Method for recycling iodine from diluted phosphoric acid for phosphoric acid manufacture with wet-process
A technology of wet-process phosphoric acid and dilute phosphoric acid, which is applied in the fields of chemical industry and environmental protection, and can solve the problems of high iodine content in raw materials, affecting normal production, and high production and operation costs.
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Embodiment 1
[0011] Embodiment 1 of the present invention: extract iodine from dilute phosphoric acid produced by wet process phosphoric acid, wherein the content of iodine in dilute phosphoric acid is: 50~110mg / L, P in dilute phosphoric acid 2 o 5 The concentration is 25-30%, and 0.01 kg of composite oxidant is added to 100 kg of the dilute phosphoric acid. The ratio of composite oxidizer is 27-35% of hydrogen peroxide, 0.1-0.2% of vanadium pentoxide, and the rest is water, namely Add 0.1~0.2% vanadium pentoxide to hydrogen peroxide. Mix for 5 minutes to carry out the oxidation reaction, then blow out the molecular iodine with hot air at 40 degrees Celsius, the volume ratio of the hot air blown to the liquid is 130:1, and then use 2 When the iodine content in the obtained liquid reaches 100g / L, add 0.5 kg of hydrogen peroxide per 100 kg of the obtained liquid to precipitate iodine, filter and centrifuge to obtain the finished iodine.
Embodiment 2
[0012] Embodiment 2 of the present invention: extract iodine from dilute phosphoric acid produced by wet-process phosphoric acid, wherein the content of iodine in dilute phosphoric acid is: 50mg / L, P in dilute phosphoric acid 2 o 5 Concentration is 25%, in 1000 kilograms of this dilute phosphoric acid, add 0.5 kilogram of composite oxidant, the proportion of composite oxidizer is hydrogen peroxide 30%, vanadium pentoxide 0.2%, the remainder is water, mixes 30 minutes and carries out oxidation reaction, Then use 40 degrees centigrade hot air to blow out the molecular iodine therein, the volume ratio of the hot air blown and the liquid is 150: 1, then use SO2 acidic solution circulation absorption, when the content of iodine in the obtained liquid reaches 150g / L, every Add 3 kg of hydrogen peroxide to 100 kg of the obtained liquid to precipitate iodine, filter and centrifuge, and refine to obtain finished iodine.
Embodiment 3
[0013] Embodiment 3 of the present invention: extract iodine from dilute phosphoric acid produced by wet-process phosphoric acid, wherein the content of iodine in dilute phosphoric acid is: 100mg / L, P in dilute phosphoric acid 2 o 5 The concentration is 41%. Add 1 kg of composite oxidant to 1000 kg of dilute phosphoric acid. The ratio of composite oxidant is 1 kg of 30% hydrogen peroxide, add 20 g of vanadium pentoxide, and mix for 10-20 minutes to oxidize. The reaction and oxidation reaction time are controlled within 10 to 20 minutes, which can not only ensure sufficient oxidation reaction, but also control production time and reduce production cost. Then use 40 degrees Celsius hot air to blow out the molecular iodine, the volume ratio of the hot air to the liquid is 150:1, and then use SO 2 When the iodine content in the obtained liquid reached 150g / L, 2 kg of hydrogen peroxide was added in every 100 kg of the obtained liquid to precipitate iodine, filtered and centrifuged...
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