BACKGROUND OF THE INVENTION:
Field of the Invention:
[0001] The present invention relates to a method for regulating flow directions of raw material
jet flows, which is applicable to a headbox in a paper machine.
Description of the Prior Art:
[0002] A headbox in a paper machine in the prior art is illustrated in a perspective view
in Fig. 9. In this figure, reference numeral 1 denotes a headbox main body, numeral
2 denotes header pipes, numeral 3 denotes a slit-shaped jet port, numeral 4 denotes
a wire, and numeral 5 denotes a header pipe block, which is a part integrating a large
number of header pipes together. The headbox operates to make raw paper material coming
out of the header pipes 2 jet from the slit-shaped jet port 3 uniformly in the widthwise
direction of the wire 4.
[0003] In addition, at the end portions of the jet liquid, correction for the flow rate
of the raw material jetted from the jet port 3 is effected taking into consideration
the fact that there exists influence of friction of the flow passageways inside of
the headbox 1 and even after it has been jetted onto the wire 4, liquid at the side
edge portions of the wire would flow outwards. As this method for correcting the flow
rate, in the prior art, either one of the following two methods was used:
(1) Supplementary raw material is made to flow by providing bypass flow passageways
14 at the end portions of the header pipe block 5 in Fig. 9.
(2) A part of the raw material is extracted to the outside of the headbox by providing
pipings in the proximities of the end portions of the jet port 3.
[0004] However, in the method for correcting the flow rates in the prior art, though it
was possible to make the raw material to be jetted from the slit-shaped jet port 3
so that the flow rate of the raw material may be uniform along the widthwise direction
of the wire, it was difficult to align the directions of the jet flow in the same
direction over the entire width.
[0005] More particularly, with only the method of making supplementary raw material flow
at the end portions, it would result in that the flow rate of the hatched portion
in the widthwise direction flow rate distribution (Fig. 10(b)) within the headbox
was supplemented, hence there was a shortcoming that the jet raw material would be
directed inwards as shown by dash-line arrows. Also, with only the method of extracting
a part of the raw material, as shown in the curve of the widthwise direction flow
rate distribution (Fig. 11(b)), it would result in that flows directed from the central
portion to the end portions were produced within the headbox, hence there was a shortcoming
that the jet raw material would be directed outwards as shown by dash-line arrows.
SUMMARY OF THE INVENTION:
[0006] It is therefore one object of the present invention to provide an improved method
for regulating flow directions, in which the above-mentioned problems of the method
in the prior art have been resolved.
[0007] A more specific object of the present invention is to provide a method for regulating
flow directions, in which not only uneven flow rate is corrected, but also correction
of jet flow directions which was difficult in the prior art, can be also realized.
[0008] According to one feature of the present invention, there is provided a method for
regulating flow directions of raw material jet flows of a headbox in a paper machine
provided with liquid branching header pipes directed from the upstream of a flow passageway
to the downstream as arrayed along the widthwise direction of the paper machine; consisting
of the steps of providing a header pipe block having such header pipes that a flow
rate through a header pipe or pipes at at least one end in the widthwise direction
of the paper machine is set or made variable so as to be set larger than a flow rate
through a header pipe or pipes at the central portion, and/or a piping or pipings
disposed on at least one of the end surfaces in the widthwise direction of a flow
passageway within the headbox at the downstream of the header pipes and capable of
feeding liquid into the headbox and a piping or pipings disposed at at least one end
in the widthwise direction of a flow passageway within the headbox at the downstream
of the header pipes and capable of extracting the raw material within the headbox
to the outside of the headbox, increasing the flow rates at the end portions in the
widthwise direction within the headbox by means of the aforementioned header pipe
block and/or the pipings, and decreasing the flow rates at the end portions in the
widthwise direction within the headbox by means of the aforementioned extracting pipings,
whereby the jet flow directions of the raw material can be regulated through the aforementioned
flow rate increasing step and the aforementioned flow rate decreasing step, in combination.
[0009] According to the present invention, by making the flow rate through the end portions
of the headbox larger than the flow rate through the central portion, the reduction
of the flow rate at the end portions caused by friction of the flow passageway within
the headbox is supplemented, furthermore by partly extracting the raw material from
the end portions, the surplus amount of the increased flow rate at the end portions
are reduced and also the inwardly directed flow caused by the surplus of the flow
rate at the end portions can be corrected.
[0010] The above-mentioned and other objects, features and advantages of the present invention
will become more apparent by reference to the following description of preferred embodiments
of the present invention taken in conjunction with the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS:
[0011] In the accompanying drawings:
Fig. 1 is a perspective view of a headbox according to one preferred embodiment of
the present invention;
Fig. 2 is a cross-section view taken along line A-A in Fig. 1;
Fig. 3 is a cross-section view taken along line B-B in Fig. 1;
Fig. 4 is a diagrammatic view showing the effect of improvements in the flow rate
distribution along the widthwise direction and the flow directions according to the
present invention;
Fig. 5(a) is a cross-section view taken along line C-C in Fig. 2;
Fig. 5(b) is a side view of the portion shown in Fig. 5(a);
Fig. 6(a) is a cross-section view taken along line C-C in Fig. 2 according to another
preferred embodiment which is different from that shown in Fig. 5(a);
Fig. 6(b) is a similar cross-section view but under a different operating state from
that shown in Fig. 6(a);
Fig. 6(c) is a side view of the portion shown in Fig. 6(a) or 6(b);
Figs. 7 and 8, respectively, are cross-section views taken along line B-B in Fig.
1 of other preferred embodiments which are different from the preferred embodiment
shown in Fig. 3;
Fig. 9 is a perspective view showing a headbox in the prior art; and
Figs. 10 and 11 are diagrammatic views respectively showing the states of flow rate
distribution before and after correction in the prior art.
DESCRIPTION OF THE PREFERRED EMBODIMENTS:
[0012] Now, the present invention will be described in greater detail in connection to the
preferred embodiments illustrated in Figs. 1 to 8 of the accompanying drawings. At
first, a first preferred embodiment of the present invention will be explained with
reference to Fig. 1. It is to be noted that in Fig. 1, since a headbox main body 1,
header pipes 2, a jet port 3 and a wire 4 are identical to those used in the headbox
in the prior art shown in Fig. 9, detailed description thereof will be omitted, and
in the following only characteristic points of the present invention will be described.
[0013] Fig. 2 is a cross-section front view of a header pipe block 5, in which provision
is made such that a flow rate through the end portion may be larger than a flow rate
through the central portion, by selecting an inner diameter
d₂ of a header pipe 2b in the end portion larger than an inner diameter
d₁ of a header pipe 2a in the inside portion. While the header pipes 2b having the
inner diameter
d₂ are provided only in one column at each end in Fig. 2, depending upon an operating
condition, modification could be done without any inconvenience such that these header
pipes 2b may be provided in two columns at the respective ends, a number of header
pipes having a larger inner diameter may be different between the respective ends,
the inner diameter of the header pipes may be different between the upper ones and
the lower ones, or the size of the inner diameter may be varied into three or more
kinds.
[0014] Next, description will be made on the method for extracting a part of the raw material
from the end portion. Fig. 3 shows a B - B cross-section in Fig. 1, in which provision
is made such that a part of the raw material at the end portions within the headbox
can be extracted to the outside of the headbox through pipings 7 disposed symmetrically
at the opposite ends on the upstream side of a slit-shaped jet port 3. Since the inner
pressure of the headbox is higher than the atmospheric pressure, provided that the
inner diameter of the pipings 7 is chosen sufficiently large, the raw material can
be extracted from the headbox merely by opening the pipings 7 to the atmosphere.
[0015] Fig. 4 shows a flow rate distribution along the widthwise direction and flow directions
improved according to the present invention. If the flow rates at the end portions
increase as compared to that in the central portion by disposing the header pipe block
shown in Fig. 2, then as shown in Fig. 4(b) the flow rates at the end portions would
become large as compared to that before correction shown in Fig. 4(a). By the way,
since liquid would flow in such direction that its flow rate may become uniform according
to a general property of a liquid flow, the flow directions would be directed inwards
as shown in Fig. 4(b). Whereas, by extracting the raw material through the pipings
7 disposed at the end portions on the upstream side of the slit-shaped jet port 3,
the flow rates at the end portions are reduced and the flow rate distribution is equalized
as shown in Fig. 4(c), at the same time the inwardly directed flows as viewed in Fig.
4(b) would be diverted outwards from the directions indicated by dotted line arrows
x to the directions indicated by solid line arrows
y, hence the flow directions also can be equalized over the entire width including
the end portions. Although the inner diameters
d₁ and
d₂ of the header pipes in Fig. 2 cannot be varied during an operation because they
are determined upon manufacture, by regulating the extracting rate of the raw material
through the pipings 7 by means of valves 8 in Fig. 1 it becomes possible to regulate
both the above-described flow rate distribution and the flow directions.
[0016] Figs. 5 and 6, respectively, illustrate two different preferred embodiments of the
header pipe 2. Fig. 5 shows one modified embodiment, in which a sleeve 9 is fitted
to the inside of the header pipe 2 in such manner that the sleeve may not slip out
due to the pressure of the raw material. By making use of such sleeves 9 having different
inner diameters in the end portions and in the central portion, the flow rates through
the end portions can be made larger than the flow rate through the central portion.
In addition, flow rate balance between the end portions and the central portion as
shown in Fig. 4(c) can be changed in a relatively simple manner by replacing the sleeves
9.
[0017] In another modified embodiment shown in Fig. 6, a tube 10 made of elastic material
such as rubber or the like is disposed inside of the header pipe 2, and by applying
a pressure to the inside of the tube 10 through a duct 11 the tube 10 is deformed
as shown in Fig. 6(b). Thus, by varying a flow resistance through the header pipe
2 in this way, the flow rate through the header pipe in the end portion can be made
larger than the flow rate through the header pipe in the central portion. In the preferred
embodiment shown in Fig. 6, during an operation by varying the inner pressure of the
tube 10 as shown in Fig. 6(b), the flow rate balance between the end portions and
the central portion can be changed. In the case of the preferred embodiments shown
in Figs. 5 and 6, respectively, also by extracting a part of the raw material from
the end portions on the upstream side of the slit-shaped jet port 3, a correction
effect for the flow directions can be attained as shown in Fig. 4(c).
[0018] Next, explaining on the preferred embodiments shown in Figs. 7 and 8, in the embodiment
illustrated in Fig. 7, by supplementing the raw material, water or other liquid to
the end portions through pipings 12 disposed on the upstream side of the pipings 7
at the pond-sides 6 to be used for extracting the raw material, the flow rates at
the end portions can be made larger than the flow rate at the central portion. Fig.
8 shows another preferred embodiment which is different from that shown in Fig. 7,
in which owing to the fact that pipings 13 are inserted into the headbox as bent along
the pond-sides 6, the fear of disturbing flow directions within the headbox is less
than the embodiment shown in Fig. 7.
[0019] In summary, the essence of the present invention resides in the header pipe block
having header pipes which are preset in such manner that the flow rates through the
header pipes in the end portions of the headbox may be larger than the flow rate through
the header pipe in the central portion, and/or the pipings disposed at the end portions
of the flow passageway and capable of feeding the liquid in the headbox, and the pipings
capable of extracting the raw material in the headbox to the outside from the end
portions of the flow passageway.
[0020] Owing to the characteristic feature of the present invention as described in detail
above, according to the present invention, by making the flow rates in the end portions
of the headbox larger than the flow rate in the central portion, and further by extracting
a part of the raw material from the end portions, the jet flow directions of the headbox
can be aligned in the same direction. According to results of experiments, flow directions
directed outwards by 0.2° before correction became to direct inwards by 0.1° by supplementing
the raw material to increase the flow rates at the opposite end portions, and furthermore,
by extracting the raw material to decrease the flow rates at the opposite end portions,
the jet directions could be aligned in the same direction. In addition, when paper
was practically made under nearly same conditions, orientation angles of fibers of
±4° prior to correction were improved up to ±2° or less. It is to be noted that the
orientation angles of fibers as referred to above are experimental values measured
by a sonic sheet tester.
[0021] While a principle of the present invention has been described above in connection
to preferred embodiments of the invention, it is intended that all matter contained
in the above description and illustrated in the accompanying drawings shall be interpreted
to be illustrative and not in a limiting sense.