Clean production method of potassium chromate
A clean production and potassium chromate technology, applied in the direction of chromate/dichromate, etc., can solve the problems of serious environmental pollution, low yield of potassium chromate, high energy consumption, etc., achieve dust-free waste gas, and improve chromium recovery The effect of rate and reaction process enhancement
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Embodiment 1
[0030] Please see attached image. Circulate the KOH solution returned to the reactor to remove part of the water, then heat up to 250°C, add 95% chromite with a particle size of less than 200 mesh, add potassium peroxide, and react for 6 hours under complete mixing conditions, wherein KOH and ore The weight ratio is 2:1; a mixed reaction product containing lye, chromium salt and iron slag is obtained; the conversion rate of chromium is above 99%. The mixed reaction product is leached with iron slag washing solution, and the temperature after leaching is 80°C; the leaching slurry is separated at 60°C to separate the coarse crystals of potassium chromate, and the iron slag and lye are separated by filtration; the coarse crystals of potassium chromate are added with water Dissolve and filter to remove a small amount of iron slag; add carbon dioxide to the potassium chromate solution to adjust pH = 6, separate and remove impurities to obtain pure potassium chromate solution; the p...
Embodiment 2
[0032] Please see attached image. The KOH solution that circulates back to the reactor removes part of the water and heats up to 320°C. Add 95% of the chromite with a particle size of less than 200 meshes, introduce air, and react for 3 hours under complete mixing conditions. Among them, the weight ratio of KOH to ore The ratio is 4:1, and the mixed reaction product containing lye, chromium salt and iron slag is obtained; the conversion rate of chromium is over 99%. The mixed reaction product is leached with iron slag washing solution, and the temperature after leaching is 140°C; the leaching slurry is separated at 110°C to separate the coarse crystals of potassium chromate, and the iron slag and lye are separated by filtration; the coarse crystals of potassium chromate are added with water Dissolve and filter to remove a small amount of iron slag; add potassium dichromate to the potassium chromate solution to adjust the pH=7, filter and separate to remove impurities to obtain...
Embodiment 3
[0034] Please see attached image. Circulate the KOH solution returned to the reactor to remove part of the water, then heat up to 400°C, add 95% chromite with a particle size of less than 200 mesh, add potassium nitrate, and react for 1 hour under complete mixing conditions, wherein the weight ratio of KOH to ore The ratio is 6:1, and a mixed reaction product containing lye, chromium salt and iron slag is obtained; the conversion rate of chromium is above 99%. The mixed reaction product is leached with iron slag washing solution, and the temperature after leaching is 180°C; the leaching slurry is separated at 120°C to separate the coarse crystals of potassium chromate, and the iron slag and lye are separated by filtration; the coarse crystals of potassium chromate are added with water Dissolve with the crystalline mother liquor of Example 2, remove a small amount of iron slag by filtration; add chromic anhydride to the potassium chromate solution to adjust pH=8, filter and sep...
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