Papermaking coating kaoline brightening and viscosity reducing process
A process method and kaolin technology, applied in fibrous fillers and other directions, can solve the problems that the comprehensive quality of kaolin products cannot be improved, the whiteness of kaolin cannot be guaranteed, and the effects of ensuring comprehensive product quality, stable product quality and reasonable design can be achieved.
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Embodiment 1
[0018] Example 1: Add water and sodium hexametaphosphate to the raw materials for pulping, classify through a three-stage cyclone, discard the sorted tailings, and then perform decanter classification. The pulp concentration of the decanter classification operation: 14~ 18%, separation factor: 3500-4000. The underflow is treated as filler, and the output pulp is subjected to high-gradient magnetic separation. Control conditions for high-gradient magnetic separation operation: pulp concentration: 8-12%, PH value: 6-7, magnetic field strength: 2.0 Tesla, separation cycle: 15 minutes / times. Discard the iron-containing tailings, and then carry out chemical bleaching. The pulp concentration of chemical bleaching: 10-12%, adding sulfuric acid: 1.8 kg / ton, sodium dithionite: 6.5 kg / ton, and bleaching time: 15 minutes. After centrifugal dehydration (removing submicron ions), dehydration by pressure filtration, and then adding surfactant sodium polyacrylate: 1.5 kg / ton, surface activa...
Embodiment 2
[0026] Step is the same as embodiment one. High gradient magnetic separation operation control conditions: pulp concentration: 8-10%, PH value: 6, magnetic field strength: 1.9 Tesla, sorting cycle: 15 minutes / time. Chemical bleaching operation control conditions: pulp concentration: 8-10%, sulfuric acid: 1.7 kg / ton, sodium dithionite: 6.6 kg / ton, bleaching time: 20 minutes. Surface activation treatment operation control conditions: add surfactant sodium polyacrylate: 1.4 kg / ton. Other operating control conditions are the same as in Embodiment 1, and the product is qualified.
Embodiment 3
[0028] Step is the same as embodiment one. High gradient magnetic separation operation control conditions: pulp concentration: 10-12%, PH value: 7, magnetic field strength: 2.2 Tesla, sorting cycle: 10 minutes / time. Chemical bleaching operation control conditions: pulp concentration: 10-12%, sulfuric acid: 1.9 kg / ton, sodium dithionite: 6.6 kg / ton, bleaching time: 10 minutes. Surface activation treatment operation control conditions: add surfactant sodium polyacrylate: 1.6 kg / ton. Other operating control conditions are the same as in Embodiment 1, and the product is qualified.
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