U.S. patent number 3,903,229 [Application Number 05/240,848] was granted by the patent office on 1975-09-02 for method for producing a compressed band of wood fibers for the production of wood fiber boards.
Invention is credited to Andre Mark.
United States Patent |
3,903,229 |
Mark |
September 2, 1975 |
Method for producing a compressed band of wood fibers for the
production of wood fiber boards
Abstract
Wood is ground into fibers and the fibers are partially dried so
that the moisture percentage is about 18 to 20 percent. The fibers
are then compressed by two screw presses in sequence and extruded
through an annular nozzle to form a hollow cylindrical piece. The
compressive action of the screw presses liberates the lignines in
the wood fibers to provide a binding agent for the extruded piece.
The extruded piece is cut open along the axis thereof and spread
out flat to form a continuous band which may be subsequently dried
and/or compressed and cut into individual pieces.
Inventors: |
Mark; Andre (Lyon,
FR) |
Family
ID: |
27253634 |
Appl.
No.: |
05/240,848 |
Filed: |
April 3, 1972 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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886921 |
Dec 22, 1969 |
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Foreign Application Priority Data
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Aug 10, 1970 [FR] |
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70.1601278 |
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Current U.S.
Class: |
264/115; 264/118;
264/124 |
Current CPC
Class: |
B29C
48/07 (20190201); B27N 3/28 (20130101); B29C
48/022 (20190201); B27N 3/10 (20130101); B29C
48/03 (20190201); B29K 2105/12 (20130101); B29K
2105/06 (20130101) |
Current International
Class: |
B29C
47/00 (20060101); B27N 3/10 (20060101); B27N
3/28 (20060101); B27N 3/08 (20060101); B29C
017/14 () |
Field of
Search: |
;264/118,124,115 |
References Cited
[Referenced By]
U.S. Patent Documents
Other References
Johnson, E. S., Editor "Wood Particle Board Handbook," School of
Engineering, North Carolina State College, 1956..
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Primary Examiner: White; Robert F.
Assistant Examiner: Hall; J. R.
Attorney, Agent or Firm: Sughrue, Rothwell, Mion, Zinn &
Macpeak
Parent Case Text
This is a continuation, of application Ser. No. 886,921, filed Dec.
22, 1969, now abandoned.
Claims
What is claimed is:
1. In a method for producing a compressed flat band for use in the
manufacture of wood fiber boards, the improvement comprising:
a. feeding wood to a grinding means to form wood fibers;
b. drying the wood fibers to a first predetermined moisture content
sufficient to give the fibers the necessary flexibility for a
subsequent extrusion and cutting operation;
c. conveying the partially dried wood fibers to a first screw press
means;
d. compressing the partially dried wood fibers into a second screw
press means by said first screw press means;
e. extruding said compressed wood fibers through an annular nozzle
by means of said second screw press means to obtain a hollow
cylindrically shaped continuous piece, whereby the compressive
action of said first and second screw press means squeezes out the
lignines in the wood fibers to provide a binding agent for the
extruded piece;
f. continuously cutting the extruded hollow cylindrically shaped
piece along its longitudinal length with a circular saw; and
g. flattening the cut extrusion on a planar surface to form a
compressed flat band which can then be cut into individual
boards.
2. In a method as recited in claim 1, further comprising the step
of drying the cut extrusion to a second predetermined moisture
content after said flattening.
3. In a method as recited in claim 1, wherein step (b) includes
conveying the wood fibers to a dryer and
supplying heated gases to said dryer to dry the wood fibers to the
first predetermined moisture content.
4. In a method as recited in claim 1, wherein said first
predetermined moisture content is approximately 18 to 20
percent.
5. In a method as recited in claim 2, wherein said second
predetermined moisture content is approximately 6 percent.
Description
This invention relates to the production of wood fiber boards.
Three kinds of methods are known for the manufacture of boards from
agglomerated wood fibers impregnated with resins or similar
binders, namely the said "wet" process, "semi-dry" process and
"dry" process.
The semi-dry and dry methods begin in the same manner, that is by
drying, wood fibers obtained from a disintegrating grinder to a
relatively low moisture content. The wood fibers are then conveyed
and dispersed in an air stream in order to be collected on a
perforated band under which a negative pressure is provided.
The so-called "felting" operation provides a fiber mat which is
compressed at a high temperature in order to obtain the
polymerisation of the incorporated binder to produce a hard
board.
In the said semi-dry process, the wood fibers are dried to about 6
percent moisture content before felting. After felting, the fiber
mat is rehumidified at about 25 percent in order to permit
compression and agglomeration with reduced addition of resin,
binder or the like, and to obtain a smooth and hard skin. About 1.5
percent resin is used in the semi-dry process instead of 2.5
percent in the dry process. However, it is necessary to leave steam
passages between the heating platens of the press. For this
purpose, a wire mesh is used as a support of the mat and,
consequently, one side of the board is scored.
In the said dry process, the wood fibers are also dried to about 6
percent before felting, but the percentage of resin incorporated
into the fibers should be higher than in the case of the semi-dry
process. Then, it is possible to compress the fiber mat between two
smooth heating platens without using a wire mesh. However,
extra-fine fibers should be dispersed on the mat in order to get
one side with smooth skin. In this case, there is no scoring of one
side of the board.
The main drawbacks of these known dry and semi-dry methods are as
follows:
1. Both methods comprise a felting installation which is bulky and
expensive. Such a felting installation requires a high power
consumption due to the fans as well as cumbersome equipment due to
the important air flow and to the necessity of eliminating dust
particles before discharging this air to the ambient atmosphere. On
the other hand, a felting installation entails a permanent risk of
fire or explosion owing to the presence of the suspension of dust
and dry fibers in the conveying and dispersing hot air stream.
Homogeneous repartition of the fibers in the felter is a very
difficult and sophisticated matter.
2. It is impossible to carry out alternately both dry and semi-dry
methods on the same plant. It is necessary to use quite independent
installations, one for the dry process and one for the semi-dry
process.
One object of this invention is to avoid the above-mentioned
drawbacks and to realize at a low cost, a new method for
manufacturing compressed wood fiber bands for the production of
wood fiber boards of the same kind as hitherto obtained, by the
semi-dry process, without use of resins or similar binders.
Another object of the invention is to provide a new method for the
production of compressed wood fiber bands for making wood fiber
boards having improved mechanical properties, specially concerning
their tensile strength.
Another object of the invention is to provide a new method for
making compressed wood fiber bands for the production of wood fiber
boards, either according to the semi-dry process by operating
without resins, or according to the dry process by impregnating the
wood fibers with resins and by using a mat dryer between the
extrusion and pressing operations.
Still another object of the invention is to provide a method for
suppressing the fire hazards inherent to the felting operation in
the prior art installations.
The method according to the invention for making a wood fiber board
is characterized by drying partially a mass of wood fibers to a
residual moisture content sufficient for ensuring their
flexibility, whereafter said mass of wood fibers is extruded
through an annular nozzle in order to obtain a hollow cylindrical
shaped product, which is slit along a generatrix and is opened and
flattened on a planar surface, after which the compressed flat mat
thus obtained is cut into successive portions which are treated in
a conventional press to produce a wood fiber board.
Owing to the compression to which the slightly wet fibrous mass is
submitted upstream of the extrusion nozzle, the individual fibers
are bent and tangled with each other thereby ensuring that the
panels obtained have the required physical qualities. The lignines
contained in the wood fibers are acting as binders of entangled
fibers, said lignines being squeezed out in the extruding nozzle.
Any use of pneumatic systems with dry air is eliminated with all
the disadvantages which result therefrom in the known
processes.
According to another feature of the invention, the mass of wood
fibers is extruded free of any additional resin or binder,
whereafter the flat mat directly enters into a press supported by a
wire mesh of the kind used in the known semi-dry process.
According to another feature of the invention, a percentage of
binder, resin or the like is incorporated to the mass of wood
fibers in the extruding machine, and, after opening of the hollow
cylindrical product, the resulting flat mat is dried before
entering into a press having two perfectly smooth platens of the
kind used in the known dry process.
A plant for carrying out said new manufacturing method is comprised
of wood fibers generator: an adjustable wood fiber dryer: a screw
press provided with an adjustable binder inlet; an outlet nozzle
provided on said screwpress for extruding a hollow cylinder of
compressed wood fibers: a circular saw mounted downstream of said
outlet nozzle on a fixed support for slitting said hollow cylinder
along its upper generatrix; fixed deflectors for supporting and
opening said slit hollow cylinder in order to form a flat mat of
said precompressed wood fibers; and an adjustable dryer through
which said flat mat is delivered to a press of known type having
two heating platens.
In a preferred embodiment, the press has two screws mounted
successively to increase compaction.
FIG. 1 is a general diagrammatical view of a plant for the carrying
into practice of the process according to the invention.
FIG. 2 is a view in elevation with parts in section showing the
extruding device of this plant.
FIG. 3 is a fragmental plan view corresponding to FIG. 2.
FIG. 4 is a section illustrating a modification of the extruding
device.
FIGS. 5 to 7 are transverse sections respectively taken along lines
V--V, VI--VI and VII--VII (FIG. 4).
Referring to FIG. 1 reference numeral 1 designates two disc
grinders or disintegrators suitably fed with wood and which
disintegrate this material in the known manner. The grinders 1 can
be of the type operating under atmospheric pressure. The fibers
from these grinders fall into a conduit 2 to which hot gases are
supplied from a combustion chamber 3 into which extends a burner 4
preferably fed with gas from a suitable source. It is known that
such an arrangement generates a hot mixture of burnt gases and of
air with reduced oxygen content, which is quite suitable for the
pneumatic transport of combustible materials, such as wood fibers.
The transport of the fibers issuing from grinders 1 is ensured by a
fan 5 which blows the said fibers into a dryer 6. The fibers
issuing from dryer 6 are directed towards a cyclone separator 8
within which they are separated from the air stream in which they
had been conveyed.
The assembly 1 to 8 forms a wood fibers generator 9, which is
characterized in that the dryer 6 is adjusted for delivering at the
outlet of the separator 8, a wood fiber mass still containing a
relatively high percentage of residual moisture. This moisture
percentage is for example about 18 to 20 percent, that is enough
for ensuring the fiber mass the flexibility necessary for
subsequent extrusion.
The seaparated fibers from the bottom of the cyclone 8 are
introduced through a duct 10 into the body of a first screw press
14 having a driven feed screw 11. Said first screw press 14 opens
into the body or conical casing of a second screw press 29 having a
driven feed screw 30. This second screw press 29 is connected with
the inlet of an extruding device designated by the general
reference 15. This device, which will be described in detail below,
yields in a continuous manner a hollow cylinder 16 which is slit
along its upper generatrix by means of a circular saw 17 and which
is thereafter opened, unrolled and flattened on an appropriate
table (not shown) in the form of a band 18.
The use of two screw presses 14 and 29 mounted successively permits
an increase in the fiber compaction. As a matter of fact, since the
fibers in the inlet duct 10 have a bulk density of about 25 to 30
Kg./m.sup.3, it has been observed that said density is about 150
Kg./m.sup.3 at the outlet 12 of the first screw press, and about
750 Kg./m.sup.3 in band 18. Therefore, there is obtained a
compression of the fibers, which results in the following
consequences:
reduction of the power necessary for a conventional platen press
(not shown) located after dryer 27;
the lignines contained within the wood fibers are squeezed out and
they form a natural binder in band 18.
It has been experienced that the use of circular saw 17 is
necessary because of the consistency of the pre-compressed mass of
wood fibers in hollow cylinder 16. More particularly, it would be
quite impossible to replace circular saw 17 by a fixed cutting
blade.
On the other hand, the body 31 of the extruding nozzle is provided
with a pair of conduits 46 and 47 each having an adjustable valve
48 and 49. Through conduits 46 and/or 47, it is possible to
discharge into the body 31 an adjustable flow of water, steam,
resin, or any other substance eventually used as a binder for the
mass of fibers.
The band 18 passes through a dryer 27 equipped with heat-radiating
panels 28 heated by gas burners, not illustrated. The gas used is
preferably supplied by a gas generator operating with wood waste
from the present apparatus, in such manner as to produce an
inexpensive heat energy.
The burners of the heating panels 28 can be as desired either
operated or switched off as will be further explained.
At the outlet of the dryer 27, the band 18 is cut into portions
which are transferred to a press of known type (not shown) for
finally obtaining rigid wood fiber boards.
FIG. 2 shows a possible embodiment of the extruding device 15.
Reference 14 again designates the vertical feeding press of the
device. This press opens into the conical casing 29 of the
horizontal screw 30 of the said device, this screw being preferably
provided with two threads in order to improve the distribution and
the compression of the material. Screw 30 forces the material into
a divergent body 31 the circular outlet of which is almost closed
by a core 32 which only leaves an intermediate annular space
adapted to form an annular circular nozzle. In the embodiment
illustrated in FIG. 2, the end of the shaft 33 of screw 30 which is
situated within body 31 is supported by a profiled bearing 34
secured to the body by arms 35 which are also profiled. Core 32 is
itself supported within body 31 by a rod 36 secured to a transverse
supporting beam 37. This beam carries an arm 38 on the upper end of
which the circular saw 17 is mounted. The saw rotates in the
vertical plane which contains the axis of body 31, in such a manner
as to intersect the annular space which separates body 31 from core
32.
In the modification of FIG. 4 the shaft 33 of the screw passes
through core 32 and is supported by a bearing 40 secured to the
supporting beam 37. Core 32 is then connected with beam 37 by means
of appropriate arms, such as 41, disposed each side of shaft 33.
Except for this arrangement the modification of FIG. 4 is identical
with the embodiment of FIG. 2 and the operation remains the
same.
As a further modification it is possible to rigidly mount core 32
on shaft 33. In this case the core rotates with the shaft while
thus smoothing the inner side of the extruded cylinder, i.e., the
side which is to become the upper side of band 18. This of course,
implies a considerable reaction on a shaft 33 which should
therefore be equipped with sufficiently strong thrust bearings.
The body 31 of the extruding device has an extension 42 made of a
sheet-iron member adapted to support the slit cylindrical extruded
product and which is shaped in such manner as to progressively open
the said product until it is brought to the flat form of band 18.
FIG. 5 clearly shows the outlet of the extruding nozzle defined by
body 31 and core 32. This nozzle ensures the continuous production
of the hollow cylindrical product 16 the upper generatrix of which
is continuously slit by saw 17. In FIG. 5 the sheet-iron extension
has already partially opened or flattened cylinder 16. In order to
improve this flattening and to maintain the band 18 applied on
extension 42, two inner deflectors 44 are suitably secured to the
supporting beam 37. In FIG. 7 the sheet-iron extension is almost
flat. It is easily understood that somewhat ahead of plane VII--VII
this member is entirely horizontal. The extruded product then
becomes the band 18 of FIG. 1. This band 18 is conveyed by a roller
conveyor 45 towards the dryer 19.
It is possible, when necessary, to inject a binder such as resin,
water or steam into the fibrous mass which flows through the
extruding device. In FIG. 4 there is shown for example, a pair of
conduits 46 and 47 through which said binder may be introduced into
body 31 in order to humidify and/or to bind the fibers when
required.
The invention thus permits the production of fiber boards by a
process which does not comprise the dispersion of the fibers in a
liquid medium, that is to say, by a process of the class of the dry
and semi-dry types, but which, in contradistinction to the known
processes of the kind in question, does not require the previous
formation of a fiber mat distributed by an air stream. Furthermore,
and as above-mentioned, it is possible to use this plant in two
different ways.
According to a first possibility, the valves 48, 49, on conduits
46, 47 are closed whilst the dryer 27, is switched off. Therefore,
the band 18 is free of any binder, resin or the like and contains a
percentage of moisture about 18 to 20 percent. Said moisture
percentage is not modified when band 18 passes through the
not-operated dryer 27, whereafter said band 18 can be processed as
in the known semi-dry process, that is compressed between heating
platens (not shown), when supported by a wire mesh.
According to a second possibility, the valves 48, 49 are opened for
delivering a resin, binder or the like into the mass of wood
fibers. The dryer 27 is operated for reducing the moisture content
of band 18 from about 18 - 20 percent to about 6 percent.
Therefore, after leaving the dryer 27, the band 18 can be processed
as in the known dry process, that is, compressed between heating
platens which are both perfectly smooth.
* * * * *