Industrial preparation of calcium carbonate nano bead string
A calcium carbonate, nano technology, applied in the direction of calcium carbonate/strontium/barium, etc., can solve problems such as unfavorable industrial production, complicated process operation, etc.
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Embodiment 1
[0019] CaCO 3 The content is 96%, MgCO 3 The natural limestone with a content of 0.7% is crushed and calcined, digested with hot water at 60°C, passed through a 250-mesh sieve, and diluted with water to prepare a refined calcium hydroxide feed liquid. The refined calcium hydroxide feed liquid is The concentration is 80 g / l.
[0020] to 20m 3 Add 14m to the reactor 3 Concentration above-mentioned calcium hydroxide slurry, then add 10 kilograms of sodium pyrophosphate, pass into the kiln gas that contains carbon dioxide and be 25% (volume concentration) and carry out carbonization, the flow rate of kiln gas is controlled at 650m 3 / h, the reaction temperature of the whole carbonization process shall not be higher than 40°C. When the carbonization reaches 8 to a pH value, add 8 kilograms of sodium lauryl sulfate and continue the carbonization until the reaction ends to obtain a uniformly dispersed calcium carbonate slurry for use, and the whole reaction is no more than 3 hour...
Embodiment 2
[0023] CaCO 3 The content is 96%, MgCO 3 The natural limestone content is 0.7%. After crushing and calcining, add hot water at 70°C for digestion, pass through a 250-mesh sieve, and dilute with water to prepare a refined calcium hydroxide feed liquid. The refined calcium hydroxide feed liquid is The concentration is 70 g / l.
[0024] to 20m 3 Add 12m to the reactor 3 Above-mentioned calcium hydroxide slurry, then add 20 kilograms of sodium pyrophosphates, pass into the kiln gas that contains carbon dioxide and be 25% (volume concentration) and carry out carbonization, the flow rate of kiln gas is controlled at 800m 3 / h, the reaction temperature of the whole carbonization process shall not be higher than 40°C. Carbon dioxide is passed through to carbonization until the end of the reaction to obtain a uniformly dispersed calcium carbonate slurry for use, and the whole reaction is no more than 3 hours.
[0025] The calcium carbonate slurry is filtered, dried at 150°C, and cr...
Embodiment 3
[0027] CaCO 3 The content is 96%, MgCO 3 The natural limestone with a content of 0.7% is crushed and calcined, digested with hot water at 60°C, passed through a 250-mesh sieve, and diluted with water to prepare a refined calcium hydroxide feed liquid. The refined calcium hydroxide feed liquid is The concentration is 80 g / l.
[0028] to 20m 3 Add 14m to the reactor 3 Above-mentioned calcium hydroxide slurry, add 40 kilograms of sodium pyrophosphates, pass into the kiln gas that contains carbon dioxide and be 40% (volume concentration) and carry out carbonization, the flow rate of kiln gas is controlled at 800m 3 / h, the reaction temperature of the whole carbonization process shall not be higher than 40°C. When the carbonization reaches 8 to the pH value, add 5 kilograms of sodium dodecylsulfonate and continue the carbonization to the end of the reaction to obtain a uniformly dispersed calcium carbonate slurry for use, and the whole reaction is no more than 3 hours.
[0029...
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