Production equipment of active coke for phenol ammonia wastewater treatment and treatment method of equipment
A technology for wastewater treatment and production equipment, applied in the field of coal chemical industry, to achieve high removal rate, reduce the difficulty of subsequent treatment, and increase the added value
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Embodiment 1
[0061] This embodiment provides a kind of activated coke production device for the treatment of phenolic ammonia wastewater, the structural diagram of the device is as follows figure 1 As shown, it includes a feed unit 1, a riser reactor 3, a charcoal burner 2, an activated coke production device 9, a separation unit and a waste water treatment unit 10;
[0062] The outlet of the feed unit 1 is connected to the inlet of the riser reactor 3, and the riser reactor 3 extends upwards into the separation unit, and the solid outlet of the separation unit is connected to the inlet of the charcoal burner 2, the The gas outlet of the separation unit is connected to the inlet of the riser reactor 3, and the waste water outlet of the separation unit is connected to the inlet of the waste water treatment unit 10;
[0063] The first outlet of the charcoal burner 2 is connected with the inlet of the riser reactor 3, the second outlet of the charcoal burner 2 is connected with the entrance o...
Embodiment 2
[0070] This embodiment provides an active coke production device for the treatment of phenolic ammonia wastewater. The structure of the device refers to the structure in Example 1, the only difference being that the active coke production device 9 includes a bubbling bed reactor, Said device does not include powder coke cooling device 8 .
Embodiment 3
[0072] This embodiment provides a kind of active coke production method that is used for the treatment of phenolic ammonia wastewater, and described method is carried out in the device described in embodiment 1, comprises the following steps:
[0073] (1) The raw coal with a particle size of 0.1mm is subjected to a pyrolysis reaction in the riser reactor 3 under the action of a carrier. The temperature of the pyrolysis reaction is 550°C and the time is 3s. Solid separation and gas-liquid separation;
[0074] (2) Part of the powdered coke obtained after separation in step (1) is subjected to charcoal burning treatment, the temperature of the charcoal burning treatment is 700°C, part of the powdered coke is directly cooled and recovered, and the powdered coke part after the charcoal burning treatment is returned to step (1) as The solid carrier is used, and the other part undergoes an activation reaction under the action of the activation medium air, and the temperature of the a...
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