Continuous production method and device of sodium gluconate
The technology of a sodium gluconate and production method is applied in the continuous production method and device field of sodium gluconate, which can solve the problems of increasing enzyme consumption, large enzyme addition amount, high cost, etc., and achieve saving of addition amount, increase of concentration, The effect of improving productivity
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Embodiment 1
[0040] The present embodiment provides a continuous production device 100 of sodium gluconate, such as figure 1 As shown, it includes: a reaction tank 110, a first buffer tank 120, a second buffer tank 130 and a storage tank 140, and the drain port 111 of the reaction tank 110 can be optionally connected with the first buffer tank 120 or the second buffer tank 130 Connect, the reaction tank 110 has the first feed port 112 (they walk different feed ports for accessing glucose, glucose oxidase, catalase, and sodium hydroxide solution, and different lines represent different feeds as shown in the figure) tube), the first buffer tank 120 and the second buffer tank 130 all have the second feed port 121 for adding sodium hydroxide solution; The third feed port 141 for the reaction liquid in 130.
Embodiment 2
[0042] The present embodiment provides a kind of continuous production method of sodium gluconate, it adopts the continuous production device 100 as shown in embodiment 1, and it comprises:
[0043] a. At 200m 3 Add 130m to the reaction tank 3 Glucose (concentration: 350g / L), 10kg defoamer, 52.5kg glucose oxidase (enzyme activity: 8.736 million U / ml), 52.5kg catalase (enzyme activity: 375,000 U / ml) , start the reaction, add 33wt% sodium hydroxide to control the pH of the reaction solution and maintain it at 5.3, the tank pressure is controlled at 0.14MPa, and the controlled rotating speed and air volume maintain 35% of dissolved oxygen in the tank.
[0044] b. When the enzyme activity of glucose oxidase in the reaction tank drops to 3000U / mL, start feeding glucose oxidase and catalase with a mass ratio of 1:1, and control the flow acceleration rate to maintain the concentration of glucose oxidase in the reaction tank. The enzyme activity is 3050U / mL.
[0045] c. After the r...
Embodiment 3
[0051] The present embodiment provides a kind of continuous production method of sodium gluconate, it adopts the continuous production device 100 as shown in embodiment 1, and this method comprises:
[0052] a. At 200m 3 Add 130m to the reaction tank 3 Glucose (concentration: 300g / L), 10kg defoamer, 50kg glucose oxidase (enzyme activity: 9.5 million U / ml), 50kg catalase (enzyme activity: 380,000 U / ml), start To react, add 33wt% sodium hydroxide to control the pH of the reaction solution to maintain 5.5, the tank pressure to be controlled at 0.14MPa, and control the rotating speed and air volume to maintain 25% of dissolved oxygen in the tank.
[0053] b. When the enzyme activity of glucose oxidase in the reaction tank drops to 2500U / mL, start feeding glucose oxidase and catalase with a mass ratio of 1:0.5, and control the flow acceleration to maintain the concentration of glucose oxidase in the reaction tank. The enzyme activity is 3000U / mL.
[0054] c. After the reaction w...
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