Method for supplying washing liquid to a process for cooking cellulose pulp
View Patent ↗The invention relates to a method for supplying washing liquid to a digester ( 1 ) for cellulose pulp and a subsequent diffuser washing device ( 2 a, 2 b). A high, disturbance-free production capacity can be obtained by using a common feed pump (P 1 ) which, via a main feed line ( 10 ), supplies both the diffuser washing device and the digester with washing liquid in parallel. The first pump (P 1 ) establishes a pressure on the washing liquid which is in the interval 2–6 bar, and is preferably 4 bar, while the second pressure level, which is established by the diffuser pump device (P 2 a , P 2 b ), is in the interval 6–12 bar, but is at least 2 bar higher than the first pressure level, and the third pressure level, which is established by the digester pump (P 3 ), is in the interval 12–25 bar The system becomes self-regulating in the event of any operational disturbances in the flow of washing liquid and, if the pumps are appropriate, a countercurrent flow of washing liquid through the system is essentially maintained.
1. Method for supplying washing liquid to a digester ( 1 ) for cellulose pulp and a subsequent diffuser washing device ( 2 a , 2 b ), with washing liquid for the diffuser wash being collected from a storage tank ( 4 ) and with washing liquid being conducted to the bottom of the digester for the purpose of obtaining a dilution and/or displacement wash at the bottom of the digester, characterized in that
the washing liquid from the storage tank ( 4 ) is pressurized to a first pressure level via a first feed pump (P 1 ) and conducted onwards to a main feed line ( 10 ),
a first constituent flow ( 11 ) is drawn from the main feed line ( 10 ), at a first upstream point 10 a ) on the main feed line, to a diffuser pump device (P 2 a , P 2 b ), which pressurizes the washing liquid to a second pressure level, and is conducted onwards ( 12 a , 12 b ), at this second pressure level, to washing liquid inlets ( 14 a , 14 b ) of a diffuser washing device,
wash filtrate from a washing liquid outlet ( 15 a , 15 b ) of the diffuser washing device ( 2 a , 2 b ) is returned to the main feed line ( 10 ) at a second point ( 10 b ) on the main feed line, which point is located downstream of the first upstream point ( 10 a ) on the main feed line,
a combined flow of washing liquid from the storage tank ( 4 ) and wash filtrate ( 16 ) from the diffuser washing device ( 2 a , 2 b ) is conducted, via the main feed line ( 10 ), to a digester pump (P 3 ) which pressurizes the combined flow to a third pressure level and conducts the combined flow ( 17 ) onwards, at this third pressure level, to washing liquid nozzles ( 18 ) which are arranged at the bottom of the digester.
2. Method according to claim 1 , characterized in that the first pressure level is lower than the second pressure level, which second pressure level is in turn lower than the third pressure level.
3. Method according to claim 2 , characterized in that each respective pressure level constitutes an increase in pressure of at least 50–125% as compared with the next lower pressure level.
4. Method according to claim 1 , characterized in that the diffuser washing device ( 2 a , 2 b ) consists of at least one pressure diffuser, which maintains a positive pressure in the pulp during the washing.
5. Method according to claim 1 , characterized in that the diffuser washing device consists of two diffuser washing devices ( 2 a , 2 b ), which are coupled in parallel with regard to the receipt and treatment of cooked pulp ( 20 ) obtained from the digester.
6. Method according to claim 5 , characterized in that the diffuser pump device consists of two diffuser pumps (P 2 a , P 2 b ) which are coupled in parallel and which are connected, on the inlet side, to the first constituent flow ( 11 ) taken from the main feed line ( 10 ), with the respective outlet from each of the diffuser pum devices only supplying one diffuser.
7. Method according to claim 6 , characterized in that the wash filtrate ( 13 a , 13 b ) which is obtained from each respective diffuser is firstly combined into a joint flow ( 16 ) in a Y coupling, after which this combined wash filtrate flow is returned to the main feed line ( 10 ) at the second point point ( 10 b ) on the main feed line which is closer to the inlet of the digester pump (P 3 ).
8. Method according to claim 1 , characterized in that the system for supplying the washing liquid to the digester and diffuser lacks any buffer or intermediate storage tanks after the first feed pump (P 1 ) has pressurized the washing liquid.