Method for preventing scaling in pipeline of phosphoric acid production equipment
An anti-scaling and equipment technology, applied in phosphoric acid, phosphorus oxyacid, chemical instruments and methods, etc., can solve the problems of a lot of manpower and material resources, phosphorus loss, affecting the start-up rate of the device, etc., to improve the operation rate and shorten the cleaning time. , easy to use effect
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Embodiment 1
[0010] Embodiment 1: earlier with 3.2 tons of solid sodium lignosulfonate, 1.6 tons of solid sodium polyacrylate, add water and mix and stir evenly, be mixed with 160 tons of anti-scaling solution; Mass concentration of sodium lignosulfonate in the prepared anti-scaling solution The concentration of sodium polyacrylate is 2%, and the mass concentration of sodium polyacrylate is 1%. Then, after heating the anti-scaling solution to a temperature of 20°C, add it into the pipeline of phosphoric acid equipment, and run with the material.
Embodiment 2
[0011] Embodiment 2: 4 tons of sodium lignosulfonate and 2.4 tons of sodium polyacrylate were mixed with water and stirred evenly to prepare 160 tons of anti-scaling solution; the mass concentration of sodium lignosulfonate in the prepared anti-scaling solution was 2.5 tons %, the mass concentration of sodium polyacrylate is 1.5%; then, after heating the antiscalant to a temperature of 30°C, add it into the pipeline of the phosphoric acid equipment, and run with the material.
Embodiment 3
[0012] Example 3: 4.8 tons of sodium lignosulfonate as a solid substance and 3.2 tons of sodium polyacrylate as a solid substance were mixed with water and stirred evenly to prepare 160 tons of anti-scaling solution; the quality of sodium lignosulfonate in the prepared anti-scaling solution The concentration is 3%, and the mass concentration of sodium polyacrylate is 2%. After the scale inhibitor is heated to a temperature of 45°C, it is added into the pipeline of the phosphoric acid equipment, and it runs with the material.
[0013] After adopting this method, the running time of the concentration system is increased from 280 days / year to 300 days, and the production capacity of a single series is increased by 7000 tons / year.
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