Method for producing nitrate-and-sulfur-based compound fertilizer and co-producing gypsum by utilizing potassium hydrogen sulfate
A technology of nitrosulfur-based compound fertilizer and potassium hydrogen sulfate, applied in the direction of calcium/strontium/barium sulfate, application, fertilization device, etc. High, simplified operation, lower investment effect
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Embodiment 1
[0034] Embodiment 1: implement raw material: 1, phosphate rock powder: P 2 o 5 The content is 30.72%, CaO is 48.28%; 2. Nitric acid: concentration 70%; 3. Industrial ammonium sulfate: ammonia content 21%.
[0035] The implementation process of the present invention comprises the following steps:
[0036] (1) After adding water to the phosphate rock powder, carry out acidolysis reaction with 70% nitric acid, the molar ratio of calcium ion and nitric acid in the phosphate rock is 1:3; the reaction temperature is 45° C., and the reaction is 0.5 hour.
[0037] (2) The crude acid hydrolyzate obtained in step (1) is filtered to remove acid insoluble matter and organic floating matter, and the filtrate is fine acid hydrolyzate.
[0038] (3) the refined acid hydrolyzate of step (2) is added to industrial ammonium sulfate and carry out metathesis reaction, and the ammonium sulfate add-on is by the mol ratio of calcium ion in ammonium sulfate and refined acid hydrolyzate 1: 1; Reactio...
Embodiment 2
[0041] Embodiment 2: implement raw material: 1, phosphate rock powder: P 2 o 5 The content is 29.85%, CaO is 48.30%; 2. Nitric acid: the concentration is 40%; 3. Industrial ammonium sulfate: the ammonia content is 21%.
[0042]The implementation process of the present invention comprises the following steps:
[0043] (1) Add water to phosphate rock powder and carry out acid hydrolysis reaction with 40% nitric acid, the molar ratio of calcium ions and nitric acid in the phosphate rock is 1:2; the reaction temperature is 70° C., and react for 4 hours.
[0044] (2) The crude acid hydrolyzate obtained in step (1) is filtered to remove acid insoluble matter and organic floating matter, and the filtrate is fine acid hydrolyzate.
[0045] (3) the refined acid hydrolyzate of step (2) is added to industrial ammonium sulfate and carry out metathesis reaction, the ammonium sulfate add-on is by the mol ratio of calcium ion in ammonium sulfate and refined acid hydrolyzate 1.2: 1; Tempera...
Embodiment 3
[0048] Embodiment 3: implement raw material: 1, phosphate rock powder: P 2 o 5 The content is 31.05%, CaO is 47.65%; 2. Nitric acid: concentration 60%; 3. Industrial sulfuric acid: concentration 98%.
[0049] The implementation process of the present invention comprises the following steps:
[0050] (1) Add water to phosphate rock powder and carry out acidolysis reaction with 60% nitric acid, the molar ratio of calcium ion and nitric acid in the phosphate rock is 1:2.3; the reaction temperature is 58° C., and the reaction is 1.5 hours.
[0051] (2) The crude acid hydrolyzate obtained in step (1) is filtered to remove acid insoluble matter and organic floating matter, and the filtrate is fine acid hydrolyzate.
[0052] (3) the refined acid hydrolyzate of step (2) is added industrial sulfuric acid to carry out metathesis reaction, and the sulfuric acid addition is by the mol ratio 1.1: 1 of calcium ion in sulfate radical ion and refined acid hydrolyzate; Reaction temperature i...
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