A reactor, system and method for in situ resource recovery of urine
A technology of resource recovery and reactor, applied in the direction of chemical instruments and methods, applications, climate change adaptation, etc., can solve the problems of water treatment facility blockage, transparency decline, carcinogenicity, etc., achieve efficient recovery, simple structure, and avoid losses Effect
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Embodiment 1
[0039] Example 1: Exploratory experiment of biochar and magnesia-loaded biochar loading
[0040] In this example, the nitrogen, phosphorus and potassium resources recovered from urine are filled with biochar and magnesium oxide-loaded biochar, and the filling amount of biochar and magnesium oxide-loaded biochar is determined according to the properties of urine, biochar properties and the replacement cycle of the reactor. First, set the reactor replacement cycle to 10 days, the number of urination per day is 0.2 per day, the ammonia nitrogen adsorption capacity of the biochar is 10mg / g, and the magnesium content of the magnesium oxide loaded biochar is 15%. The formula for calculating the filling amount of biochar is as follows;
[0041]
[0042] The filling amount of biochar was 0.56kg, and the filling amount of magnesium oxide-loaded biochar was 0.09kg.
[0043] The results of resource recovery are: the recovery rate of ammonia nitrogen is 99%, the recovery rate of phosp...
Embodiment 2
[0044] Example 2: Exploring experiment of biochar and magnesia-loaded biochar loading
[0045] The operation steps of filling the filler for recovering urine nitrogen, phosphorus and potassium resources in this example are the same as those in Example 1, and the difference from Example 1 is that the capacity of the biochar to adsorb ammonia nitrogen set in this example is 4 mg / g, and the biochar is obtained. The filling amount is 1.40kg. The results of resource recovery are: the recovery rate of ammonia nitrogen is 99%, the recovery rate of phosphorus is 93%, and the recovery rate of potassium is 24%. The comparison between Examples 1 and 2 shows that when the adsorption capacity of biochar to ammonia nitrogen is high, the filling amount of biochar can be reduced, thereby reducing the cost of technical application, and the recovery rate of potassium resources is higher, and the resource recovery effect is better.
Embodiment 3
[0046] Example 3: Exploratory experiment of biochar and magnesia-loaded biochar loading
[0047] The operation steps of filling the filler for recovering urine nitrogen, phosphorus and potassium resources in this example are the same as those in Example 1, and the difference from Example 1 is that the magnesium content of the magnesium oxide-loaded biochar set in this example is 5%, and the magnesium oxide-loaded biochar is set at 5%. The biochar filling amount is 0.27kg. The results of resource recovery are: the recovery rate of ammonia nitrogen is 99%, the recovery rate of phosphorus is 92%, and the recovery rate of potassium is 26%. The comparison between Examples 1 and 3 shows that when the magnesium content of the magnesium oxide-loaded biochar is high, and the magnesium element content of the magnesium oxide-loaded biochar is high, the filling amount of the magnesium oxide-loaded biochar can be reduced, which is beneficial to reduce the cost of technical application.
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