Compound decoloring and deodorizing coagulant and preparation process thereof
A manufacturing process and technology for coagulants, which are applied in the field of composite decolorizing and odorous coagulants and their manufacturing processes, can solve problems such as ineffectiveness, and achieve the effects of low price, high degradation rate and wide application range of pH value.
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Embodiment 1
[0084] Embodiment 1 (best embodiment)
[0085] Composite decolorizing taste coagulant, comprises the raw material of following percentage by weight and makes magnesium sulfate:
[0086] 40% magnesium oxide with a content of 85%;
[0087] 30% concentration of sulfuric acid 60%;
[0088] Then the above-mentioned magnesium sulfate prepared is formulated into the product of the present invention with active calcium hydroxide in the following weight percentages:
[0089] Magnesium sulfate 40%;
[0090] Content is 98% active calcium hydroxide 60%.
[0091] The product obtained in this embodiment has a good effect for urban sewage treatment.
Embodiment 2
[0092] Embodiment 2 (with reference to the preparation mode of embodiment 1, hereinafter the same)
[0093] Magnesium oxide 35% with a content of 85%;
[0094] 30% concentration of sulfuric acid 65%;
[0095] Magnesium sulfate 35%;
Embodiment 3
[0098] 30% magnesium oxide with a content of 85%;
[0099] 30% concentration of sulfuric acid 70%;
[0100] Magnesium sulfate 30%;
[0101] Content is 98% active calcium hydroxide 70%.
[0102] The manufacturing process of the above-mentioned composite decolorizing coagulant, according to the weight percentage of the raw materials, the concentration of the waste sulfuric acid produced by the sulfuric acid method to produce titanium dioxide by-products is adjusted to 25-30% and put into the reaction pool, and the magnesium oxide with a content of 85% is used according to the proportioning ratio. Add to the reaction tank; the reaction releases heat, and the reaction time is 1 to 3 hours, preferably 2 hours; after filtration, the liquid is lifted to the concentration tank with an acid-resistant pump, heated to 250°C to 300°C, preferably 280°C, and concentrated for 1 to 3 hours. Preferably 2 hours; when referring to the crystallization pool, the crystallization time at room temp...
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