Method for recycling phosphorus and fluorine in defluorination residues
A technology for defluorinated slag and phosphoric acid, applied in chemical instruments and methods, phosphate fertilizers, phosphate, etc., can solve problems such as defluorinated slag being put into the market, crop poisoning, and recycling of fluorine-free resources, achieving strong demonstration significance and promotion value , easy to promote, and improve the effect of using value
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Embodiment 1
[0025] Weigh 1000g of defluorination slag (P 2 o 5 content 29.8%, F content 7.1%, CaO content 30.1%, free water 5%), 98% sulfuric acid 554g, phosphoric acid back acid 4150g (P 2 o 5 Content 18.1%) quantitatively and continuously fed into the acid reaction tank, referring to the traditional method of sulfuric acid decomposition of phosphate rock, the reaction conditions are: control SO 3 The concentration is about 35g / L, the reaction temperature is 78°C, the reaction time is 4 hours, and the liquid-solid ratio is about 4:1. After the reaction is completed, filter, wash, and filter the obtained dilute phosphoric acid P 2 o 5 The content is about 26.1%, and the F content is about 5.6%. Take 1085g of dilute phosphoric acid as dilute phosphoric acid product and enter the concentration section.
[0026] Concentrate the above 1085g of dilute phosphoric acid at an absolute pressure of 10kPa and 75°C to obtain 611g of concentrated phosphoric acid (P 2 o 5 content of about 46...
Embodiment 2
[0028] Weigh 1650g of defluorination slag (P 2 o 5 content 13.7%, F content 4.8%, CaO content 28.1%, free water 39%), 98% sulfuric acid 850g, phosphoric acid back acid 4810g (P 2 o 5 Content 15.7%) quantitatively and continuously fed into the acid reaction tank, referring to the traditional method of sulfuric acid decomposition of phosphate rock, the reaction conditions are: control SO 3 The concentration is about 25g / L, the reaction temperature is 75°C, the reaction time is 3 hours, and the liquid-solid ratio is about 3.5:1. After the reaction is completed, filter, wash, and filter the obtained dilute phosphoric acid P 2 o 5 The content is about 18.2%, and the F content is about 5.7%. Take 1182g of dilute phosphoric acid as dilute phosphoric acid product and enter the concentration section.
[0029] Concentrate the above 1182g of dilute phosphoric acid at an absolute pressure of 11kPa and 80°C to obtain 607g of concentrated phosphoric acid (P 2 o 5content of about 35.3...
Embodiment 3
[0031] Weigh 1315g of defluorination slag (P 2 o 5 content 25.1%, F content 8.75%, CaO content 35.8%, free water 24%), 98% sulfuric acid 1008g, phosphoric acid back acid 2390g (P 2 o 5 Content 20.8%) quantitatively and continuously fed into the acid reaction tank, referring to the traditional method of sulfuric acid decomposition of phosphate rock, the reaction conditions are: control SO 3 The concentration is about 80g / L, the reaction temperature is 95°C, the reaction time is 1 hour, and the liquid-solid ratio is about 2:1. After the reaction is completed, filter, wash, and filter the obtained dilute phosphoric acid P 2 o 5 The content is about 28.1%, and the F content is about 9.1%. Take 1105g of dilute phosphoric acid as dilute phosphoric acid product and enter the concentration section.
[0032] Concentrate the above 1105g of dilute phosphoric acid at an absolute pressure of 10kPa and 78°C to obtain 578g of concentrated phosphoric acid (P 2 o 5 content of ab...
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