Gelatin production pickling process control method
A technology of pickling and gelatin, which is applied in the control field of continuous pickling process, to achieve the effect of reducing uncertain factors, reducing errors and improving consistency
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Embodiment 1
[0027] Take 3 parts of raw bovine bone, 100g each, after washing, put it into a muffle furnace for calcination, the calcination temperature is 650°C, measure the average ash content in the raw material bone after calcination is 63.34g, calculate its calcium carbonate content as 6.334g , the content of tricalcium phosphate is 57g, and the theoretical acid consumption per ton of aggregate (30% concentration) calculated according to the calcium content is 104.9 tons.
[0028] After the aggregate pickling starts, measure the pH value of the inlet and outlet of each pool for continuous pickling, and take a sample test every half an hour; draw a curve with the pH value of the inlet and outlet as the ordinate, and the time as the abscissa, according to the acid concentration difference between the inlet and outlet Integrate by time to calculate the actual acid consumption as figure 1 :
[0029] Integral calculation shows that the actual acid consumption is 105.6 tons, which has reac...
Embodiment 2
[0033] Take 3 parts of raw pork bones, 100g each, wash them, put them into a muffle furnace for calcination, and the calcination temperature is 650°C. The average ash content in the raw material bones after calcination is measured to be 54.85g, and the calcium carbonate content is calculated to be 5.485g , the content of tricalcium phosphate is 49.37g, and the theoretical acid consumption per ton of aggregate (concentration 30%) is 90.8 tons based on the calcium content.
[0034] After the aggregate pickling starts, measure the pH value of the inlet and outlet of each pool for continuous pickling, and take a sample test every half an hour; draw a curve with the pH value of the inlet and outlet as the ordinate, and the time as the abscissa, according to the acid concentration difference between the inlet and outlet Integrate by time to calculate the actual acid consumption as figure 2 :
[0035] Integral calculation shows that the actual acid consumption is 92.2 tons, which h...
example 3
[0039] Get 3 parts of raw material mixed bone, each part of 100g, after cleaning, put into muffle furnace for calcination, the calcination temperature is 650 ℃, measure the ash content mean value in the raw material bone after calcination to be 57.75g, calculate its calcium carbonate content as 5.775g, the content of tricalcium phosphate is 51.975g, the theoretical acid consumption per ton of aggregate (30% concentration) is 95.67 tons according to the calcium content, if the volatilization in the acid mixing process is calculated as 5‰, the acid consumption should be 96.15 Ton.
[0040] After the aggregate pickling starts, measure the pH value of the inlet and outlet of each pool for continuous pickling, and take a sample test every half an hour; draw a curve with the pH value of the inlet and outlet as the ordinate, and the time as the abscissa, according to the acid concentration difference between the inlet and outlet According to time integration, calculate the actual aci...
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