Method for preparing raw material of desulfurizer by using chlorinated waste molten salt produced in the production of tcl4
A technology of desulfurization agent and molten salt, which is applied in the field of treating waste molten salt and Cl-containing wastewater, can solve the problem of low utilization rate of desulfurization agent, and achieve the effect of reducing pollution
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Embodiment 1
[0019] Such as the process flow of processing waste molten salt figure 1 As shown, in the waste molten salt chloride layer, water accounting for 90.0%-280.0% of the chloride mass is gradually added to form a chloride supersaturated solution, and the crude NaCl solid and chloride saturated solution are separated after filtration; the chloride saturated solution, First add Fe in solution 2+ and Fe 3+ Equivalent (obtained greater than Fe 2+ and Fe 3+ equivalent) of NaOH, to obtain a precipitate and chloride solution, the precipitate is mainly Fe (OH) 2 and Fe(OH) 3 , the wet ferric hydroxide and ferrous hydroxide separated by filtration are then cleaned, precipitated and matured, dried and other processes, and finally α-Fe with desulfurization activity is obtained 2 o 3 ·H 2 O, γ-Fe 2 o 3 ·H 2 O and γ-Fe 2 o 3 Active iron oxide in three forms, then add binder and pore-forming agent according to the proportion, adjust the pH value to make it alkaline, and then form, dr...
Embodiment 2
[0025] Such as the process flow of processing waste molten salt figure 2 As shown, water accounting for 90.0%-280.0% of the chloride mass is gradually added to the waste molten salt chloride layer to form a chloride supersaturated solution at a temperature of 40-95°C, and the crude NaCl solid and hot chloride are separated after filtration Saturated solution; the chloride saturated solution, first added to the solution with Mn 2+ , Fe 2+ and Fe 3+ Equivalent (obtained greater than Mn 2+ , Fe 2+ and Fe 3+ equivalent) of NaOH, to obtain a precipitate and chloride solution, the precipitate is mainly Mn (OH) 3 , Fe(OH) 2 and Fe(OH) 3 , the wet manganese hydroxide, ferric hydroxide and ferrous hydroxide separated by filtration are then cleaned, precipitated and matured, dried and other processes, and finally the manganese oxide and α-Fe with desulfurization activity are obtained. 2 o 3 ·H 2 O, γ-Fe 2 o 3 ·H 2 O and γ-Fe 2 o 3 Active iron oxide and manganese oxide in...
Embodiment 3
[0030] Such as the process flow of processing waste molten salt image 3 As shown, water accounting for 90.0%-280.0% of the chloride mass is gradually added to the waste molten salt chloride layer to form a chloride supersaturated solution at a temperature of 40-95°C, and the crude NaCl solid and hot chloride are separated after filtration Saturated solution; To chloride saturated solution, first add Fe in the solution 2+ and Fe 3+ Equivalent (obtained greater than Fe 2+ and Fe 3+ equivalent) of milk of lime to obtain precipitate and chloride solution, the precipitate is mainly Fe(OH) 2 and Fe(OH) 3 , the wet ferric hydroxide and ferrous hydroxide separated by filtration are then cleaned, precipitated and matured, dried and other processes, and finally α-Fe with desulfurization activity is obtained 2 o 3 ·H 2 O, γ-Fe 2 o 3 ·H 2 O and γ-Fe 2 o 3 Active iron oxide in three forms, then add binder and pore-forming agent according to the proportion, adjust the pH value ...
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