Active carbon and modification method as well as application thereof in processing water containing endocrine disrupters
An activated carbon and modified technology, applied in the direction of adsorbed water/sewage treatment, etc., can solve the problems of pollution, high technical cost, difficult adsorption efficiency of activated carbon, etc., to extend service life, improve adsorption efficiency, large adsorption capacity and renewable sexual effect
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specific Embodiment approach 1
[0018] Specific embodiment one: The treatment method of the activated carbon modification of the present embodiment is as follows: the activated carbon with particle size between 40 mesh and 10 mesh is placed in the quartz tube of the muffle furnace, and hydrogen gas is first passed through the muffle furnace for 1 hour at room temperature. hour, the gas flow rate was 50 ml / min, and then under the protection of the same hydrogen flow, the muffle furnace was heated to 600°C at a rate of 10°C / min and kept for 3 hours. After the temperature dropped to 30°C, the hydrogen flow was stopped. Continue to pass air at a flow rate of 50 ml / min for 1 hour, take out the activated carbon, put it and hydrochloric acid (35%) at a mass ratio of 10%, and boil it under reflux for 3 hours. After the end, wash the carbon sample with deionized water to chloride ions If there is no detection, it is modified carbon. Activated carbon needs to be washed repeatedly with deionized water before modificati...
specific Embodiment approach 2
[0019]Specific embodiment two: the water treatment method of the present invention is implemented according to the following process: the water after the traditional water treatment process is processed enters the reactor that modified charcoal is housed, and charcoal exists in fluidized bed form or fixed bed form therein, and control The residence time of water in the activated carbon bed is 10-60 minutes, and the water flow velocity is 1-15 m / hour. When the fluidized bed form is adopted, the modified carbon is loaded into the reactor from the top of the reactor, the raw water enters from the bottom of the reactor in a downstream manner, and the activated carbon is in a flowing state in the reactor; when the fixed bed form is adopted, the modified carbon is loaded in advance. Into the reactor, the height of the carbon bed is between 0.5m and 2m, and the raw water can enter the reactor in three ways, namely the downstream type (the raw water enters from the bottom right and exi...
specific Embodiment approach 3
[0020] Embodiment 3: The difference between this embodiment and Embodiment 2 is that the reactor filled with modified charcoal is a multi-cascade reactor in the form of a plurality of circular tube reactors connected in series, and the charcoal is contained in it. It exists in the form of a fixed bed, and the filling height of carbon in each tube is 0.5 meters to 2 meters. The raw water enters the reactor in a forward or countercurrent manner, and the residence time of the water in the activated carbon bed is controlled to be 10 to 60 minutes. The water flow rate is 1 to 15 meters per hour. This embodiment can ensure that the water quality of the seriously polluted raw water reaches the safety standard.
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