Method for solid-liquid separation during sheet production through papermaking process
A technology for solid-liquid separation and papermaking, which is applied in the separation of sediments, tobacco, and food science by centrifugal force, and can solve the problems of low requirements for solid-liquid separation and singleness, so as to reduce the cost of cigarettes, improve the yield, and save money. The effect of resources
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Embodiment 1
[0020] 600kg of tobacco stems and 600kg of tobacco leaf fragments were soaked in hot water at 40°C and 30°C for 1.5 hours respectively, extracted, and the tobacco leaf fragments were directly pumped into a decanter centrifuge. The solid tobacco stem residue and the solid tobacco leaf fragment residue are obtained, and the filtrates are combined to obtain an extraction centrate 1. The absolute dry solid content of solid slag is 28.3% (tested by oven method at 105°C to constant weight), and the liquid slag content rate is 1.2%. The solid slag is made into a thin sheet substrate. The extracted centrifugate 1 was passed through a decanter centrifuge again to obtain a centrifuge 2 with a slag content rate of 0.50%. The centrate 2 is passed through the disc separator to obtain the centrate 3, the liquid slag rate is 0.08%, and the centrate 3 is pumped into the three-legged upper discharge centrifuge for centrifugation (the filter bag mesh number is 1000 mesh) to obtain the centrate...
Embodiment 2
[0024] 600kg of tobacco stems and 600kg of tobacco leaf fragments were soaked in hot water at 40°C and 30°C for 1.5 hours respectively, extracted, and the tobacco leaf fragments were directly pumped into a decanter centrifuge. The solid tobacco stem residue and the solid tobacco leaf fragment residue are obtained, and the filtrates are combined to obtain an extraction centrate 1. The dry average solid content of solid slag is 28.4%, and the liquid slag content rate is 1.3%. The solid slag is made into a thin sheet substrate. The extracted centrifugate 1 was passed through a decanter centrifuge again to obtain a centrifuge 2 with a slag content rate of 0.51%. The centrifugate 2 is passed through the disc separator to obtain the centrifugate 3, and the liquid slag rate is 0.07%, and the centrifugate 3 is pumped into the flat plate upper discharge centrifuge for centrifugation (the filter bag mesh number is 1000 mesh), and the centrifugate 4 is obtained. , the liquid slag conte...
Embodiment 3
[0028] 600kg of tobacco stems and 600kg of tobacco leaf fragments were soaked in hot water at 40°C and 30°C for 1.5 hours respectively, extracted, and the tobacco leaf fragments were directly pumped into a decanter centrifuge. The solid tobacco stem residue and the solid tobacco leaf fragment residue are obtained, and the filtrates are combined to obtain an extraction centrate 1. The absolute dry solid content of solid slag is 28.3%, and the liquid slag content rate is 1.2%. The solid slag is made into a thin sheet substrate. The extracted centrifugate 1 was passed through a decanter centrifuge again to obtain a centrifuge 2 with a slag content rate of 0.50%. The centrate 2 is passed through the disc separator to obtain the centrate 3, the liquid slag rate is 0.08%, and the centrate 3 is pumped into the three-legged upper discharge centrifuge for centrifugation (the filter bag mesh number is 600 mesh) to obtain the centrate 4. The liquid residue rate is 0.012%. The centrifu...
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