additives are 2% starch solution and 0.5% sodium dodecylsulfonate; the oxidant is oxygen, and the peroxygen ratio is selected as 2.5; the temperature of high-temperature supercritical water is 600 ° C, which is compatible with pharmaceutical The flow ratio of wastewater is 2.5:1.
[0043] Pharmaceutical wastewater with 2% starch solution and 0.5% sodium lauryl sulfate and 3% Fe 2 o 3 The particles are mixed in the mixing storage tank 4 to form a uniform suspension, which is pressurized to 28MPa by the booster pump 5, and enters the mixer 6 without any preheating along the way; in the mixer 6, the material is mixed with high-temperature supercritical water and oxygen Mixing reaches 3...
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