U.S. patent number 3,850,792 [Application Number 05/301,167] was granted by the patent office on 1974-11-26 for steam drying device for paper making machine.
Invention is credited to Rohe V. Pennington.
United States Patent |
3,850,792 |
Pennington |
November 26, 1974 |
STEAM DRYING DEVICE FOR PAPER MAKING MACHINE
Abstract
Steam is applied to the paper web on a papermaking machine at a
flow rate which not only causes the usual dewatering enhancement by
reducing the viscosity of the water but also applies sufficient
heat to remove water by evaporation. The steam is applied to the
web through an unrestricted throat of large area. The steam is
delivered to this throat through a series of pressure-reducing
stages. Succeeding stages deliver the steam in substantially
opposite directions and the final stage delivers the steam into a
throat-defining housing in a direction directed away from the
throat.
Inventors: |
Pennington; Rohe V. (Rome,
GA) |
Family
ID: |
23162232 |
Appl.
No.: |
05/301,167 |
Filed: |
October 26, 1972 |
Current U.S.
Class: |
162/290; 162/297;
68/5D; 239/553.3 |
Current CPC
Class: |
D21F
7/008 (20130101); D21F 5/00 (20130101) |
Current International
Class: |
D21F
7/00 (20060101); D21F 5/00 (20060101); D21f
005/00 (); F26b 013/10 () |
Field of
Search: |
;162/290,297,207,208
;34/23,34,155,226 ;68/5R,5B,5D |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
486,146 |
|
Sep 1952 |
|
CA |
|
1,024,671 |
|
Apr 1963 |
|
GB |
|
Primary Examiner: Bashore; S. Leon
Assistant Examiner: Fisher; Richard V.
Attorney, Agent or Firm: Newton, Hopkins & Ormsby
Claims
What is claimed is:
1. In a papermaking machine having travelling web-supporting means,
headbox means for depositing stock onto said web-supporting means,
and suction means for removing water from the stock downstream of
said headbox means to form a progressively dewatered paper web, the
improvement which comprises:
means positioned opposite said suction means for applying a high
mass rate flow blanket of steam substantially at atmospheric
pressure to said web substantially uniformly throughout a plan-view
area extending across said web and an area sufficient to dewater
the web by evaporation without damaging the web by steam
impingement thereagainst, said means for applying a high mass rate
flow blanket of steam comprising a housing having a substantially
uniform transverse dimension substantially to encompass the width
of said web and presenting an unrestricted discharged throat of
sufficient plan view area to deliver steam at said high mass flow
rate without damaging said web, a final steam delivery chamber
having openings facing away from said throat, and delivering steam
into said housing, at least one further steam delivery chamber
within said final delivery chamber having openings facing toward
said throat, said openings in said final delivery chamber and said
further chamber being sized to reduce the pressure of said steam in
stages to provide substantially atmospheric pressure steam at a
sufficient mass flow rate to dewater said web by evaporation.
2. In a papermaking machine as defined in claim 1 wherein said
housing means includes an arched roof facing said throat, said
final delivery chamber is in the form of a cylinder extending along
the length of and spaced closely to said roof, and said further
chamber is in the form of a cylinder and substantially coextensive
in length with said cylinder.
3. In a papermaking machine as defined in claim 2 wherein said
further chamber is eccentrically disposed within said final chamber
in the direction of said throat.
4. In a paper making machine as defined in claim 1 and further
characterized in that the openings in the further steam delivery
chamber are of a constant size and of a spacing which progressively
diminishes away from said means for supplying steam.
5. In a paper making machine as defined in claim 1 further
characterized in that the openings in the further steam delivery
chamber are of equidistant spacing and which progressively increase
in a size from said means for supplying steam.
6. In a paper making machine including travelling web-supporting
means having a partially dewatered paper web thereon, and drying
means for receiving said web, the combination of:
supply means for supplying steam at a pressure sufficiently high to
deliver steam to said web, prior to introduction to said drying
means, at a flow rate high enough to evaporate water from said web;
and
steam applicator means disposed adjacent said web-supporting means
and connected to said supply means for reducing the pressure of
said steam in stages substantially to atmospheric pressure and
applying it at said high mass rate of flow to said web whereby to
remove water from the web by evaporation, said steam applicator
means comprising a housing having a substantially uniform
transverse dimension substantially to encompass the width of said
web and presenting an unrestricted discharge throat of sufficient
plan veiw area to deliver steam at said high mass flow rate without
damaging said web, a final steam delivery chamber having openings
facing away from said throat and delivering steam into said
housing, at least one further steam delivery chamber within sid
final delivery chamber having openings facing toward said throat,
said openings in said final delivery chamber and said further
chamber being sized to reduce the pressure of said steam in stages
to provide substantially atmospheric pressure steam at a sufficient
mass flow rate to dewater said web by evaporation.
Description
BACKGROUND OF THE INVENTION
This invention relates to improved dewatering devices for
dewatering wet fibrous webs such as paper webs. The dewatering of
fibrous webs in papermaking machines has been the subject of
substantial activity throughout the years and many mechanisms have
been proposed and are utilized to enhance the natural drainage of
water through the web and its support as the web moves from the
headbox to the final drying apparatus.
It has long been known, for example, that the application of heat
to the fibrous web enhances the dewatering action by reason of
reducing the viscosity of the water. An example of this technique
may be seen in U.S. Pat. No. 3,097,994 issued to Willaim A.
Dickens, et al. As has been stated, such devices previously
proposed operate to enhance dewatering by reason of elevating the
temperature of the web and thereby decreasing the viscosity of the
water. These previous techniques are successful, despite the fact
that a slight amount of water is actually added to the web by the
steam, by reason of the significant decrease in the water viscosity
effected by the elevation in temperature.
While it is of course theoretically conceivable that the flow rate
of steam could be increased in such devices to such an extent that
the amount of heat added would elevate the temperature of the water
in the web to a point at which the water actually would be removed
by evaportion, such techniques have previously not been employed
because the resultant steam velocity would be sufficiently high as
to cause damage to the web. This is so despite the fact that the
steam normally available at a papermaking site is of sufficiently
high pressure and temperature as to enable the requisite flow rate
to be applied to the web.
BRIEF SUMMARY OF THE INVENTION
It is of primary concern in connection with the present invention
to provide a steam-applying system for papermaking machines in
which a sufficiently high mass rate flow of steam can be applied to
the web as will not only cause the conventional enhancement of
dewatering by virtue of decreasing the viscosity of the water, but
which will also effect evaporation of water directly from the
web.
Generally speaking, the above objective of the present invention is
achieved by virtue of applying the steam at a high mass rate flow
through an unrestricted throat which is of sufficiently large
cross-sectional area as to avoid high velocity impingement of the
steam against the web thereby effectively avoiding damaging the web
while achieving the requisite rate of heat transfer thereto as to
effect evaporation of water from the web.
The introduction of steam to the throat is effected in a plurality
of stages, the final stage of which directs the steam into a
housing which defines the throat in a direction directed away from
the throat. Each stage effects a pressure drop in the steam and the
steam is delivered to the throat essentially at low pressures such
as atmospheric pressure whereby the impingement velocity of the
steam against the web is extremely low and is in any event well
below that velocity which could cause damage to the web.
The successive stages of steam delivery or staging each effects a
pressure drop in the steam and each is effected directionally such
that successive stages deliver steam in relatively opposite
directions. Thus, the steam changes directions a number of times
before exiting through the throat as aforesaid.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a diagrammatic elevational view illustrating the present
invention and its environment in a papermaking machine;
FIG. 2 is an enlarged section taken substantially along the plane
of section line 2-2 in FIG. 1 showning details of the present
invention;
FIG. 3 is a plan view showing the first stage delivery chamber body
in flattened condition clearly to show the steam delivery
ports;
FIG. 4 is a view similar to FIG. 3 but showing the final delivery
chamber body in flattened condition illustrating also its steam
delivery ports;
FIG. 5 is an enlarged transverse section taken substantially along
the plane of section line 5--5 in FIG. 2; and
FIG. 6 is a perspective view of the steam applicator according to
this invention.
DETAILED DESCRIPTION OF THE INVENTION
Reference is had first to FIG. 1 although it will be understood
that the papermaking machine diagrammatically illustrated therein
is not intended to be limitive with respect to the present
invention in any way and is illustrated herein in the manner shown
strictly for the purpose of describing in general the environmental
relationship with which the present invention is to be utilized. As
shown in FIG. 1, there is provided the usual headbox 10 which
receives the conventional slurry of cellulosic fiber in water and
discharges same through the nozzle 12 onto the upper flight of an
endless web-supporting means 14 which as is conventional will be a
foraminous belt, wire or felt. The support means 14 passes over a
breast roll 16 and then passes over a number of table rolls 18 and
thereafter over the suction boxes 20 to reverse direction over the
driven roll 22 and is supported along its path of movement back to
the breast roll 16 by the conventional return rolls 24 as the web W
of fibrous material passes from right to left in FIG. 1 from the
nozzle which originates its formation. It is conventional first to
allow dewatering of the web by gravity drainage through the
foraminous support means 14, which water is collected in the
receiving pan 26 from which it either will be returned to headbox
or discarded. Further dewatering of the forming web is effected by
the suction boxes 20 which, as is conventional, are connected to a
suitable source of vaccum such as motor driven pumps and,
ultimately, the web issues as indicated at 28 from the support
means 14 to pass between press rolls 30 and ultimately to a dryer
32.
The steam-drying arrangement according to the present invention is
indicated generally by the reference character 34 and will be seen
preferably to be located in the suction box region of the
papermaking machine. As can be seen in FIG. 2, the mechanism 34 is
in the form of a housing which defines a throat T of relatively
large cross-sectional area and which is unrestricted having a
transverse dimension completely or substantially completely to
encompass the width of the web W. The housing proper may be formed
by an inner wall structure which, as is shown in FIG. 5, includes
the opposite end walls 36 and 38 joined by the downwardly facing
arched roof portion 40 and having the planar opposite side walls
42. The lower edges 44 and 46 of the end wall structures are
positioned in close proximity to and above the web W whereas the
opposite side wall structures have their lower edges 48 and 50
disposed in somewhat elevated position as is shown. Suitable
support bracket portions 52 are provided on the housing structure
facilitating its mounting on the frame portions 54 of the
papermaking machine, as will be evident.
The housing structure preferably includes an outer wall structure
56 spaced from the inner wall structure and defining a space with
the latter within which is received suitable insulating material 58
to avoid unnecessary heat loss.
A final steam delivery chamber body 60 is located within a housing
means and preferably is of cylindrical form extending between the
opposite side walls 42 so as to be coextensive or substantially
coextensive in length with the arched roof 40. It will also be
noted that the body member 60 is displaced within the housing so as
to be spaced more closely to the arched roof 40 and relatively
remote from the unrestricted throat portion T. It is also preferred
that the arched roof portion 40 be coaxial or substantially coaxial
with respect to the cylindrical body member 60 as is shown in FIG.
5.
Located within the body 60 is a further body 62 also of cylindrical
form and again coextensive or substantially coextensive in length
both with the body member 60 and the arched roof 40. In the form of
the invention shown, the body member 62 is eccentrically disposed
within the body 60 so as to be displaced in the direction of the
arched roof 40.
The further body 62 is provided with a flange 64 at that portion
thereof which projects outwardly of the housing as is shown in FIG.
2 and is adapted to be connected to a source of relatively high
pressure steam. In operation of the device, the high pressure steam
is introduced into the interior of the body 60 and issues therefrom
through a series of openings 66, 68 and 70 which direct the steam
into the interior of the body 60 while effecting a first stage
pressure drop. The issuing steam impinges against and is directed
toward the lower inner wall region 72 of the body 60 where it
reverses direction and flows upwardly around the body 62 to issue
into the interior of the housing through the series of openings 74,
76 and 78 which, as shown, are directed generally away from the
direction of the throat I so that the issuing steam is directed
toward and impinges against the arched roof 40 whereafter it
changes direction to flow downwardly around the body 60 ultimately
to issue through the throat T at a low velocity, high mass rate of
flow in the blanket or cloud at relatively low pressure.
The flattened body 62 is illustrated in FIG. 3 whereas the
flattened body 60 is illustrated in FIG. 4. In FIG. 3, it will be
seen that the lines of openings 66, 68 and 70 are distributed
through a minor circumferential extent of the body 62 and that,
from the entrance end 80 of the body toward the opposite or blind
end thereof, the lines of openings 66, 68 and 70 are of
progressively diminishing spacing. The purpose of this arrangement
is to effect a uniform flow of steam along the length of the body
62 so as to introduce the steam at substantially uniform pressure
into the interior of the body 60. It will be understood that the
arrangment need not be exactly as is shown in FIG. 3 since other
arrangements would be effective to produce the same result. For
example, the lines of openings 66, 68 and 70 could be such that the
spacing between the individual openings are equidistant with the
openings being of progressively greater diameter from the end 80 to
the blind end or any other suitable arrangement could be
utilized.
Since the introduction of the steam is of substantially uniform
pressure along the length of the body 60, its openings as
illustrated in FIG. 4 can be of uniform spacing and sizes as
indicated.
In any event, it will be apparent that a number of pressure drop
stages are provided and they may be of any number required. For
example, it is desirable that the pressure drop stages be
sufficiently gradual as will not cause the propagation of any undue
sound or noise whereat, the same time, the pressure drops should be
such as cumulatively effects substantially no pressure, i.e.,
atmospheric pressure, of the steam at the throat T. Such an
arrangement is entirely satisfactory when the invention is utilized
in association with suction boxes as is shown in FIG. 1 since the
negative pressure created by the suction boxes will be more than
adequate to cause the low pressure steam to pass through the
fibrous web material
Most importantly, the overall arrangement should be such that the
mas rate of flow of the steam is sufficiently high as to create a
dewatering action by evaporation of the water from the foraminous
web material. By following the above described relationships, the
velocity of the steam issuing through the throat I will be
insufficient to cause any damage to the web.
Steam available at papermaking machinery sites normally is of
relatively high pressure, i.e., at least several atmospheres and is
otherwise suitable for producing a sufficiently high mass rate of
flow of steam as to achieve the objectives according to the present
invention. As an example of a practical embodiment according to the
present invention, steam at 50 psig and 350.degree.F is introduced
into the body 62, the openings 66, 68 and 70 are sufficient to
achieve a steam pressure of 20 psig within the interior of the body
60 at a temperature of 347.degree.F and the openings 74, 76 and 78
are sized to achieve substantially atmospheric pressure steam at
345.degree.F issuing through the throat T with the rate of steam
flow being approximately 45,000 pounds per hour.
* * * * *