TECHNICAL FIELD
[0001] The present invention relates to a drying device for drying and at the same time
removing cleaning solvent from clothes and other fabric which have been cleaned using
petroleum-based dry-cleaning solvent.
BACKGROUND ART
[0002] Conventional dryers for drying clothes and other fabric which have been cleaned using
petroleum-based dry-cleaning solvent call for, as described in, for example, Japanese
Utility Model Laid Open No. 73298/1984, recycling air by conveying air heated in a
heating chamber into a drying chamber, cooling the air exhausted from the drying chamber
in a cooling chamber, liquifying solvent vapor and moisture contained in the exhaust
air, then heating the air again, from which solvent vapor has been removed, in the
heating chamber and conveying it into the drying chamber in order to dry said items
while recovering dry-cleaning solvent.
[0003] Widely known among such dryers is a mechanism for detecting the solvent concentration
inside the circulating route in order to intake the outside atmosphere into the drying
chamber and exhausting the air which has passed through the drying chamber to the
outside of the device when detecting the concentration to be high enough to present
the danger of explosion of the solvent vapor - a high concentration may be caused
by a stoppage or decrease in ventilation - so that said explosion could be prevented.
[0004] When solvent vapor becomes highly concentrated, dryers having a conventional structure
as above are able to dilute the concentration of the solvent vapor in the drying chamber
by intaking the outside air, thereby eliminating the danger of an explosion. On the
other hand, instead of recovering solvent vapor, they discharge it toghether with
exhaust air into the outside atmoshpere, which presents the problem of releasing the
disagreeable smell of the solvent vapor.
[0005] In case of drying laundered clothes, too, conventional dryers pass air through a
cooling chamber equipped with a condenser in the same manner as when drying dry-cleaned
items. As a result, when drying laundered objects, the drying efficency is poor due
to high ventilation resistance.
[0006] For details of a drying device breadly according to the classifying portion of claim
1 herein, the reader is directed to the disclosure in US-A-4 281 465.
[0007] An object of the present invention is the provision of a device and a method for
drying clothes and other similar fabric which solves the above problems of conventional
cloth dryers by means of cooling air passed through the drying chamber before exhausting
it into the outside atmosphere, in order to recover as much solvent vapor from the
exhaust air as possible and also reduce, by means of cooling, the smell of however
little solvent vapor which might remain in the exhausted air.
[0008] Another object of the present invention is the provision of a device for drying clothes
and other similar fabric which recovers cleaning solvent from dry-cleaned items while
drying them in the solvent recovery circulating process and, in case of drying laundered
clothes and other fabric which do not use petroleum-based dry-cleaning solvent, makes
exhaust air pass through a ventilation route with low ventilation resistance, thereby
achieving high drying efficiency.
[0009] According to the present invention there is provided a drying device for drying clothes
and other such items, including a solvent recovery circuit and comprising a drying
chamber having a drying drum, an air discharge channel provided with a blower and
connected to an exhaust port of said drying chamber, an air intake channel connected
to an air intake port of said drying chamber, which air intake channel includes a
heater, and a cooling chamber located between and connected by means of a first exhaust
duct to the air intake channel and to the air discharge channel, which cooling chamber
is a part of a solvent recovery circuit which includes said first exhaust duct and
wherein:
the air intake channel of the solvent recovery circuit has an open air inlet port
for introducing outside air into the air intake channel, said open air inlet port
being capable of easily opening and closing;
a switching damper at the outlet end of said cooling chamber and an atmospheric air
vent for the said first exhaust duct which damper is constructed and arranged to selectively
connect the outlet of the cooling chamber to that atmospheric air vent or to said
solvent recovery circuit,
characterized by a second exhaust duct being arranged in parallel with said first
exhaust duct including the cooling chamber, to permit selective bypassing of the cooling
chamber by air discharged from the drum; and
a further switching damper between the air discharge channel, the inlet end of
said first exhaust duct which includes the cooling chamber and between an inlet of
said second exhaust duct which further damper is constructed and arranged to permit
air discharged from the drying chamber to either pass through said first exhaust duct
including the cooling chamber or to pass through said second exhaust duct.
[0010] When drying clothes or other objects to be dried in the drying chamber, air heated
in the heating chamber is conveyed into the drying chamber to vaporize solvent and
moisture contained in the objects in the drying drum; air containing the vaporized
solvent and moisture is conveyed into the cooling chamber to be cooled therein so
that the moisture and the solvent is liquified and thus separated from the air; and
the cooled air is heated again in the heating chamber and then conveyed into the drying
chamber. Thus, air circulates in order from the heating chamber to drying chamber
and the cooling chamber, recovering solvent in the process. When the concentration
level of solvent vapor becomes too high or when introducing the outside atmosphere
in the circulation process of solvent recovery or discharging air in the drying chamber
into the outside air at the end of the drying process, air is cooled before being
exhausted. The solvent vapor in the air is liquified and separated from the air by
cooling and is thus recovered. Therefore, recovery efficiency is improved, and even
if some solvent still remains in the air discharged into the open air, its odor is
relatively low because it has been cooled.
[0011] The cooling chamber of a clothes dryer according to the present invention can be
provided with a condenser therein as well as a viewport formed at a side thereof,
through which the inside of the cooling chamber can be seen from the outside.
[0012] As the inside of the cooling chamber can be easily observed from the outside through
the viewport, equipment of the cooling chamber, such as the condenser can be easily
maintained and checked.
[0013] A clothes dryer according to the present invention can also be provided with a concentration
sensor which detects concentration of solvent vapor in the solvent recovery channel
and, when the concentration level is detected to be in a preset range, opens the said
open air inlet port and switches the switching damper at the same time so that the
outlet end of the cooling chamber becomes connected to the open air end of the exhaust
vent.
[0014] With the configuration as above, when the concentration sensor detects during the
solvent recovery circulating process that concentration of solvent vapor is in a specified
range, the open air inlet port is opened while the outlet end of the cooling chamber
becomes connected to the open air end of the exhaust vent by means of switching the
damper at the outlet end of the cooling chamber in order to lower the temperature
in the drying chamber and reduce the concentration of solvent vapor, thereby preventing
an explosion.
[0015] A clothes dryer according to the present invention can further be provided with a
temperature sensor which detects temperature in the solvent recovery channel and,
when detecting temperature to exceed a specified degree, opens the open air inlet
port and switches the switching damper in order to connect the outlet end of the cooling
chamber to the open air end of the exhaust vent.
[0016] With the configuration as above, when the temperature sensor detects during the circular
process of solvent recovery that the temperature has been increased to exceed a specified
degree, the open air inlet port is opened while the outlet end of the cooling chamber
becomes connected to the open air end of the exhaust vent by means of switching the
damper at the outlet end of the cooling chamber in order to lower the temperature
in the drying chamber and as well as the temperature of the solvent vapor, thereby
preventing an explosion.
[0017] A clothes dryer according to the present invention is provided with an exhaust vent
which is formed parallel to the cooling chamber of the solvent recovery circuit and
open to the outside atmosphere, an open air inlet port in the air intake channel of
the solvent recovery circuit, said open air inlet port capable of opening and closing
for introducing the outside air, and a switching damper selectively connecting the
cooling chamber or the exhaust vent to the outlet end of the air discharge channel.
[0018] With the configuration as above, when drying clothes and other objects cleaned without
using dry-cleaning solvent but other means such as laundry, the damper is switched
to connect the exhaust vent to the outlet end of the air discharge channel while the
open air inlet port is opened to introduce the outside atmosphere into the air intake
channel; air heated by the heater is introduced into the drying chamber where moisture
contained in the objects is vaporized; and the air containing the vapor is exhausted
through the air discharge channel to the outside atmosphere, thus bypassing the cooling
chamber. As the air does not go through the cooling chamber, heated air efficiently
moves through the drying chamber because of low ventilation resistance, thereby achieving
effective drying performance.
[0019] A method for dryingclothes and other objects with a device according to the present
invention uses a solvent recovery circulating process which consists of supplying
air heated in the heating chamber into the drying chamber in which the drying drum
is installed, vaporizing solvent from the objects, introducing solvent vapor and air
from the exhaust port of the drying chamber into the cooling chamber through the air
discharge channel, recovering solvent from the solvent recovery channel by means of
liquifying the solvent vapor, and reheating the air in the heating chamber and directing
it into the drying chamber; and the open air introduction process which consists of
opening an open/shut open air inlet port to supply the outside air into said drying
chamber, introducing solvent vapor and the air in the drying chamber into the cooling
chamber through the air discharge channel, recovering solvent from the solvent recovery
channel by means of liquidifying solvent vapor, and discharging the air through an
exhaust vent which is connected to the outlet end of said cooling chamber, said method
selectively and alternatively performing said solvent recovery circulating process
and said open air introduction process by turns.
[0020] The device according to the present invention can also supply the outside air from
an open air inlet port of the air intake channel into the drying chamber for the purpose
of lowering the temperature in the drying chamber as well as reducing the concentration
of solvent vapor, thereby preventing an explosion.
[0021] The method for drying clothes and other objects can require switching and repeating,
at predetermined regular intervals, the solvent recovery circulating process and the
open air introduction process.
[0022] The method for drying clothes and other objects may further provide for detecting
the concentration of solvent vapor in the drying chamber in the solvent recovery circuit
and switching the solvent recovery circulating process to the open air introduction
process when detecting the concentration to be in a specified range.
[0023] The method for drying clothes and other objects may further provide calls for detecting
the temperature in the drying chamber in the solvent recovery circuit and switching
the solvent recovery circulating process to the open air introduction process when
detecting the temperature to be more than a specified degree.
BRIEF DESCRIPTION OF THE DRAWINGS
[0024] Figure 1 is a sectional view of a preferred embodiment of a clothes dryer according
to the present invention.
BEST MODE FOR CARRYING OUT THE INVENTION
[0025] For the sake of better understanding the present invention, explanation is given
hereunder, referring to the attached drawing.
[0026] Numeral 1 denotes a drying chamber, in which generally cylindrical-shaped drying
drum 2 made of punching metal or other similar materials and having numerous ventilation
holes therearound is installed. Objects to be dried, such as clothes, can be put in
and taken out of drying drum 2 through a door (not shown) on the front panel of said
drying chamber 1. Stirring fan 3 for stirring objects to be dried is installed in
drying drum 2.
[0027] Exhaust port 4 is open at the bottom of drying chamber 1, and air discharge channel
6 provided with blower 5 is connected to said exhaust port 4. Air intake port 7 is
open at the top of drying chamber 1, and heating chamber 11 provided with heater 10
which has steam pipe 9 is formed in air intake channel 8 connected to said air intake
port 7.
[0028] Cooling chamber 14, provided with condenser 13 which has cooling water pipe 12, is
connected to air discharge channel 6, the outlet end of cooling chamber 14 leading
to said air intake channel 8. Solvent recovery channel 15, to which solvent/ moisture
separator 16 is attached, is connected to the bottom of cooling chamber 14, solvent/moisture
separator 16 having solvent discharge port 17 and water discharge port 18, which are
vertically arranged in relation to each other in order to separate solvent and water
by means of the difference in their specific gravities.
[0029] Exhaust vent 19 installed parallel to cooling chamber 14 is connected to the outlet
end of air discharge channel 6, the outlet end of exhaust vent 19 opening to the outside
air.
[0030] Air discharge channel 6 is provided with Linton filter 20 which is installed at the
intake side of blower 5.
[0031] Open/shut open air intake port 21 for taking in the outside air is bored in air intake
channel 8, open air intake port 21 being provided with the first damper 22 which can
be opened and closed by such means as an air cylinder, a hydraulic cylinder, an electromagnetic
device, etc.
[0032] A second damper 23 for the selective connection of air discharge channel 6 to cooling
chamber 14 or exhaust vent 19 is installed at the outlet end of exhaust channel 6.
A third damper 24 for switching connection of cooling chamber 14 to said air intake
channel 8 or exhaust vent 19 is installed at the outlet end of cooling chamber 14,
both dampers 23 and 24 capable of opening and closing by such means as an air cylinder,
a hydraulic cylinder, an electromagnetic device, etc.
[0033] With the configuration as above, solvent recovery circuit 25 is formed with said
drying chamber 1, air discharge channel 6 connected to exhaust port 4 of drying chamber
1, and cooling chamber 14 connected to the outelt end of exhaust channel 6, the outlet
end of cooling chamber connected to air intake channel 8.
[0034] Steam pipe 9 of said heater 10 is provided with adjusting valve 26, which can be
adjusted, allowing heater 10 to heat the air to an appropriate temperature for objects
to be dried.
[0035] Drying chamber 1 is also provided with raw steam blowing nozzle 27.
[0036] Cooling chamber 14, which has condenser 13, is also provided with open/shut viewport
28, through which the inside of the cooling chamber can be seen from the outside.
[0037] With the configuration as above, clothes and other objects to be dried which have
been cleaned with petroleum-based dry-cleaning solvent are put in drying drum 2 of
drying chamber 1. Solvent recovery circuit 25 is formed by closing open air inlet
port 21 of air intake channel 8 with the first damper 22, connecting the outlet end
of air discharge channel 6 to cooling chamber 14 by means of the second damper 23,
and connecting the outlet end of cooling chamber 14 to air intake channel 8 by means
of the third damper 24.
[0038] Then, by means of circulating steam through steam pipe 9 of heater 10 and driving
blower 5, air heated by heater 10 of air intake channel 8 is introduced into drying
chamber 1, petroleum-based dry-cleaning solvent and moisture contained in the drying
objects in drying drum 2, which is being rotated, is vaporized and directed through
air discharge channel 6 into cooling chamber 14 to be liquified therein by cooling.
[0039] The liquefied solvent and moisture is discharged into solvent recovery channel 15,
and solvent which is introduced from solvent recovery channel 15 into solvent/moisture
separator 16 is separated due to the differences in specific gravities and recovered
from solvent discharge port 17, and moisture is discharged from water discharge port
18 located below solvent discharge port 17. The air, divested of solvent and moisture,
is introduced into air intake channel 8 and reheated by heater 10. As this process
is sequentially repeated, the objects are dried, and the solvent is recovered.
[0040] During this solvent recovery circulating process, raw steam is injected from raw
steam blowing nozzle 27 into drying chamber 1 at appropriate times in order to increase
the humidity in drying chamber 1 and give some moisture to the objects in drying drum
2, thereby preventing generation of static electricity and, consequently, explosion
of solvent vapor that might otherwise be caused by electrostatic discharge.
[0041] When the above solvent recovery circulating process has continued for a period of,
for example, 15 minutes, open air inlet port 21 for continually introducing the outside
air into air intake channel 8 is opened by the first damper 22 using a timer control,
while the third damper 24 is switched to connect the outlet end of cooling chamber
14 to the open air through exhaust vent 19, in order to direct the outside air from
open air inlet port 21 of air intake channel 8 into drying chamber 1, thereby lowering
the temperature in drying chamber 1, reducing the concentration of the solvent vapor
and, consequently, preventing an explosion. At that time, the outlet end of air discharge
channel 6 remains to be connected to cooling chamber 14 by means of the second damper
23.
[0042] Solvent vapor and air discharged from drying chamber 1 is directed through air discharge
channel 6 into cooling chamber 14, where vaporized solvent is liquified and recovered
through the solvent recovery channel, and the cooled air is exhausted through exhaust
vent 19. Thus, the open air introduction process and the exhausting process described
above are conducted for a period of, for example, 5 seconds. Then, the system is switched
without a break to the previously described solvent recovery circulating process by
closing, with the first damper 22, open air inlet port 21 for introducing the outside
air into air intake channel 8, and connecting the outlet end of cooling chamber 14
to air intake channel 8 by means of switching the third damper 24 while maintaining
the connection of the outlet end of air discharge channel 6 into cooling chamber 14
by means of the second damper 23, and the solvent recovery circulating process is
conducted for the period of, for example, 30 seconds. These two processes, i. e. the
open air introduction process and the solvent recovery circulating process, are alternatively
conducted for the period of, for example, 5 - 10 minutes. As the air exhausted during
the open air introduction process is chilled, the solvent recovery ratio increases,
and even if some amount of solvent vapor remains in the exhaust air, there will not
be much smell.
[0043] After the cycle operation of the open air introduction process and the solvent recovery
circulating process, the circular cooling process is initiated, without halting the
system, by means of the timer control; open air inlet port 21 for introducing the
outside air into air intake channel 8 is closed by the first damper 22, the outlet
end of air discharge channel 6 is connected to cooling chamber 14 by means of the
second damper 23, the outlet end of cooling chamber 14 is connected to air intake
channel 8 by means of switching the third damper 24, heater 10 of air intake channel
8 is stopped, and the air cooled in cooling chamber 14 is circulated to drying chamber
1, thereby cooling drying chamber as well 1 as the objects to be dried in drying drum
2. After conducting this circular cooling operation for a period of, for example,
5 - 10 minutes, and then without break, the timer control opens open air inlet port
21 to introduce the outside air into air intake channel 8 with the first damper 22
and switches the third damper 23 to connect the outlet end of cooling chamber 14 to
the outside air through exhaust vent 19, while keeping the outlet end of air discharge
channel 6 to be connected to cooling chamber 14 by means of the second damper 23.
In this state, heater 10 is stopped, the outside air is supplied from open air inlet
port 21 into air intake channel 8 to cool drying chamber 1 with its low temperature
and is cooled in cooling chamber 14 and then exhausted to the outside form the open
air end of exhaust vent 19. Thus, drying chamber 1 is deodorized, and the odor of
the exhaust air is also reduced by cooling. After this deodorizing process is conducted
for the period of, for example, 1 minute, the entire drying process is completed.
[0044] In case of drying objects laundered without using petroleum-based dry-cleaning solvent,
open air inlet port 21 for introducing the outside air into air intake channel 8 is
opened by the first damper 22, the outlet end of air discharge channel 6 is connected
to exhaust vent 19 by the second damper 23, and the inlet end of air intake channel
8 is closed by the third damper 24. Then, when steam is circulated through steam pipe
9 of heater 10 while blower 5 is driven, the air heated by heater 10 of air intake
channel 8 is introduced into drying chamber 1, where moisture contained in the objects
in drying drum 2, which is being rotated, is vaporized, and the vaporized moisture
is then exhausted together with the air through air discharge channel 6 and exhaust
vent 19 into the outside air. As the air thus exhausted to the outside does not pass
through cooling chamber 14, it moves smoothly without receiving much ventilation resistance,
and the drying efficiency is therefore improved.
[0045] Air discharge channel 6 of drying chamber 1 is provided with temperature sensor 30
so that when temperature sensor 30 detects the temperature of the air discharged from
drying chamber 1 to exceed a specified degree, signals from temperature sensor 30
cause the first damper 22 of open air inlet port 21 to open and switch the third damper
24 to connect the outlet end of cooling chamber 14 to the open-air end of exhaust
vent 19.
[0046] With the configuration as above, when temperature sensor 30 detects the temperature
to exceed a specified degree during the solvent recovery circulating process, open
air inlet port 21 is opened, while the third damper 24 at the outlet end of cooling
chamber 14 is switched to connect the outlet end of cooling chamber 14 to the open
air end of exhaust vent 19, thereby lowering the temperature of solvent vapor, as
well as the temperature in drying chamber 1, and consequently preventing an explosion.
After conducting the open air introduction process for a specified time period, open
air inlet port 21 is closed while the third damper 24 at the outlet end of cooling
chamber 14 is switched to connect the outlet end of cooling chamber 14 to air intake
channel 8. After conducting this solvent recovery circulating process for a specified
time period, the system switches to perform the open air introduction process again,
and after alternatively repeating the open air introduction process and the solvent
recovery circulating process, the entire drying process is completed with the aforementioned
cooling process which is followed by the deodorizing process.
[0047] Further, it is possible to install a concentration sensor for detecting the concentration
of solvent vapor instead of said temperature sensor 30 so that when the concentration
sensor detects the concentration of solvent vapor to be in a specified range where
there is the strong possibility of explosion of solvent vapor, signals from the concentration
sensor cause said open air inlet port 21 to open and switch the third damper 24 at
the outlet end of cooling chamber 14 to connect the outlet end of cooling chamber
14 to the open air end of exhaust vent 19.
[0048] With the configuration as above, when concentration sensor 30 detects the concentration
of solvent vapor to be in a specified range, e. g. 1% - 6%, during the solvent recovery
circulating process, open air inlet port 21 is opened, while the third damper 24 at
the outlet end of cooling chamber 14 is switched to connect the outlet end of cooling
chamber 14 to the open air end of discharged air duct 19, thereby reducing the concentration
of the solvent vapor, as well as lowering the temperature of the temperature in drying
chamber 1, and consequently preventing an explosion. After conducting the open air
introduction process for a specified time period, open air inlet port 21 is closed
while the third damper 24 at the outlet end of cooling chamber 14 is switched to connect
the outlet end of cooling chamber 14 to air intake channel 8.
[0049] After conducting this solvent recovery circulating process for a specified time period,
the system switches to perform the open air introduction process again, and after
alternatively repeating the open air introduction process and the solvent recovery
circulating process, the entire drying process is completed with the aforementioned
cooling process which is followed by the deodorizing process.
[0050] Furthermore, as the inside of cooling chamber 14 can be easily observed from the
outside through viewport 28, equipment of the cooling chamber, such as the condenser,
can be easily maintained and checked.
[0051] Although the above embodiment is explained assuming that condenser 13 of cooling
chamber 14 uses cooling water pipe 12, it is possible to use circulated water or other
cooling agent chilled by a cooling device.
INDUSTRIAL APPLICABILITY
[0052] The present invention is suitable for drying clothes and other objects cleaned with
petroleum-based dry-cleaning solvent.
1. Vorrichtung zum Trocknen von Wäsche und dergleichen, einschließlich eines Lösungsmittelwiedergewinnungskreislaufs
und umfassend,
eine Trocknungskammer (1), die eine Trockentrommel (2), und einen Luftauslaßkanal
(6) besitzt, der mit einem Gebläse (5) versehen und mit einer Auslaßöffnung (4) der
Trocknungskammer (1) verbunden ist, einen Lufteinlaßkanal (8), der mit einer Lufteinlaßöffnung
(7) der Trocknungskammer (1) verbunden ist, wobei der Lufteinlaßkanal (8) eine Heizvorrichtung
(10) umfasst, und wobei eine Kühlungskammer (14) zwischen dem Lufteinlaßkanal (8)
und dem Luftauslaßkanal (6) angeordnet und mittels eines ersten Auslaßkanals mit dieser
verbunden ist, wobei die Kühlungskammer (14) Teil eines Lösungsmittelwiedergewinnungskreislaufs
(25) ist, der den ersten Auslaßkanal umfasst,
und wobei der Lufteinlaßkanal (8) des Lösungsmittelwiedergewinnungskreislaufs (25)
eine Freilufteinlaßöffnung (21) zum Einlassen von Außenluft in den Lufteinlaßkanal
(8) besitzt, und wobei sich die Freilufteinlaßöffnung (21) leicht Öffnen und Schliessen
lässt,
einen Verschiebungsdämpfer (24) am Auslaßende der Kühlungskammer (14) und eine Entlüftungsöffnung
zur Atmosphäre hin für den ersten Auslaßkanal, wobei der Dämpfer (24) derart aufgebaut
und angeordnet ist, daß er selektiv den Auslaß der Kühlungskammer (14) mit der atmosphärischen
Entlüftungsöffnung oder mit dem Lösungsmittelwiedergewinnungskreislauf (25) verbindet,
gekennzeichnet durch einen zweiten Auslaßkanal (19), der parallel zum ersten Auslaßkanal,
einschließlich der Kühlungskammer (14) angeordnet ist, um ein wahlweises Umgehen der
Kühlungskammer (14) durch Luft zu ermöglichen, die aus der Trommel (2) abgelassen
wird, und
einen weiteren Verschiebungsdämpfer (23) zwischen dem Luftauslaßkanal (6), dem Einlaßende
des ersten Auslaßkanals, der die Kühlungskammer (14) umfasst, und zwischen einem Einlaß
des zweiten Auslaßkanals (19), wobei dieser weitere Dämpfer (23) derart aufgebaut
und angeordnet ist, daß er von der Trocknungskammer abgelassene Luft entweder durch
den ersten Auslaßkanal, einschließlich der Kühlkammer (14), oder durch den zweiten
Auslaßkanal (19) strömen läßt.
2. Vorrichtung zum Trocknen nach Anspruch 1, die mit einem Konzentrationssensor versehen
ist, um die Konzentration des Lösungsmitteldampfes im Lösungsmittelwiedergewinnungskanal
zu ermitteln, und wobei, wenn die Lösungsmitteldampfkonzentration in einem besonderen
Bereich erfaßt wird, der Konzentrationssensor die offene Freilufteinlaßöffnung (21)
öffnen und den Verschiebungsdämpfer (24) verschieben kann, um das Auslaßende der Kühlungskammer
(14) zum Freiluftende des ersten Auslaßkanals zu verbinden.
3. Vorrichtung zum Trocknen nach Anspruch 1, ferner umfassend
einen Temperatursensor (30), zum Erfassen der Temperatur im Lösungsmittelwiedergewinnungskreislauf
(25), und wobei nach Erfassen einer Temperatur oberhalb einer vorgegebenen Temperatur
der Sensor bewirkt, daß die Freilufteinlaßöffnung (21) geöffnet wird und der Verschiebungsdämpfer
(24) verschoben wird, um das Auslaßende der Kühlungskammer (40) mit dem Freiluftende
des ersten Auslaßkanals zu verbinden.
4. Vorrichtung zum Trocknen nach irgendeinem vorstehenden Anspruch, bei der der Auslaß
des zweiten Auslaßkanals (19) mit dem Auslaßende des ersten Auslaßkanals, einschließlich
der Kühlungskammer (14) verbunden ist, und wobei der Auslaß der Kühlungskammer (14)
mit dem Lufteinlaßkanal (8) im Bereich des Dämpfers (24) verbunden ist.