Fraction of pulp that is retained on a 3/8” perforated plate
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defibering
Improves the fiber properties and reduces the refining requirements later
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brown stock washers
The most removal of pulping chemicals and lignin with the least amount of wash water
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cleanliness of the pulp and the amount of water used
compromise of brown stock washing
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pulp moves opposite direction of the wash water
brown stock washing sequence
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washing and leaching
brown stock washing mechanisms
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leaching
diffusion and desorption
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diffusion
dissolved solids and chemicals in the interior of the pulp fibers must move into the surrounding liquor to be removed
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desorption
attached dissolved solids and chemicals leaved the fibre surface for the surrounding liquor
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displacement
liquor in the pulp is displaced with weaker wash liquor or clean water
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dilution/extraction
pulp slurry is diluted and mixed with weak was liquor or clean water. then the liquor is extracted by thickening the pulp.
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rotary vacuum washer
type of washer used at IP
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drop leg
applied to siphon the water from the washer
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specific loading
oven dry tons of pulp per square foot of cylinder surface
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air
as much as possible must be removed to avoid foaming problems
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dilution factor
weight of wash water introduced into the black liquor per unit of weight of oven dry pulp being washed
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displacement ratio
measures the effectiveness of a single washing stage
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displacement ratio
=(Cv-Cs)/(Cv-Cw)
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thickening factor
(Win-Wout)/Win
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wash loss
amount of washable compounds in the pulp suspension that could have been removed in washing
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soda loss
washable sodium content of the pulp leaving with the pulp
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total soda loss
washable sodium and chemically bound sodium leaving with the pulp
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drum displacer
incorporates all washing stages on a single rotary drum
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horizontal belt washer
resembles fourdrinier
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diffusion washing
submerged environment, long contact time between the chips and the washing water
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kamyr atmospheric diffusion washer
kamyr used at IP
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brown stock washing efficiency
determined by the amount of solute is removed and the amount of wash water needed to remove that solute
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norden’s method
measures the degree of polymerization (viscosity test)
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screening
operation of removing oversized, troublesome particles and shives
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vibratory
type of screen, obsolete, rotary of flat form
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gravity centrifugal screens
type of screen, mostly obsolete, good fibers hydrate well and align themselves with the direction of the flow, while coarse fibers do not hydrate well and are carried across the plate
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pressure
type of screen that is most dominantly used, utilizes perforated cylindrical plates
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Er
=(Sr/Si)\*Rw
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centrifugal cleaning
removal of contaminants or unwanted particles from pulp and paper stock by centrifugal force and fluid shear
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3\.5-4%
slusher, pulp is retained on the cylinder and excess water passes through wire mesh cylinder
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4-8%
gravity thickener, same as slusher but a couch roll is added
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10-12%
valveless washers are used
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dilute stocks to 12%
multidisk thickeners are used
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12-16%
vacuum washers are used to extract more water from the pulp slurry
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above 15%
screw presses are used
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newtonian fluid
has constant viscosity regardless of the shear rate or applied stress
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blending
reduces variations in kappa number and improves the bleaching control
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dewatering
needed if transporting pulp
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boiling point rise
liquid mixture that contains dissolved organic and/or inorganic substances will boil at a higher temperature than water at the same pressure
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sodium sulfite
compound that sulfur is converted to during chemical recovery
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13-18%
concentration of solids in black liquor leaving the washers
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60-80%
what is the ideal solid concentration in black liquor before burning in the recovery furnace?
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steam is applied countercurrent to the liquor
how do multi-stage evaporators work?
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long tube
most common type of evaporator unit, entering weak liquor boils and thickens as it travels quickly up the tubes
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thermosiphon
fluid, usually a liquid or a gas, is driven by temperature differences. It is a passive system that does not require any mechanical pump or external power source to move the fluid
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falling film
indirectly heated evaporators, industry standard
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cascade
type of evaporator that consists of a series of steel tubes arranged cylindrically in a rotating wheel immersed in black liquor
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cyclone
type of evaporator where liquor is sprayed into the gas as it enters
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venturi evaporator-scrubber
type of evaporator where the black \n liquor is sprayed into a turbulent flow of \n the flue gas as it passes through a \n venturi throat.
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black liquor oxidation
required only if direct contact evaporators are in operation
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oxidation
converts unstable sulfide to a stable thiosulfate
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concentrator
indirectly heated evaporators, most common type is falling film with recirculation
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evaporates water, burns organic matter, supplies heat to make steam
3 functions of a recovery boiler
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drying, oxidation, reduction
zones of the recovery boiler furnace
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function of caustic plant
convert Na2CO3 to NaOH\`
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green liquor clarifier
removes insolubles, unburned carbon, and inorganic impurities
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slaker
mixes with violent agitation of green liquor with CaO at elevated temperatures
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calcining
converts lime mud back to CaO for reuse
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calcining
lime kilns are used for
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drying, heating, maintaining
3 phases in calcining
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repulping
mechanical action to disperse dry, compacted pulp fibers into pulp slurry
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refining
to develop and modify the structure of pulp fibers to optimize the properties of the paper product
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refining
strains fibers by the transfer of energy from the beating element to the fibers
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bruising
refining at higher consistencies with a large gap between the refiner plates creates this. increases paper strength and density
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cutting
refining at low consistencies with a small distance between refiner plates creates this. increases quality of formation
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refining
fibers move parallel to the bar crossing
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beating
fibers move perpendicular to the rotating bars
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refining
does refining or beating have better control, lower operating costs, and is quicker?
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facilitate sheet making
an objective for beating/refining
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high
level of consistency that produces curled, kinky fibers with low bonding ability after refining
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medium
level of consistency that produces curled, microcompressions, internal fibrillation, and swelling
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refining
optimize strength development and control of stock drainability and sheet formation
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fiber flexibility
important because it controls the development of fiber to fiber contact during drying
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blend chest
where pulp stock and additives are mixed with an agitator