Phosphoric acid method activated carbon acid recovery, rinsing and dehydration three-in-one automatic process
A three-in-one, acid recovery technology, applied in inorganic chemistry, carbon compounds, chemical instruments and methods, etc., can solve the problems of inability to achieve acid recovery, washing and dehydration, low dehydration efficiency, and inability to continuously fabricate
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Embodiment 1
[0081] Please refer to Figure 1 to Figure 3 As shown, the three-in-one automatic process of phosphoric acid activated carbon recovery, rinsing and dehydration includes the following steps:
[0082] Step 1. Put the carbon slurry into the centrifuge for dehydration treatment, and collect the phosphoric acid into the first storage tank;
[0083] Step 2, add 320L in the centrifuge for the first time influent (phosphoric acid of 28 ° of Bé), carry out dehydration treatment 5min, collect the first time effluent in the first storage tank; the phosphoric acid water in the first storage tank is used for Prepare the next batch of carbon slurry;
[0084] Step 3, add 320L second time water inflow (phosphoric acid of 18 ° of Bé) in the centrifuge, carry out dehydration treatment 12min, collect the second time effluent in the second storage tank, described second time effluent is used as the next rinsing The first water use;
[0085] Step 4, add 320L in the centrifuge for the third time...
Embodiment 2
[0099] The difference between embodiment 2 and embodiment 1 is only that the phosphoric acid concentration of the first water inflow to the sixth inflow is different, and the first water inflow to the sixth inflow in embodiment 2 are respectively from the second water out to the seventh water out;
[0100] The first water inlet to the sixth water inlet of Example 2 are respectively: phosphoric acid of 32°Bé, phosphoric acid of 20°Bé, phosphoric acid of 14°Bé, phosphoric acid of 9°Bé, phosphoric acid of 4°Bé, phosphoric acid of 0.5°Bé .
Embodiment 3
[0102] The only difference between embodiment 3 and embodiment 1 is that the phosphoric acid concentration of the first water inflow to the sixth inflow is different, and the first water inflow to the sixth inflow in embodiment 3 are respectively From the second effluent to the seventh effluent, the high-concentration phosphoric acid water in the first storage tank is used to prepare the next batch of carbon slurry. It can also be used to adjust the concentration of the second effluent to the sixth effluent within the required range;
[0103] The first water inlet to the seventh water inlet of embodiment 3 are respectively: the phosphoric acid of 35°Bé, the phosphoric acid of 25°Bé, the phosphoric acid of 18°Bé, the phosphoric acid of 12°Bé, the phosphoric acid of 5°Bé, the phosphoric acid of 1°Bé Phosphoric acid of Bé.
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