Magnesium citrate crystal and production method thereof
A technology of magnesium citrate and its production method, which is applied in chemical instruments and methods, carboxylate preparation, carboxylate preparation, etc., and can solve problems such as inclusion and excess of reactants, low content of magnesium citrate crystals, doping, etc. , to increase content, prevent double-teaming and overdose
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Embodiment 1
[0044] This embodiment is used to illustrate magnesium citrate crystal of the present invention and production method thereof
[0045] The citric acid content is 25% by weight (density is 1102 kg / m 3 ) of citric acid feed solution once injected effective volume is 8m 3 In the crystallizer, then the magnesia slurry (based on the magnesia slurry, the content of magnesium element is 20% by weight) in 5m 3 The rate of / hour is continuously injected into the citric acid feed liquid for reaction crystallization. During the injection process, the temperature of the reaction crystallization is kept at 70°C, and the reaction end point is controlled by an online pH meter. When the pH of the feed liquid in the crystallizer is 6.8 , stop injecting the magnesium oxide slurry, keep it for 20 minutes, and obtain the crystal slurry liquid, then discharge the crystal slurry liquid, and carry out solid-liquid separation, and then dry at 90°C for 30 minutes to obtain the magnesium citrate crys...
Embodiment 2
[0047] This embodiment is used to illustrate magnesium citrate crystal of the present invention and production method thereof
[0048]The citric acid content is 20% by weight (density is 1081 kg / m 3 ) of citric acid feed solution once injected effective volume is 8m 3 In the crystallizer, then the magnesia slurry (based on the magnesia slurry, the content of magnesium element is 25% by weight) in 2.6m 3 The rate of / hour is continuously injected into the citric acid feed liquid for reaction crystallization. During the injection process, the temperature of the reaction crystallization is kept at 90°C, and the reaction end point is controlled by an online pH meter. When the pH of the feed liquid in the crystallizer is 7.5 , stop injecting the magnesium oxide slurry, keep it for 30 minutes, and obtain the crystal slurry liquid, then discharge the crystal slurry liquid, and carry out solid-liquid separation, and then dry at 110°C for 20 minutes to obtain the magnesium citrate cr...
Embodiment 3
[0050] This embodiment is used to illustrate magnesium citrate crystal of the present invention and production method thereof
[0051] The citric acid content is 35% by weight (density is 1144 kg / m 3 ) of citric acid feed solution once injected effective volume is 8m 3 In the crystallizer, then the magnesium hydroxide slurry (based on the magnesium hydroxide slurry, the content of magnesium element is 15% by weight) with 9.5m 3 The rate per hour is continuously injected into the citric acid feed liquid for reaction crystallization. During the injection process, the temperature of the reaction crystallization is kept at 60°C, and the reaction end point is controlled by an online pH meter. When the pH of the feed liquid in the crystallizer is 6.0 , stop injecting the magnesium oxide slurry, keep it for 10 minutes, and obtain the crystal slurry liquid, then discharge the crystal slurry liquid, and carry out solid-liquid separation, and then dry at 70°C for 40 minutes to obtain t...
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