U.S. patent number 3,921,918 [Application Number 05/489,138] was granted by the patent office on 1975-11-25 for mechanical refining of fiber material including steam recycle.
This patent grant is currently assigned to SCA Development Aktiebolag. Invention is credited to Viking Per Peterson.
United States Patent |
3,921,918 |
Peterson |
November 25, 1975 |
Mechanical refining of fiber material including steam recycle
Abstract
Refiner pulp is prepared by the steps of pretreating fibrous
material with steam in a preheater followed by the step of refining
the steam-treated material in a disc refiner whereby steam is
developed, and at least a part of the developed steam is conducted
back to the preheater for maintaining desired pressure and
temperature conditions in the preheater.
Inventors: |
Peterson; Viking Per
(Sundsvall, SW) |
Assignee: |
SCA Development Aktiebolag
(Sundsvall, SW)
|
Family
ID: |
20318459 |
Appl.
No.: |
05/489,138 |
Filed: |
July 17, 1974 |
Foreign Application Priority Data
Current U.S.
Class: |
241/28; 162/19;
162/28; 241/245; 162/23; 162/47 |
Current CPC
Class: |
D21D
1/30 (20130101) |
Current International
Class: |
D21D
1/00 (20060101); D21D 1/30 (20060101); B02C
007/00 (); B27L 011/08 () |
Field of
Search: |
;162/28,47,23,19
;241/28 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Lindsay, Jr.; Robert L.
Assistant Examiner: Corbin; Arthur L.
Attorney, Agent or Firm: Pierce, Scheffler & Parker
Claims
I claim:
1. In a method of treating fiber material involving the steps of
first preheating the material with steam under elevated temperature
and superatmospheric pressure in a preheater space and then feeding
the material as a stream into a disc refiner for refining the
material during its outward passage from between the grinding discs
of the disc refiner during which passage steam at superatmospheric
pressure is developed, the improvement consisting of conducting
part of said developed pressurized steam back into the preheater
space in order to maintain the temperature and pressure in said
preheater space.
2. The method according to claim 1, wherein the superatmospheric
pressure within the preheater space is controlled by evacuating any
excess steam from said space.
3. The method according to claim 1, wherein preheated material is
fed from said preheater space to the disc refiner by causing the
material to fall freely through a feeding chute.
4. The method according to claim 1, wherein the fibre material is
heated by the steam to 105.degree.-115.degree.C, the steam pressure
being 0.2-0.6 kg/cm.sup.2.
5. The method according to claim 1, wherein the refining is carried
out in a single step.
6. The method according to claim 1, wherein the refining is carried
out in two steps.
Description
This invention relates to a method of producing mechanical refiner
pulp of various types of fibre material.
It is previously known to expose fibre material for a relatively
short time to heating with steam to above 110.degree.C and to a
pressure increased corresponding to the temperature. The pressure
is thereafter allowed to expand to a value somewhat above
atmospheric pressure before the preheated fibre material is
introduced between the refining surfaces of a disc refiner. The
steam developed during the refining can by special means entirely
or partially be led away from the central space between the
grinding discs. Steam possibly following along from the preheating
zone may, of course, also be evacuated in the same way. This
implies, contrary to conventional systems, a greater freedom of
refining with smaller gaps between the grinding discs and,
consequently, with higher energy supply, without giving rise to
serious process disturbances. The entire defibering and refining
process to the finished product can in this way be carried out in a
single step. At the production of certain pulp grades the refining
may also be carried out in several, preferably two steps, but the
portion of the total energy amount consumed in the first step
immediately after preheating would still be so great that the steam
developed during the process would cause serious disturbances, if
the steam would be forced to pass out in its entirety through the
gap between the beating discs, as is the case with conventional
systems. According to the method described above, the preheater
vessel is not in direct connection with the refiner, and the
preheating of the fibre material usually takes place within the
temperature range 110.degree.-170.degree.C, the pressure during the
preheating being higher than the pressure which prevails
immediately after the preheater vessel and in the central space
between the grinding discs, and the steam developed during the
refining being entirely or partially led away by special means from
said space. It was found suitable to carry out the refining at a
steam pressure of 0.2-0.6 kg/cm.sup.2, corresponding to a
temperature of about 105.degree.-115.degree.C, within which range
the refining energy consumption seems to be at a minimum. It was
found in a great number of mill experiments on an industrial scale
that very good pulp grades can be produced also when the preheating
of the fibre material takes place in the lower part of the
aforesaid temperature range, or at about 110.degree.-115.degree.C.
Although the resulting mechanical pulps do not reach the same high
quality levels as at preheating at higher temperatures, preferably
130.degree.C or above, their properties yet are so good that the
pulps are fully acceptable for the production of a plurality of
paper grades. This development has become possible by the
application of increasingly finer patterns of the grinding surfaces
on the segments mounted on the refiner discs, thereby rendering it
possible to carry out a greater part of the defibering work with
the segments and correspondingly reduce the energy consumption in
the preheating phase.
One main object of the present invention is to establish a
simplified system for producing mechanical pulps of high quality
while maintaining the advantages involved with the refining of
preheated fibre material, in such a manner, that a large part of
the steam developed during the refining can be evacuated rearwards
through the system from the space between the grinding discs, but
at the same time this steam is utilized for preheating the fibre
material in order to save energy. According to the invention, the
fibre material is exposed to heating with steam to
110.degree.-115.degree.C and to a pressure increased corresponding
to the temperature. The temperature and pressure are maintained
equal during the refining. The steam developed during the refining
is led away from the space between the grinding discs through the
feed screw of the refiner or through another suitable device to the
preheater vessel, which is in direct connection with the refiner.
It is hereby possible, if desired, to consume in a single step the
entire energy amount required for the process without giving rise
to process disturbances. Contrary to conventional systems, the
steam developed by the refiner is utilized in this way for heating
the fibre material. No steam generated in a different way need be
supplied to the system, so that substantial energy can be saved
compared with conventional systems. The refiner produces more steam
than can be utilized for heating the fibre material, and the excess
is removed from the preheater vessel through a pressure control
valve. The energy savings thereby possible correspond to about
150-300 kWh/t of produced mechanical pulp, or 10-20 % of the total
refining energy. The refining may, if desired, be carried out with
the housing enclosing the beating discs being pressureless and
open.
The invention is described in greater detail in the following, with
reference to the FIGURE showing an apparatus for carrying out the
process according to the invention.
The embodiment according to the FIGURE comprises a rotary vane
feeder 1 for feeding the fibre material into a preheater vessel 2.
The fibre material has a high concentration and is metered to a
correct amount by means of a metering device (not shown) arranged
before the rotary vane feeder 1. The fibre material is advanced
through the preheater vessel 2 by means of a screw 3 with such a
speed that the staying time is as long as desired, i.e. 1/2 - 3
minutes, preferably 1/2 - 1 1/2 minutes. The screw 3 is for this
purpose provided with variable operation. The heated fibre material
after its passage through the preheater vessel 2 is allowed to fall
freely through a chute 4 adjusted to local conditions, usually in
the form of a pipe, which is drawn through a separation funnel 5
mounted on the opening 6 to the feed device 7 of the refiner which
at the embodiment shown is an inclined double-screw. The feed
device may also be of another kind, such as one or two separate
horizontal feed screws. The chute 4 opens suitably spaced from the
opening 6 to the feed screws, so that the chips unobstructedly can
fall into the feed screws 8, which feed the fibre material between
the grinding discs 11, 12 of the refiner through the feed opening
13 in the grinding disc 12. Said discs 11, 12 are provided with
refining surfaces 9, 10. The feed screws 8 are operated at such a
high number of revolutions that they are only partially filled. It
is hereby possible for the greater part of the steam formed during
the refining process to escape rearwards through the system, from
the refining zone and the central space between the grinding discs
out through the feed openings 13 and through the only partially
filled feed screws 8 out into the steam separation funnel 5. The
chute 4 for the chip transport being drawn down to a point close to
the opening 6 of the feed screws 8, the greater part of the steam
coming from the refiner can be transported through a separate duct
14 to the preheater vessel 2 and be utilized for heating the fibre
material to 105.degree.-115.degree.C. Thereby, only a part of the
steam will be transported through the chute 4, and the fibre
material, therefore, falls down through the chute without being
disturbed by large steam amounts flowing in the opposite direction.
The steam discharged from the refiner is the only heat source for
heating the fibre material, and no further steam need be added. The
steam flows through the preheater vessel 2 in a direction opposite
to and thereby heating the fibre material, and the excess steam is
evacuated through the duct 15 and control valve 16 located at the
end of the preheater vessel where the fibre material is charged. By
means of the control valve 16, the pressure and temperature are
adjusted to the desired level in the entire system, as described
above.
The invention, of course, is not restricted to the embodiment
shown, but can be varied within the scope of the claims. The
refiner, for example, may be of the single-disc type and the fibre
material can then be charged in a corresponding manner through the
stationary disc.
* * * * *