Continuous digester with fluid circulation
View Patent ↗The arrangement concerns an improved design for at least one of the cooling, dilution and washing at the bottom of a continuous digester for the production of cellulose pulp. By arranging at least one extra strainer section above the lowermost strainer section, with the addition of washing fluid or dilution fluid between the extra strainer section and the lowermost strainer section, more washing fluid can be added at the bottom of the digester without counteracting the flow of the column of chips. This provides space for the increase of production, for improvement of the flow of the column of chips, or for combinations of these effects while retaining good cooling, washing and dilution at the bottom of the digester.
1. A method for adding and withdrawing fluids in a final wash stage in a digester, comprising:
providing a digester having an inlet and an outlet defined therein, the digester having a lowermost wash strainer section disposed at a bottom of the digester, the lowermost wash strainer section having a strainer surface arranged along a circumference of an inner wall of the digester, the digester further having an extra wash strainer section disposed above the lowermost wash strainer section inside the digester, the extra wash strainer being spaced away from the lowermost wash strainer section so that a gap is defined therebetween in a gap segment of the digester,
continuously feeding wood chips through the inlet at a top of the digester and cooking the wood chips in a cooking fluid to form cellulose pulp in the digester,
the lowermost wash strainer section and the extra wash strainer section withdrawing consumed cooking fluid from the digester,
a plurality of gap nozzles, disposed in the gap around the circumference of the inner wall of the digester,
continuously providing a dilution fluid or a washing fluid radially inwardly into a column of pulp disposed in the gap of the digester,
a plurality of bottom nozzles, disposed under the lowermost wash strainer section between the lowermost wash strainer section and the outlet, adding dilution fluid or washing fluid into the column of pulp disposed below the lowermost wash strainer section, and
continuously feeding the cellulose pulp through the outlet at the bottom of the digester.
2. The method according to claim 1 wherein the method further comprises the step of pumping dilution fluid or washing fluid into a distribution channel that runs around the inner wall of the digester, the distribution channel being in fluid communication with the gap nozzles.
3. The method according to claim 1 wherein the method further comprises the step of evenly distributing the gap nozzles along the circumference of the digester.
4. The method according to claim 1 wherein the method further comprises the step of each gap nozzle delivering a concentrated jet into the column of pulp.
5. The method according to claim 1 wherein the method further comprises the step of dividing a total volume of wash or dilution liquid added to the bottom of the digester in at least two layered wash stages, each layered wash stage having a strainer section and nozzles for addition of wash or dilution liquid below the strainer section, such that a total lifting force on the column of pulp created by the addition of the total volume of wash or dilution liquid is reduced.
6. A method for adding and withdrawing fluids in a final wash stage in a digester, comprising:
providing a digester having an inlet and an outlet defined therein, the digester having a first wash strainer section and a second strainer section, the first wash strainer section being above the second wash strainer section at a bottom of the digester so that the first and second wash strainer sections each forms a layered wash stage, the first wash strainer section having inwardly directed radial nozzles, disposed between the first and second wash strainer sections, for adding a wash or dilution fluid below the first strainer section,
the second wash strainer section having nozzles for adding a wash or dilution fluid below the second strainer section,
feeding wood chips through the inlet at a top of the digester and cooking the wood chips in a cooking fluid to form cellulose pulp in the digester,
withdrawing consumed cooking fluid from the first and second wash strainer sections,
dividing a total volume of the wash or dilution fluid added to the first and second wash strainer sections at the bottom of the digester such that a total lifting force, created by the addition of the total volume on a column of pulp, is reduced,
the nozzles, disposed between the first and second wash strainer sections, being disposed around a circumference of an inner wall of the digester, continuously providing a first portion of the total volume of the dilution fluid or a washing fluid radially inwardly into a column of pulp disposed in the digester,
the nozzles, disposed under the second wash strainer section between the second wash strainer section and the outlet, adding a second portion of the total volume of the dilution fluid or washing fluid into the column of pulp disposed below the second wash strainer section, and feeding the cellulose pulp through the outlet at the bottom of the digester.