Production method of industrial-grade potassium dihydrogen phosphate coproduced water-soluble fertilizer
A technology of high-grade potassium dihydrogen phosphate and potassium dihydrogen phosphate, which is applied in the field of co-production of industrial-grade potassium dihydrogen phosphate water-soluble fertilizer, can solve the problems of water-soluble fertilizer production process confusion, low exchange solution concentration, and small exchange capacity, and achieve saving The effect of raw material cost and production energy consumption, simple process route and low raw material cost
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Embodiment 1
[0034] Example 1: Industrial grade potassium dihydrogen phosphate co-production water-soluble fertilizer production process
[0035] (1) With 40% P in the phosphoric acid workshop 2 o 5 Wet-process phosphoric acid and urea are used as raw materials. Wet-process phosphoric acid is filtered to remove solid insoluble matter, then heated to 65°C, and urea is directly added to phosphoric acid at a molar ratio of phosphoric acid to urea of 1.0:1.0. Concentrate the urea phosphate slurry to a specific gravity of 1.52, cool and crystallize, control the discharge temperature to 40°C and filter to obtain the urea phosphate product.
[0036] (2) Using urea phosphate and potassium hydroxide as raw materials, place urea phosphate and potassium hydroxide saturated solution at 50°C in the reaction tank with the molar ratio of urea phosphate and potassium hydroxide at a ratio of 1.0:1.5, and control the specific gravity of the slurry to 1.32, slurry temperature ≤ 95°C, filter to remove sol...
Embodiment 2
[0038] Example 2: Industrial grade potassium dihydrogen phosphate co-production water-soluble fertilizer production process
[0039] (1) With phosphoric acid plant 46%P 2 o 5 Wet-process phosphoric acid and agricultural high-quality urea are used as raw materials. After wet-process phosphoric acid is filtered to remove solid insoluble matter, it is heated to 75°C, and urea is directly added to phosphoric acid at a molar ratio of phosphoric acid to urea of 1.0:1.05. After constant temperature reaction for 60 minutes, 75 Concentrate the urea phosphate slurry under reduced pressure at a temperature of 1.52 to 1.52, cool and crystallize, control the discharge temperature to 45°C and filter to obtain a urea phosphate product.
[0040] (2) Using urea phosphate and potassium hydroxide as raw materials, place urea phosphate and potassium hydroxide saturated solution at 60°C in the reaction tank with a molar ratio of urea phosphate and potassium hydroxide of 1.0:1.6, and control the...
Embodiment 3
[0042] Example 3: Industrial grade potassium dihydrogen phosphate co-production water-soluble fertilizer production process
[0043] (1) Use 50% P in the phosphoric acid workshop 2 o 5 Wet-process phosphoric acid and urea are used as raw materials. Wet-process phosphoric acid is filtered to remove solid insoluble matter, then heated to 85°C, and urea is directly added to phosphoric acid at a molar ratio of phosphoric acid to urea of 1.0:1.10. Concentrate the urea phosphate slurry to a specific gravity of 1.52, cool and crystallize, control the discharge temperature to 50°C and filter to obtain the urea phosphate product.
[0044] (2) Using urea phosphate and potassium hydroxide as raw materials, place urea phosphate and a saturated solution of potassium hydroxide at 70°C in a reaction tank with a molar ratio of urea phosphate and potassium hydroxide of 1.0:1.7, and control the specific gravity of the slurry to 1.32, slurry temperature ≤ 95°C, filter to remove solid insolub...
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