A method for improving the dispersibility of insoluble sulfur
A dispersive, sulfur technology, applied in the preparation/purification of sulfur, can solve the problems of a large amount of solvent washing, increase the ash content of the product, and exceed the ash content of the product, so as to reduce the consumption of resources and energy, improve the filling and sealing effect, reduce the The effect of the recycling step
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Embodiment 1
[0027] Add 4,000 kg of sieved insoluble sulfur powder into a jacketed horizontal twin-ribbon mixer, and melt 62# paraffin (melting point 62°C) through the The submerged pump, mass flow meter and nozzle of the insulation jacket quantitatively add 60 kg into the mixer, the paraffin temperature is 70°C, and the opening of the valve is adjusted to control the addition time of the molten paraffin to 10 minutes. The stirring shaft and the double-layer ribbon of the stirring mixer are hollow. While adding paraffin, the cooling circulating water is passed through the stirring shaft, double-layer ribbon and the jacket of the mixer to cool down the material in the mixer, and the temperature of the material is kept at 30- 40°C. Continue to stir at this temperature for 20 minutes after the paraffin wax is added, then add 940 kg of naphthenic oil into the mixer through the naphthenic oil nozzle for filling and mixing, and the oil filling is completed after mixing for 30 minutes.
[0028] ...
Embodiment 2
[0035] Add 4000 kilograms of insoluble sulfur powders through sieving in the horizontal twin-screw ribbon stirring mixer with jacket, under the stirring speed of 29 revs / min, the molten state rosin glyceride that temperature is 90 ℃ passes through with The submerged pump, mass flow meter and nozzle of the insulation jacket quantitatively add 80 kg into the mixer, and the opening of the valve is adjusted to control the addition time of rosin glyceride for 10 minutes. The stirring shaft and double-layer ribbon of the stirring mixer are hollow. While adding rosin glyceride, the cooling circulating water is passed through the stirring shaft, double-layer ribbon and mixer jacket to cool down the material, and the temperature of the material is kept at 30-40°C. . Continue to stir at this temperature for 20 minutes after the rosin glyceride is added, then add 920 kg of naphthenic oil into the mixer through the naphthenic oil nozzle for filling and mixing, and the oil filling is compl...
Embodiment 3
[0039] Add 4000 kg of sieved insoluble sulfur powder into a horizontal double-ribbon mixer with a jacket, and at a stirring speed of 29 rpm, the molten pentaerythritol stearate at a temperature of 70°C passes through A submerged pump with an insulating jacket, a mass flow meter and a nozzle quantitatively add 80 kilograms in the mixer, and the valve opening control pentaerythritol stearate addition time is 10 minutes. The stirring shaft and the double-layer ribbon of the stirring mixer are hollow. When pentaerythritol stearate is added, the cooling circulating water is passed through the stirring shaft, the double-layer ribbon and the jacket of the mixer to cool down the material, and the temperature of the material is kept at 30- 40°C. After pentaerythritol stearate was added, continue to stir at this temperature for 20 minutes, then add 920 kg of naphthenic oil into the mixer through the naphthenic oil nozzle for filling and mixing, and the oil filling was completed after mi...
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