Production process for preparing magnesium sulfate by using alkylation waste acid
A technology of alkylation waste acid and production process, applied in the direction of magnesium sulfate, magnesium fertilizer, application, etc., can solve the problems of high environmental protection pressure, increase the total investment of the device, and more equipment, and achieve the effect of low production cost
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Embodiment 1
[0031] The invention discloses a production process for preparing magnesium sulfate by using alkylation waste acid. The process comprises the following steps.
[0032] In the first step, the reaction generates solid magnesium sulfate.
[0033] The magnesium oxide powder was continuously stirred, and during the stirring process, alkylated waste acid was added to the magnesium oxide powder. In this embodiment, the concentration of concentrated sulfuric acid was 85% by mass. Concentrated sulfuric acid in the alkylation waste acid reacts with magnesium oxide powder to form solid magnesium sulfate. At the same time, a large amount of heat is released during the reaction, which creates a high-temperature reaction environment in the reactor. The temperature can reach more than 300 °C, and the high temperature makes the alkyl The organic matter in the spent acid is carbonized to produce solid dross whose main component is carbon.
[0034] The mass percentage concentration of magnesiu...
Embodiment 2
[0059] The difference from Example 1 is: in this example, the mass percent concentration of concentrated sulfuric acid is 87%. Concentrated sulfuric acid in the alkylation waste acid reacts with magnesium oxide powder to form solid magnesium sulfate. At the same time, a large amount of heat is released during the reaction, which creates a high-temperature reaction environment in the reactor. The temperature can reach more than 300 °C, and the high temperature makes the alkyl The organic matter in the spent acid is carbonized to produce solid dross whose main component is carbon.
[0060] The mass percentage concentration of magnesium oxide adopted in the present embodiment is 83%, and in the stirring process, the injection flow rate of alkylation waste acid is 0.4m 3 / h, the stirring speed of magnesium oxide powder is 17 rpm.
[0061] During the reaction, the mass ratio of magnesium oxide powder to the injected alkylation waste acid is 1:2.3. In this embodiment, 1 ton of magn...
Embodiment 3
[0064] The difference from Example 1 is: in this example, the mass percent concentration of the concentrated sulfuric acid is 89%. Concentrated sulfuric acid in the alkylation waste acid reacts with magnesium oxide powder to form solid magnesium sulfate. At the same time, a large amount of heat is released during the reaction, which creates a high-temperature reaction environment in the reactor. The temperature can reach more than 300 °C, and the high temperature makes the alkyl The organic matter in the spent acid is carbonized to produce solid dross whose main component is carbon.
[0065] The mass percentage concentration of magnesium oxide adopted in the present embodiment is 87%, and in the stirring process, the injection flow rate of alkylation waste acid is 0.6m 3 / h, the stirring speed of magnesium oxide powder is 14 rpm.
[0066] During the reaction, the mass ratio of magnesium oxide powder to the injected alkylation waste acid is 1:2.5. In this embodiment, 1 ton of ...
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