Multielement compound fertilizer produced by utilizing waste catalyst and production method thereof
A production method and technology of compound fertilizer, applied in the application, fertilization device, fertilizer mixture and other directions, can solve the problems of unreasonable nutrient ratio, high use cost, unable to meet the demand of nutrients, etc., and achieve harmless treatment and resources. Chemical utilization, more nutrients, good fertilizer effect
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Embodiment approach 1
[0024] Raw material and weight ratio
[0025] 1.2 parts of waste catalyst, 1500 parts of mixed fertilizer;
[0026] production method:
[0027] 1. Acidify the waste catalyst with 98% sulfuric acid, and the consumption of sulfuric acid is 1.1 times of the molar weight of metal oxides participating in the acidification reaction in the waste catalyst to obtain acidification clear liquid and waste residue;
[0028] 2. Import the acidified clear liquid obtained in step 1 into the ammonium aluminum sulfate reactor, add ammonium chloride to generate ammonium aluminum sulfate crystals, and cool to a temperature below 35°C;
[0029] 3. After the ammonium aluminum sulfate crystals are separated by centrifugation, clear liquid A is obtained for subsequent use;
[0030] 4. Use the waste residue obtained in step 1 with a concentration of 15-20%, and the dosage is MoO in the waste residue 3 Soak in ammonia water 2.6 times the molar amount, the soaking temperature is controlled at 70-80°C...
Embodiment approach 2
[0035] Raw material and weight ratio
[0036] 1 part of waste catalyst, 1200 parts of mixed fertilizer
[0037] production method:
[0038] 1. Acidify the waste catalyst with 98% sulfuric acid, and the amount of sulfuric acid is 1.1 times of the molar weight of metal oxides participating in the acidification reaction in the waste catalyst to obtain acidification clear liquid and waste residue;
[0039] 2. Import the acidified clear liquid obtained in step 1 into the ammonium aluminum sulfate reactor, add ammonium chloride to generate ammonium aluminum sulfate crystals, and cool to a temperature below 35°C;
[0040] 3. After the ammonium aluminum sulfate crystals are separated by centrifugation, clear liquid A is obtained for subsequent use;
[0041] 4. Use the waste residue obtained in step 1 with a concentration of 15-20%, and the dosage is MoO in the waste residue 3 Soak in ammonia water 2.6 times the molar amount, the soaking temperature is controlled at 70-80°C, the pH ...
Embodiment approach 3
[0046] Raw material and weight ratio
[0047] 1.5 parts of waste catalyst, 1400 parts of mixed fertilizer
[0048] production method:
[0049] 1. Acidify the waste catalyst with 98% sulfuric acid, and the amount of sulfuric acid is 1.1 times of the molar weight of metal oxides participating in the acidification reaction in the waste catalyst to obtain acidification clear liquid and waste residue;
[0050]2. Import the acidified clear liquid obtained in step 1 into the ammonium aluminum sulfate reactor, add ammonium chloride to generate ammonium aluminum sulfate crystals, and cool to a temperature below 35°C;
[0051] 3. After the ammonium aluminum sulfate crystals are separated by centrifugation, clear liquid A is obtained for subsequent use;
[0052] 4. Use the waste residue obtained in step 1 with a concentration of 15-20%, and the dosage is MoO in the waste residue 3 Soak in ammonia water 2.6 times the molar amount, the soaking temperature is controlled at 70-80°C, the p...
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