Method and device for treating coking wastewater
A technology for coking wastewater and treatment method, applied in the direction of oxidized water/sewage treatment, etc., can solve the problems of slow reaction rate, high toxicity, poor biodegradability, etc., and achieve the effect of saving consumption, strong adaptability and stable operation
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Embodiment 1
[0023] The treatment method of coking wastewater described in this embodiment specifically includes the steps of: in a subcritical state, add oxygen into 1L of coking wastewater as an oxidant, and then add catalyst K 2 CO 3 , to oxidize coking wastewater to produce hydrogen, wherein the reaction time is 60 s, the pressure is 25.00MPa, the temperature is 300°C, and the heating rate is 20°C / min;
[0024] The reaction device for realizing the treatment method of coking wastewater described in this embodiment includes a coking wastewater storage tank 1, a high-pressure metering pump 2, an oxidant storage tank 3, a gas booster pump 4, a preheater 5, a supercritical reactor 6, Buffer tank 7, gas-liquid separator 8, liquid collection tank 9, gas collection tank 10, coking wastewater storage tank 1 and oxidant storage tank 3 are respectively connected to pre-heater 5 through high-pressure metering pump 2 and gas booster pump 4. The heater 5, the supercritical reactor 6, and the buffe...
Embodiment 2
[0031] The treatment method of coking wastewater described in this embodiment specifically includes the steps of: in a supercritical state, adding hydrogen peroxide into 1L of coking wastewater as an oxidizing agent, and then adding catalyst Na 2 CO 3 , to oxidize coking wastewater to produce hydrogen, wherein the reaction time is 400 s, the pressure is 23MPa, the temperature is 600°C, and the heating rate is 50°C / min;
[0032] The reaction device for realizing the treatment method of coking wastewater described in this embodiment includes a coking wastewater storage tank 1, a high-pressure metering pump 2, an oxidant storage tank 3, a gas booster pump 4, a preheater 5, a supercritical reactor 6, Buffer tank 7, gas-liquid separator 8, liquid collection tank 9, gas collection tank 10, coking wastewater storage tank 1 and oxidant storage tank 3 are respectively connected to pre-heater 5 through high-pressure metering pump 2 and gas booster pump 4. The heater 5, the supercritica...
Embodiment 3
[0039] The treatment method of coking wastewater described in this embodiment specifically includes the steps of: in a supercritical state, add oxygen into 1L of coking wastewater as an oxidant, then add a catalyst and then add catalyst K 2 CO 3 and Na 2 CO 3 mixture, where K 2 CO 3 and Na 2 CO 3 The mass ratio is 1:3 to oxidize the coking wastewater to produce hydrogen. The reaction time is 150 s, the pressure is 24.00 MPa, the temperature is 400°C, and the heating rate is 30°C / min;
[0040] The reaction device for realizing the treatment method of coking wastewater described in this embodiment includes a coking wastewater storage tank 1, a high-pressure metering pump 2, an oxidant storage tank 3, a gas booster pump 4, a preheater 5, a supercritical reactor 6, Buffer tank 7, gas-liquid separator 8, liquid collection tank 9, gas collection tank 10, coking wastewater storage tank 1 and oxidant storage tank 3 are respectively connected to pre-heater 5 through high-pressure...
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