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The basic idea of continuous cooking is to close the chain of continuous processes
in the fiber line. Based on the original process, technologies have developed over
time which employ in-digester washing and advanced alkali and temperature profiling.
The outline of a typical single-vessel continuous cooking system is illustrated in
Fig. 4.137. Vapor recovered from the extraction liquor is used to remove air from
the chips and to preheat them. The chips are then continuously transported to the
digester with the help of liquor circulated between the chip feeding system and
the digester top. A percentage of the cooking chemicals is charged with white
liquor to the top circulation, while the remainder of the white liquor goes to the
digester.
The continuous digester itself is a huge vessel of vertical cylindrical design.
Chips move from the top of the digester to the bottom by gravity. The vessel is
equipped with a top separator, which separates the circulation liquor from the
chips, and with a scraper and outlet device in the bottom. The digester has strainers
at different levels, which hold back wood and pulp when liquor is extracted
from the digester. Several liquor circulation loops are used to change the chemical
regime and/or to adjust the temperature in the different zones of the digester. A
central pipe discharge brings the circulation liquor back to the center of the digester
near the corresponding set of circulation screens. Steam is used for liquor
heating, preferably in indirect shell-and-tube heat exchangers.
Spent liquor which is not circulated back to the cooking process is extracted for
vapor recovery. The weak black liquor is then subjected to fiber separation and
cooling before being transferred to the evaporation plant.
Continuous cooking systems can be categorized into single-vessel and two-vessel
systems, with hydraulic or steam/liquor phase digesters. Two-vessel systems have a
separate vessel where the impregnation of chips takes place. In such a system, the
chips are fed to the top of the impregnation vessel and then transferred from the bottom
of the impregnation vessel to the digester top by a separate circulation loop.
CHIP STEAMING,
CHIP FEEDING
SYSTEM
VAPOR
RECOVERY
SYSTEM
Extraction liquor
Pulp
Chips Top
circulation
liquor
Chips and liquor
Wash filtrate
Weak black liquor
Vapor
DIGESTER
White liquor
Steam
Fig. 4.137 Outline of single-vessel continuous cooking system.
4.2 Kraft Pulping Processes 377
Hydraulic digesters are completely filled with liquor, whereas steam/liquor phase
digesters have a vapor phase at the top. In a steam/liquor phase digester, the chips
reach above the liquor level. They can be heated to cooking temperature with
direct steam, which in most cases requires prior impregnation and therefore
makes sense mainly in a two-vessel system.
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