Feed of a mixture of chips and fluid from a low-pressure system to a high-pressure system
AssigneeMetso Fiber Karlstad AB
InventorVidar Snekkenes
Life of this patent
Estimating the term…
Abstract
Chips are sluiced from a low-pressure section to a high-pressure section with a sluice feeder. The fluid that is used to expel the chips from the sluice feeder principally includes pressurized fluid withdrawn from the treatment vessel. This pressurized fluid is normally withdrawn from the treatment vessel for recovery (REC). By using this pressurized fluid instead for expelling the chips from the sluice feeder and subsequently sending the previously pressurized fluid to the recovery system (REC), the requirement for high pressure pumps that consume large quantities of electrical energy can be considerably reduced.
Claims7
A method for feeding a mixture of cellulose chips and fluid from a low-pressure system to a high-pressure system during the continuous cooking of chemical cellulose pulp, comprising:
- arranging a sluice feeder between the low-pressure system and the high-pressure system for sluice feeding fluid and cellulose chips, the sluice feeder having a first inlet, a second inlet, a first outlet and a second outlet defined therein, the sluice feeder having a rotor with a first pocket and a second pocket placed alternately in connection with the high-pressure system and the low-pressure system;
- placing the first pocket, located in a first position, in connection with a chip bin or with an impregnation vessel while filling the first pocket with a chips mixture and at the same time expelling fluid present in the first pocket via the first outlet;
- placing the second pocket, located in a second position, via the second outlet in connection with a transfer line in the high-pressure system while feeding the chips mixture out from the second pocket;
- transporting the chips mixture onwardly to a treatment vessel in the high-pressure system with an aid of a fluid that is fed into the second pocket through the second inlet;
- connecting the second inlet via at least one withdrawal line connected to the treatment vessel;
- withdrawing pressurized fluid from the treatment vessel;
- positioning the first pocket into the second position so that the first pocket is in connection with the high-pressure system;
- using the pressurized fluid to expel chips mixture from the first pocket when the first pocket is in connection with the high-pressure system;
- positioning the first pocket in the first position so that the first pocket is in connection with the low-pressure system;
- withdrawing previously pressurized fluid from the first pocket via the first outlet of the sluice feeder;
- forwarding the previously pressurized fluid, withdrawn from the first outlet, directly to a recovery system wherein the withdrawn previously pressurized fluid constituting at least 20% of a total amount (RECtot) withdrawn for recovery, while being at least 1 m3/ton of pulp;
- and
- reducing a total amount of electrical energy required to pump a chips suspension from the low pressure system to the high pressure system through the sluice feeder.
Dependencies are inferred from the claim text.