Preparation method of strong-acidic water-soluble fertilizer special for alkaline soil
A strong acid water and soil technology, applied in fertilizer mixture, application, fertilization device and other directions, can solve the problems of complex process operation, limited application, not mass-produced by enterprises, etc., and achieve the effect of simple process flow and convenient operation.
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[0032] (1) Preparation of urea sulfate slurry:
[0033] Slowly add urea to 93-98wt% sulfuric acid, stir while adding, and control the temperature of the slurry in the reaction tank at 85-90°C, and stop adding urea when the pH value of the slurry is between 1.0-1.3 to obtain urea sulfate slurry;
[0034] (2) Preparation of powdered monoammonium phosphate:
[0035] (3) The urea sulfate slurry and powder monoammonium phosphate are passed through a liquid-solid mixer to obtain a semi-finished product; wherein the ratio of urea sulfate slurry and powder monoammonium phosphate is 50-95 parts by weight of monoammonium phosphate, and 5-50 parts by weight of urea sulfate ;
[0036] (4) The semi-finished product is dried, crushed and screened to obtain a strong acidic water-soluble fertilizer for alkaline soil.
[0037] As a preferred solution of the present invention, in the above-mentioned solution, the specific gravity of the urea sulfate slurry is controlled to 1.8-2.0kg / L, more ...
Embodiment 1
[0051] The specific operation steps are as follows:
[0052] (1) Slowly add urea into the first reaction kettle with 98% sulfuric acid, start stirring, remove the heat of reaction released by the reaction while adding urea, control the temperature of the slurry in the reaction tank at 85-90°C, and control the temperature of the slurry in the reaction tank. When the material pH value is between 1.0-1.3, stop adding urea, obtain the first raw material urea sulfate slurry, and keep warm for use;
[0053] (2) Slowly feed ammonia into the second reaction kettle with defluorinated wet-process phosphoric acid, and start stirring at the same time. When the pH value is between 4.2-4.6, stop feeding ammonia to obtain monoammonium phosphate slurry , after the slurry is spray-dried to obtain the powdered monoammonium phosphate raw material, wherein the air temperature entering the tower is controlled at 600°C, and the air temperature at the exit of the tower is 150°C;
[0054] (3) After ...
Embodiment 2
[0057] Concrete operation steps of the present invention are as follows:
[0058] (1) Slowly add urea into the first reaction kettle with 98% sulfuric acid, start stirring, remove the heat of reaction released by the reaction while adding urea, control the temperature of the slurry in the reaction tank at 85-90°C, and control the temperature of the slurry in the reaction tank. Material pH value is between 1.0-1.3, stops adding urea, obtains the first raw material urea sulfate slurry, and insulation stand-by;
[0059] (2) Slowly feed ammonia into the second reaction kettle with defluorinated wet-process phosphoric acid, and start stirring at the same time. When the pH value is between 4.2-4.6, stop feeding ammonia to obtain monoammonium phosphate slurry , after the slurry is spray-dried to obtain powdery monoammonium phosphate raw material, wherein the temperature of the air entering the tower is controlled at 500°C, and the air temperature at the exit of the tower is 100°C;
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