Method and a digester for the continuous cooking of wood raw material to cellulose pulp
AssigneeMetso Fiber Karlstad AB
InventorVidar Snekkenes
Life of this patent
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Abstract
The digester and method are for the continuous cooking of pulp. At least two withdrawal positions (11E, 11D) for cooking fluid are arranged at different heights in the digester (10). The cooking fluid in the first and second position is withdrawn after the chips have had a retention time that differs by at least 10 minutes. The differential pressure between the positions is determined and when this exceeds a pre-determined level, a connection (17E) opens between these positions, establishing a flow parallel to a flow of cooking fluid between these positions in the digester. Several withdrawal positions are preferably connected in a common shunt system (17A-17F), with valves (18A-18F), controlled by the differential pressure, that are located between adjacent positions.
Claims10
A method for the continuous cooking of wood raw material for the production of cellulose pulp, comprising:
- feeding a wood raw material and a cooking fluid to a top of a continuous digester;
- establishing a cooking temperature of 130-170° in the digester while the wood raw material experiencing a retention time of at least 90 minutes at the cooking temperature;
- the wood raw material sinking continuously through the digester from the top down to a bottom of the digester in order to finally expelling the wood raw material from the bottom of the digester;
- arranging a first withdrawal position in the digester for the cooking fluid and arranging a second withdrawal position in the digester for the cooking fluid, the second withdrawal position being above the first withdrawal position;
- withdrawing cooking fluid at the first and second withdrawal positions, the wood raw material having experienced a first retention time in the digester at the first withdrawal position and a second retention time in the digester at the second withdrawal position, the first retention time being at least 10 minutes different from the second retention time;
- establishing a zone of a countercurrent or a concurrent flow in the digester between the first and second withdrawal positions;
- providing an openable shunt line extending between the first withdrawal position and the second withdrawal position, the shunt line being in a closed position;
- a differential pressure (ΔP) between the second withdrawal position and the first withdrawal position falling below a first predetermined threshold value or rising above a second predetermined threshold value;
- and
- opening the shunt line extending between the first and second withdrawal positions.
Dependencies are inferred from the claim text.