
- •Isbn: 3-527-30999-3
- •Introduction
- •Isbn: 3-527-30999-3
- •1072 1 Introduction
- •Isbn: 3-527-30999-3
- •Inventor of stone groundwood. Right: the second version
- •1074 2 A Short History of Mechanical Pulping
- •In refining, the thinnings (diameter 7–10cm) can also be processed.
- •In mechanical pulping as it causes foam; the situation is especially
- •In mechanical pulping, those fibers that are responsible for strength properties
- •Isbn: 3-527-30999-3
- •In mechanical pulping, the wood should have a high moisture content, and the
- •In the paper and reduced paper quality. The higher the quality of the paper, the
- •1076 3 Raw Materials for Mechanical Pulp
- •1, Transversal resistance; 2, Longitudinal resistance; 3, Tanning limit.
- •3.2 Processing of Wood 1077
- •In the industrial situation in order to avoid problems of pollution and also
- •1078 3 Raw Materials for Mechanical Pulp
- •2, Grinder pit; 3, weir; 4, shower water pipe;
- •5, Wood magazine; 6, finger plate; 7, pulp stone
- •Isbn: 3-527-30999-3
- •4.1.2.1 Softening of the Fibers
- •1080 4 Mechanical Pulping Processes
- •235 °C, whereas according to Styan and Bramshall [4] the softening temperatures
- •Isolated lignin, the softening takes place at 80–90 °c, and additional water
- •4.1 Grinding Processes 1081
- •1082 4 Mechanical Pulping Processes
- •1, Cool wood; 2, strongly heated wood layer; 3, actual grinding
- •4.1.2.2 Defibration (Deliberation) of Single Fibers from the Fiber Compound
- •4 Mechanical Pulping Processes
- •Influence of Parameters on the Properties of Groundwood
- •In the mechanical defibration of wood by grinding, several process parameters
- •Improved by increasing both parameters – grinding pressure and pulp stone
- •In practice, the temperature of the pit pulp is used to control the grinding process,
- •In Fig. 4.8, while the grit material of the pulp stone estimates the microstructure
- •4 Mechanical Pulping Processes
- •4.1 Grinding Processes
- •Is of major importance for process control in grinding.
- •4 Mechanical Pulping Processes
- •4.1.4.2 Chain Grinders
- •Is fed continuously, as shown in Fig. 4.17.
- •Initial thickness of the
- •4 Mechanical Pulping Processes
- •Include:
- •Increases; from the vapor–pressure relationship, the boiling temperature is seen
- •4 Mechanical Pulping Processes
- •In the pgw proves, and to prevent the colder seal waters from bleeding onto the
- •4.1 Grinding Processes
- •In pressure grinding, the grinder shower water temperature and flow are
- •70 °C, a hot loop is no longer used, and the grinding process is
- •4 Mechanical Pulping Processes
- •Very briefly at a high temperature and then refined at high
- •4.2 Refiner Processes
- •4 Mechanical Pulping Processes
- •Intensity caused by plate design and rotational speed.
- •4.2 Refiner Processes
- •1. Reduction of the chips sizes to units of matches.
- •2. Reduction of those “matches” to fibers.
- •3. Fibrillation of the deliberated fibers and fiber bundles.
- •1970S as result of the improved tmp technology. Because the key subprocess in
- •4 Mechanical Pulping Processes
- •Impregnation Preheating Cooking Yield
- •30%. Because of their anatomic structure, hardwoods are able to absorb more
- •Is at least 2 mWh t–1 o.D. Pulp for strongly fibrillated tmp and ctmp pulps from
- •4 Mechanical Pulping Processes
- •4.2 Refiner Processes
- •1500 R.P.M. (50 Hz) or 1800 r.P.M. (60 Hz); designed pressure 1.4 mPa
- •1500 R.P.M. (50 Hz) or 1800 r.P.M. (60 Hz); designed pressure 1.4 mPa;
- •4.2 Refiner Processes
- •4 Mechanical Pulping Processes
- •In hardwoods makes them more favorable than softwoods for this purpose. A
- •4.2 Refiner Processes
- •Isbn: 3-527-30999-3
- •1114 5 Processing of Mechanical Pulp and Reject Handling: Screening and Cleaning
- •5.2Machines and Aggregates for Screening and Cleaning 1115
- •In refiner mechanical pulping, there is virtually no such coarse material in the
- •1116 5 Processing of Mechanical Pulp and Reject Handling: Screening and Cleaning
- •5.2Machines and Aggregates for Screening and Cleaning
- •5 Processing of Mechanical Pulp and Reject Handling: Screening and Cleaning
- •5 Processing of Mechanical Pulp and Reject Handling: Screening and Cleaning
- •5.3 Reject Treatment and Heat Recovery
- •55% Iso and 65% iso. The intensity of the bark removal, the wood species,
- •Isbn: 3-527-30999-3
- •1124 6 Bleaching of Mechanical Pulp
- •Initially, the zinc hydroxide is filtered off and reprocessed to zinc dust. Then,
- •2000 Kg of technical-grade product is common. Typically, a small amount of a chelant
- •6.1 Bleaching with Dithionite 1125
- •Vary, but are normally ca. 10 kg t–1 or 1% on fiber. As the number of available
- •1126 6 Bleaching of Mechanical Pulp
- •6.2 Bleaching with Hydrogen Peroxide
- •70 °C, 2 h, amount of NaOh adjusted.
- •6.2 Bleaching with Hydrogen Peroxide
- •Is shown in Fig. 6.5, where silicate addition leads to a higher brightness and a
- •Volume (bulk). For most paper-grade applications, fiber volume should be low in
- •Valid and stiff fibers with a high volume are an advantage; however, this requires
- •1130 6 Bleaching of Mechanical Pulp
- •6.2 Bleaching with Hydrogen Peroxide
- •Very high brightness can be achieved with two-stage peroxide bleaching, although
- •In a first step. This excess must be activated with an addition of caustic soda. The
- •Volume of liquid to be recycled depends on the dilution and dewatering conditions
- •6 Bleaching of Mechanical Pulp
- •6 Bleaching of Mechanical Pulp
- •Is an essential requirement for bleaching effectiveness. Modern twin-wire presses
- •Is discharged to the effluent treatment plant. After the main bleaching stage, the
- •6.3 Technology of Mechanical Pulp Bleaching
- •1136 6 Bleaching of Mechanical Pulp
- •Isbn: 3-527-30999-3
- •7.3 Shows the fractional composition according to the McNett principle versus
- •1138 7 Latency and Properties of Mechanical Pulp
- •7.2 Properties of Mechanical Pulp 1139
In practice, the temperature of the pit pulp is used to control the grinding process,
with typical shower water temperatures of 60–75 °C being used in atmospheric
grinders.
The pit consistency, in practical terms, is set from 1.0% to 2.5%, and interacts
with the pit temperature. Increasing the pit consistency also enables the pit temperature
to be increased, at constant shower water temperature. Depending on
either the pit consistency or possible stone immersion in the pit (Fig. 4.6), a certain
amount of pit pulp is transported with the stone and passes back into the
grinding zone. Here, regrinding takes places, so that the pulp suspension from
the grinder pit is passed to the grinding zone instead of the shower water.
A deeper immersion of the stone into the pit, or a higher weir height in the pit,
leads to a larger quantity of circulating pulp. The stone surface will be lubricated
by pulp particles and appears duller than it really is, and this in turn reduces the
freeness of the pulp.
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4.1 Grinding Processes
Fig. 4.6 Pulp stone immersion and weir height in grinding.
1, Pulp stone immersion; 2, weir height; 3, grinder pit;
4, measuring point of pit temperature and pit consistency;
VH, feeding speed = grinding pressure; VU, pulp stone rotational
speed.
A high shower water pressure [at least 350 kPa (3.5 bar)] and the position of the
shower water pipes at front of the grinding zone cleans the pulp stone surface,
and complete stone sharpening can occur. If pit-less grinding is carried out, these
influences and interactions disappear, while high shower water pressures are
applied.
The moisture of the wood is the most important parameter in grinding, as
high-quality pulp can be produced from moist wood, at a lower specific grinding
energy consumption. Neither technical nor technological developments can
replace the effect of moisture in wood. The highest possible quality values are not
found in the range of fiber saturation (moisture of wood ≥23%), but rather at a
wood saturation of 50–60% moisture content. The request by grinding mills to
receive pulpwood with at least 30% moisture content represents an objective need
for the optimal use of a wood source.
Groundwood made from logs with a higher moisture content has a higher
brightness, higher strength properties (see Fig. 4.7), and a higher long fiber content
with high-quality fines.
The pulp stone requires a certain surface structure (stone surface profile) to produce
a certain pulp quality, and distinction must be made between the macrostructure
and microstructure of that profile. The macrostructure is gained by sharpening
of the stone (see also Section II-4.1.4). A typical sharpness profile is shown
In Fig. 4.8, while the grit material of the pulp stone estimates the microstructure
(Fig. 4.9).
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4 Mechanical Pulping Processes
Fines
Short fibers
Long fibers
Shives
0
20
40
60
80
100
0 20 40 60 80 100
Rel. moisture content of wood [%]
Fractional composition
0
1
2
3
4
0 20 40 60 80 100
Rel. moisture content of wood [%]
Strength values
Breaking length [km]
In-plane tear
strength [N]
Tear strength [N]
16.5 28 37.5 44.5 50
Abs. moisture content of wood [%]
16.5 28 37.5 44.5 50
Abs. moisture content of wood [%]
Fig. 4.7 Influence of wood moisture content on groundwood
properties. Left: Effect on tensile strength and tear strength.
Right: Effect on fractional composition.
Land
Groove
Grit
Fig. 4.8 Cross-section of a pulpstone pattern.
Fig. 4.9 Ideal grit positioning (according to Atack).
The mechanical defibration of wood to groundwood is a highly energy-intensive
process. The specific grinding energy consumption can be used to characterize
the energy used, and with this the groundwood quality. In grinding, values between
0.6 MWh t–1 and 2.0 MWh t–1 o.d. pulp are typical for the production of
1086