Mitigation technique in use for producing bleached chemical pulp by using raw material of grass
A technology for chemical pulp and raw material pulp, applied in the field of dispersing technology, can solve the problems of low impurity removal rate, pollution, difficulty in recovery of alkali from cooking black liquor, etc.
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Embodiment 1
[0034]The rice straw is cooked by the ammonium method. After cooking, the hardness of the rice straw pulp is 16 potassium permanganate value, which is equivalent to the kappa value of 24. The straw pulp is transported to the deflagging machine for deflaking. It is 20°SR. It can be seen by the naked eye that there are no rod-shaped fibers after the straw pulp has been decompressed, which shows that the effect of fiber bundle separation can be achieved through the decompression operation. The decompression degree of the straw pulp after decompression is 22° SR, relative to the rice straw pulp before deflaking, the temperature of the straw pulp after deflaking increases by about 5-10°C. The decomposed straw pulp is then pumped to the screw press machine for "concentrated" black liquor treatment, the obtained thick black liquor can be used for subsequent evaporation as fertilizer, and the concentration of the extruded pulp is changed from that before extrusion to 10% is brought up...
Embodiment 2
[0036] The wheat straw is cooked by the ammonium method. After cooking, the hardness of the wheat straw pulp is 18. The potassium permanganate value is equivalent to the kappa value of 29. The wheat straw pulp is pumped to the screw press for squeezing, and the extruded black The liquid is evaporated and used as fertilizer, and the concentration of the extruded pulp is increased from 8% before the extrusion to 19%. At this time, the pH value of the pulp is 8, and the concentration of the extruded black liquor is 11 ° Be (20 ° C), and the residual ammonium is 8g / L, transport the pulp obtained after pulping to the high-frequency deflaking machine for deflaking, and at the same time add alkali with a concentration of 36g / L to the deflaking equipment, the weight of the lye is the mass of the dry pulp 2%, the knocking degree of the wheat straw pulp before deflaking is 20°SR, it can be seen by the naked eye that after the deflaking operation, the wheat straw pulp has no rod-shaped f...
Embodiment 3
[0038] Cotton stalks are cooked by alkaline method. After cooking, the hardness of cotton stalk pulp is 20. The potassium permanganate value is equivalent to 34 kappa value. The concentration of the pulp is increased from 8% before squeezing to 20%. At this time, the pH value of the pulp is 8.5. The obtained pulp is added to the black liquor for jumping screen. Before the jumping screen, adjust the concentration of the pulp and dilute the concentration of the pulp to 3.0%, the skipping sieve loss is 0.2%, and then the pulp obtained after skipping the screen is transported to the deflaking machine for deflaking, and at the same time, add alkali with a concentration of 38g / L to the deflaking equipment, and the weight of the lye is the dry pulp mass 3%, the degree of knocking of the cotton stalk pulp before deflaking is 20°SR, and it can be seen by the naked eye that there are no rod-shaped fibers after the cotton stalk pulp that has undergone the deflaking operation, which shows ...
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