Method for removing crystal water in green vitriol
A technology for removing crystallization water and crystallization water, applied in the direction of ferric sulfate, etc., can solve the problems of scaling and wall sticking of drying equipment
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Embodiment 1
[0025] This embodiment is used to illustrate the method for removing the water of crystallization in the green vitriol provided by the invention.
[0026] Mix 100 parts by weight of green vitriol to be removed of crystal water and 5 parts by weight of calcium oxide evenly, and then add it to the rotary kiln (purchased from Beijing Zhuochuan Electronic Technology Co., Ltd., model ZZ99-SHY-I). In the rotary kiln Continuously feed air at a temperature of 30°C (based on 1kg of green vitriol to be removed from crystal water, the flow rate of the air is 0.5m 3 / h), and dried at a temperature of 60°C for 2 hours, then raised the temperature of the rotary kiln to 120°C for 2 hours, and then raised the temperature of the rotary kiln to 300°C for 2 hours to obtain anhydrous ferrous sulfate . The results show that there is no fouling and wall sticking phenomenon in the rotary kiln, and the production capacity of the rotary kiln is 15kg anhydrous ferrous sulfate / hour.
Embodiment 2
[0028] This embodiment is used to illustrate the method for removing the water of crystallization in the green vitriol provided by the invention.
[0029] Mix 100 parts by weight of green vitriol to be removed of crystal water and 10 parts by weight of calcium hydroxide evenly and then add it into the rotary kiln, and continuously feed air at a temperature of 100°C in the rotary kiln (with 1kg of water to be removed of crystal water Green vitriol as a benchmark, the flow rate of the air is 1.0m 3 / h), and dried at a temperature of 80°C for 1.5 hours, then raised the temperature of the rotary kiln to 100°C for 1.5 hours, and then raised the temperature of the rotary kiln to 350°C for 1 hour to obtain anhydrous ferrous sulfate . The results show that there is no fouling and wall sticking phenomenon in the rotary kiln, and the production capacity of the rotary kiln is 16kg anhydrous ferrous sulfate / hour.
Embodiment 3
[0031] This embodiment is used to illustrate the method for removing the water of crystallization in the green vitriol provided by the invention.
[0032] Mix 100 parts by weight of green vitriol to be removed of crystal water, 5 parts by weight of calcium oxide and 3 parts by weight of calcium hydroxide and add them into the rotary kiln. 1kg of green vitriol to be removed of crystal water is used as the benchmark, and the air flow rate is 0.7m 3 / h), and dried at a temperature of 70°C for 1 hour, then raised the temperature of the rotary kiln to 110°C for 1 hour, and then raised the temperature of the rotary kiln to 320°C for 1.5 hours to obtain anhydrous ferrous sulfate . The results show that there is no fouling and wall sticking phenomenon in the rotary kiln, and the production capacity of the rotary kiln is 13kg anhydrous ferrous sulfate / hour.
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