Magnesium sulfate and manufacturing method thereof
A manufacturing method and technology of magnesium sulfate, applied in magnesium sulfate and other directions, can solve the problems of high cost of raw materials, extensive use, low efficiency and efficiency, and achieve the effects of good product quality, promoting the development of circular economy industries, and no pollution and secondary pollution.
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Embodiment 1
[0017] Embodiment 1, produce 1000 kilograms of magnesium sulfates.
[0018] Get 1000 kilograms of chemical by-product sulfuric acid (mass percentage concentration is 60%, is the by-product sulfuric acid associated when producing products such as p-toluenesulfonyl chloride, o-toluenesulfonyl chloride or o / p-toluenesulfonyl chloride.), mass percentage content 80% 345 kg of magnesium oxide powder, 0 kg of 98% industrial concentrated sulfuric acid and 0 kg of water (because the mass percentage concentration of the chemical by-product sulfuric acid is 60%, between 55% and 70%, so it is not necessary to process industrial concentrated sulfuric acid and Water) was evenly added in proportion to the mixing reactor one after another, and stirred and mixed to prepare a moderately dry and dilute slurry. At the outlet of the mixer, the temperature of the slurry discharged from the overflow was controlled at 140 degrees. Then, the reaction slurry discharged after the reaction is successivel...
Embodiment 2
[0019] Embodiment 2, produce 1000 kilograms of magnesium sulfates.
[0020] Get 660 kilograms of chemical by-product sulfuric acid (mass percentage concentration 40%, take chlorosulfonic acid as raw material to participate in the by-product sulfuric acid associated in chemical production reaction), 340 kg of magnesia powder with mass percentage content 85%, 98% industrial 340 kg of concentrated sulfuric acid and 0 kg of water. Add it into the mixing reactor evenly in proportion, carry out stirring and mixing reaction, and prepare a dry and thin moderate slurry. At the outlet of the mixer, the temperature of the slurry discharged from the overflow is controlled at 120 degrees. Then, the reaction slurry discharged after the reaction is successively transferred to the conversion chamber and left for 70 minutes to be matured, dried and solidified. 0.8H2O的素食石。 Finally, through crushing, shaping, cooling and other processes, magnesium sulfate in the form of MgSO4. 0.8H2O is obtaine...
Embodiment 3
[0021] Embodiment 3, produce 1000 kilograms of magnesium sulfates.
[0022] Get 860 kilograms of chemical by-product sulfuric acid (mass percentage concentration 75%, is the sulfuric acid formed in the process of producing glufosinate and dimethyl phosphite), 355 kilograms of magnesium oxide powder with mass percentage content 70%, 98% industrial concentrated sulfuric acid 0 kg and 140 kg of water. Add it into the mixing reactor evenly and in succession according to the proportion, carry out stirring and mixing reaction, and prepare a dry and thin moderate slurry. At the outlet of the mixer, the temperature of the slurry discharged from the overflow is controlled at 155 degrees. Then, the reaction slurry discharged after the reaction is successively transferred to the conversion chamber and left for 30 minutes to be matured, dried and solidified. Finally, the magnesium sulfate in the form of MgSO4.1.5H2O can be obtained through crushing, shaping and cooling.
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