BACKGROUND OF THE INVENTION
[0001] This invention relates to evaporative drying systems, hereinafter called dryers,
more particularly to dryers that are used to dry-solvent based or water-based inks,
paints or coatings.
[0002] Traditional dryers dry by projecting heated air and/or radiating heat energy. The
most common form of a projected air dryer delivers lightly pressurized preheated air
into a distribution plenum, which is then dispersed through a series of slots or circular
orifices to the medium being dried. These types of dryers typically rely on large
volumes of air to adequately dry, thus consuming substantial amounts of energy and
requiring extensive air handling equipment.
[0003] In some of the more recent forced hot air dryers, compressed air is preheated prior
to entering the distribution plenum(s). The preheating is typically accomplished by
the use of a separate heat plant device such as the common triple pass or inline air
heater. Using a heat plant that is separated from the air distribution system introduces
inefficiencies of operation; additional equipment and manufacturing costs; and additional
equipment. The added equipment can also make the dryer prohibitively large in size
for some applications that have limited available space.
[0004] Current dryer systems have their operating controls located remotely from the distribution
plenum(s), which increases the complexity of the controls system and the associated
costs for the manufacturing and installation of the entire system.
[0005] EP 0 647 524 A1 discloses an air distribution system according to the preamble of claim 1.
[0007] Finally,
EP 0 320 966 A1 discloses an air distribution system for a forced hot air drying unit, comprising:
(a) a housing with an air inlet to allow air to enter said housing; (b) a heat exchanger
inside the housing, the heat exchanger being designed with an internal cavity; (c)
an outlet to allow air to pass to the exterior of said housing; (d) an electric heater
mounted within said internal cavity of said heat exchanger; (e) the heat exchanger
having multiple heat fins that extend outwardly from the internal cavity, and (f)
air passages are formed between the multiple heat fins and the housing.
BRIEF SUMMARY OF THE INVENTION
[0008] The invention provides a forced hot air dryer for the printing, painting and coating
industries that fully integrates the air handling equipment, heat plant, air flow
control and air temperature control into a single compact package. The preferred embodiment
utilizes a solid cartridge heater within a specially designed air distribution system
to raise the temperature of the forced air just before it discharges. The invention
greatly simplifies the complexity, reduces space requirements, and maximizes the energy
efficiencies over current drying systems.
[0009] Further, the air distribution system according to the invention as defined in claim
1 comprises a heat exchanger having multiple heat fins that extend outwardly, so that
air passages are formed between the multiple heat fins and the housing of the air
distribution system.
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS
[0010] The invention will be explained in conjunction with illustrative embodiments shown
in the accompanying drawings, in which:
FIG. 1 is a schematic illustration of a narrow web in-line printing press with multiple
color stations.
FIG 2 is a schematic illustration detailing a single color station of the narrow web
in-line printing press of Fig. 1.
FIG 3 is an end view of the air distribution system.
FIG 4 is a side view of the air distribution system and solid cartridge heater.
FIG 5 is a cross-sectional view of Fig. 4 with the solid cartridge heater partially
removed.
FIG 6 is a side view of the manifold connected to multiple air distribution systems.
FIG 7 is a cross-sectional front view of Fig. 6.
FIG 8 is a schematic illustration of the air flow control system for the dryer.
FIG 9 is a schematic illustration of a variable transformer electrical control system
for the dryer.
FIG 10 is a schematic illustration of an electronic control system for the dryer.
FIG 11 is a side view of the assembled control box enclosure.
FIG 12 is a front view of Fig. 11.
FIG 13 is a side view of the assembled dryer.
FIG 14 is a front view of Fig. 13.
FIG 15 is a sectional view of the temperature monitoring means for the dryer.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0011] Printing, coating, and painting lines have various configurations and methods of
operation. Configurations vary in the number of printing decks, method of conveying
the product, line speeds, etc., which will all depend on the type of product, process,
and application. Products can be conveyed in several different ways such as in the
form of a continuous web, sheet, or simply moving the product through via a conveyor.
[0012] More particularly, the flexographic press, illustrated in Figure 1 is a conventional
and well-known type of narrow web printing and/or coating press, hereinafter called
narrow web press (11). The narrow web press (11) typically prints and/or applies coating
on a continuous web (1), hereinafter called web, whereupon the freshly applied inks
or coating need to be dried. The web (1) enters the narrow web press from the unwind
station (2) and then travels through a series of idler rollers (3) in a serpentine
path while passing through multiple print stations (4).
[0013] Figure 2 details an individual printing station of Figure 1. A print station (4)
consists of a transfer roll (5) and plate roll (6) that apply a printed image (37)
or coating onto the web as it passes through the print station (4). After being applied
to the web, the printed image (37) or coating moves past the transfer roll and plate
roll area, and subsequently enters a drying zone (7) where it will be partially or
completely dried before entering the next printing station.
[0014] As the printed or coated web exits the last printing station (8), depending on the
product, process, and application, a final drying stage (9) may be required. The final
drying stage (9) may be comprised of a single or multiple dryers. The final drying
stage will evaporate the residual traces of ink solvents from the ink, and/or cure
the already substantially dried inks prior to being rewound in the narrow web press
rewinder (10).
[0015] The practice of configuring the combination of the web, unwind, print stations, dryers,
and rewind is well known. The particular configuration of these fundamental elements
of a printing press can vary greatly between printing technologies and process applications.
[0016] The nature of this invention includes the novel method of simplifying and making
compact a heated forced air dryer system. This is specifically accomplished by the
integration of a dedicated solid cartridge heater into a specially designed air distribution
system.
[0017] The preferred embodiment of the invention creates a means of efficiently transferring
heat energy from the solid cartridge heater to the air as the air passes through the
air distribution system. The preferred embodiment of the invention substantially equalizes
the temperature of the heated air that is projected out of the dryer, across the dryer
width.
[0018] A solid cartridge heater is used to heat the air in the drying system. The solid
cartridge heater is a commercially available device that is typically used to heat
solid metal structures for plastic or metal manufacturing processes, and to heat liquids
in tanks or pipes. The heating element is an electrical resistance heater that is
ultimately powered by a voltage source. Various size solid cartridge heaters can be
used that may vary in diameter, length, power level and mounting depending on the
process and application. The preferred solid cartridge heater is of cylindrical geometry
of approximately ½ inch cylindrical diameter with the cylindrical length of the solid
cartridge heater approximately equal to the dryer width. The solid cartridge heater
is well described in
U.S. Patent 3,970,822.
[0019] To simply pass air over a solid cartridge heater that is housed within a simple shell
plenum such as a common cylindrical or square tube may result in non-optimal operating
conditions, including inefficient and uneven transfer of heat energy to the air. The
inefficiencies originate from the limited surface area of the solid cartridge heater
that is exposed to the passing air as well as unrestricted airflow patterns within
the simple shell. The inefficient and uneven heat transfer results in localized hot
spots within the solid cartridge heater that can severely reduce the operable life
of the solid cartridge heater and can produce greatly varying forced air temperatures
across the width of the dryer.
[0020] The preferred embodiment of this invention incorporates a specially designed air
distribution system (13) that is fundamentally comprised of two separate metallic
extrusions including the cartridge heat exchanger (14) and air distribution plenum
(15) as shown in Figure 3.
[0021] In the preferred embodiment, the cartridge heat exchanger (14) is designed with a
cylindrical cavity (16) to accept the solid cartridge heater (12) (See Figures 4 and
5). The cylindrical diameter of the cylindrical cavity (16) is carefully controlled
to minimize the clearance between the outside surface of the solid cartridge heater
(17) (See Figure 5) and the internal surface of the cylindrical cavity (38) in the
cartridge heat exchanger (14) to provide better heat transfer and power density of
the solid cartridge heater (12).
[0022] The cartridge heat exchanger (14) has multiple heat fins (18) that extend outwardly
from the cylindrical cavity (16). The outer geometrical profile of the cartridge heat
exchanger (14) compliments the internal geometry of the air distribution plenum (15)
to create air passages (19). During operation, the solid cartridge heater (12) is
energized by a voltage source. Heat that is generated by the solid cartridge heater
is transferred into the cartridge heat exchanger (14) and will migrate outwardly into
the heat fins (18). The heat energy is then transferred to the air moving along the
heat fin surfaces (24) as the air moves through the air passages (19).
[0023] Pressurized air enters the air distribution system (13) through a port that leads
into the inlet cavity (20) of the air distribution plenum. Located at the bottom of
the inlet cavity (20), a baffle plate (21) is used to redistribute the air in order
to provide a uniform and even air flow along the dryer width as the air exits the
inlet cavity (20) through the baffle plate (21). The baffle plate (21) is fabricated
with a pattern of baffle plate orifices (22) that may vary in diameter, spacing, and
arrangement across the width and length of the baffle plate (21) to facilitate the
desired even and uniform flow. The baffle plate is located and captured by the baffle
plate recesses (23) that are incorporated into the inner geometry of the air distribution
plenum (15).
[0024] Once the air passes through the baffle plate (21), the air moves along the heat fin
surfaces (24) as shown in Figure 3. As the air passes over the surface of the heat
fins (18), the air absorbs the heat energy from the heat fins (18) of the cartridge
heat exchanger (14) through thermal convection. The circuitous air passages (19) increase
the dwell time that the air is in contact with the heat fins (18) thus increasing
the convective heat transfer efficiency.
[0025] Engineering thermodynamics states that heat energy output, Q, is directly proportional
to the convective heat transfer coefficient, h, the surface area, A, and the temperature
differential, Δ
T, where Q =
h*A*Δ
T. By increasing the heat transfer surface area, the temperature differential between
the heater and air can be lowered inversely while maintaining a substantially equivalent
heat energy output to the air. The lowered temperature differential allows the solid
cartridge heater to operate at lower temperatures, thereby increasing the expected
life of the solid cartridge heater.
[0026] At the end of the circuitous air passages (19) the heated air enters one of two orifice
chambers (25) located near the bottom of the air distribution plenum (15). The air
distribution plenum walls (26) in the area of the orifice chambers (25) are fashioned
to provide a simplified means of manufacturing a series of air release orifices (27)
that connect the orifice chamber (25) with the outside of the air distribution system
(13). The air release orifices (27) can be manufactured to project the air either
directly away (28) from the air distribution system, canted towards the middle (29)
of the air distribution system or outwardly from the middle (30) of the air distribution
system. In the preferred embodiment shown in Figure 3, the canted surfaces are constructed
at 45 degrees to the central axis of the air distribution system (13).
[0027] The air release orifices (27) may vary in diameter, spacing, and arrangement across
the width and length of the air distribution system (13), depending on the process
or application. The air release orifices (27) are typically 1 millimeter in diameter
or less.
[0028] Solid cartridge heaters are commercially available with variable power densities
along the axial length of the solid cartridge heater as well described in
U.S. Patent 3,970,822. The variable power densities can be used to counteract hot or cold spots resulting
from uneven flow patterns past the solid cartridge heater. The variable power densities
can also be used to deliberately create heated and unheated regions along the length
of the solid cartridge heater. This allows the dryer system to be very versatile in
meeting certain process or application requirements where more or less drying capacity
is required in specific intervals or in specific areas along the width of the dryer.
[0029] In the preferred embodiment shown in Figure 3, two isolated elongated thin recesses
(31) are located towards the outside wall of the air distribution plenum (15) to function
as thermal insulators between the air passages (19) and the outside of the air distribution
plenum (15). By creating a barrier for heat transfer from the air passages (19) to
the outside walls of the air distribution system, the elongated thin recesses (31)
improve the overall efficiency of the invention and maintain a reduced external surface
temperature of the air distribution system (13).
[0030] In the preferred embodiment shown in Figure 4 and 5, the air distribution system
(13) is manufactured with end plates (32) and (33), and gaskets (34) and (35) to effectively
seal off the inlet cavity (20), air passages (19) and orifice chambers (25) from the
outside of the air distribution system (13). One of the end plates, the heater bulkhead
end plate (32) is manufactured with a threaded port (36) to fasten the solid cartridge
heater (12), and to effectively prevent pressurized air from escaping at the juncture
of the solid cartridge heater (12) and the heater bulkhead end plate (32). The threaded
port (36) also provides a convenient means of assembling and/or replacing the solid
cartridge heater (12).
[0031] By the means described above, the heat source for the dryer unit has been completely
integrated within the air distribution system to result in a very compact package.
In this preferred embodiment, the end profile of the air distribution system (13)
as shown in Figure 3 is approximately 2" by 2".
[0032] The preferred embodiment described herein is capable of operating the solid cartridge
heater at high temperatures while simultaneously maintaining substantially lower external
surface temperatures given that air is flowing adequately through the air distribution
system. This is an important aspect of the invention necessary to reduce risks of
operation in solvent laden atmospheres that can spontaneously ignite in the presence
of exceedingly high temperatures, and where human interaction can cause bodily injury
upon skin contact with the hot surfaces.
[0033] The process of evaporative drying of inks, coatings, and paints is not instantaneous.
In many cases the maximum narrow web press line speed is limited by the drying capacity
of the dryer system. In prior art, it is standard dryer design practice to increase
drying capacity by adding additional length to the dryer, thus increasing the residence
time of the product being dried within the dryer.
[0034] The invention increases drying capacity by: the incremental addition of air distribution
systems; redistributing a given number of air distribution systems over a greater
dryer length; or a combination of both. It is to be understood that the addition of
an air distribution system will also, but not necessarily always, include the addition
of an integrated solid cartridge heater.
[0035] Figures 6 and 7 illustrate the means by which the invention incorporates a manifold
(39) to accommodate multiple air distribution systems (13). The manifold (39) used
to couple the air distribution systems has a central cavity (40) in the major axis
of the manifold that is sized sufficiently to provide adequate air flow to all coupled
air distribution systems (13). The coupling of the air distribution system to the
manifold can be achieved through a variety of means including threading, sealant,
liquid gasket, crushed-gasket sealing, etc. The preferred arrangement of the preferred
embodiment is an o-ring face seal (41) held at the joining surfaces of the manifold
(39) and the air distribution system(s) (13). A series of fasteners (43) are used
to pre-load the o-ring (41) and to prevent the air distribution system (13) from moving
relative to the manifold (39).
[0036] The control of the invention involves control of air flow and control of electrical
power to the solid cartridge heater. The preferred embodiment of the invention provides
a means for operators of the invention to vary both the temperature of the air and
flow of the air to dry the product. This variability is necessary because products
that can be processed on the narrow web press have broad ranges of thermal yield characteristics,
and excessive temperature and airflow conditions can detrimentally affected fragile
product structures.
[0037] The preferred embodiment of the invention utilizes a simple and inexpensive control
system for the dryer system.
[0038] The volume of air moving through an air conveying medium such as tubing or piping,
hereinafter referred to as pipe, is dependent on the geometry of the pipe and the
inlet pressure of air moving into the pipe. Variations in inlet pressure, pipe diameter,
or pipe length can have a significant affect on the volume of air flowing through
the pipe. It is difficult to reliably control the air flow through a pipe system by
controlling the pipe system's inlet pressure if the characteristic of the downstream
pipe system are unknown or if the pipe geometry can change arbitrarily. This is the
inherent difficulty of utilizing a centralized or remotely located flow control system
to control flow in a widely distributed air distribution system. Such systems will
typically rely on remote sensing of pressure and/or flow and therefore adjust the
pipe system's inlet pressure accordingly. It is one advantage of the invention to
overcome the undesirable effects noted above.
[0039] It is foreseen that multiple drying systems will be integrated into a narrow web
press; therefore, it is an advantage of the invention that a repeatable control of
air flow is possible by using a common air flow setting for each respective dryer
system. According to the preferred embodiment of the invention, by maintaining consistent
pipe geometry in each dryer system, air flow through the air distribution system can
be reasonably predicted and adequately controlled by controlling the inlet pressure
into the dryer system.
[0040] As illustrated in Figure 8, the air flow control system is achieved by the use of
an air flow regulator (42) which is a relatively inexpensive, minimally complicated,
and commercially available device. Pressurized air (44) is supplied to the air flow
regulator (42) which controls the output pressure of the air flow discharging from
the air flow regulator (42). The air flow regulator pressure is substantially equivalent
to the inlet pressure of the pipe. The volume of air flowing out of the air flow regulator
(42), and thus through the dryer system, can be modified by changing the settings
of the air flow regulator (42).
[0041] The solid cartridge heater is an electrical device with an electrical resistance,
R, that generates thermal power, P, from electrical current,
I, by Ohm's Law (
P =
I2R). Note the electrical current is also related to the electrical voltage,
V, by Ohm's Law (
I=
V/
R) therefore
(P=V2/
R). The electrical resistance of the solid cartridge heater is dependent on the operating
temperature of the solid cartridge heater typically varying the electrical resistance
of the solid cartridge heater by a margin of approximately 10%. The electrical resistance
increases with the operating temperature of the solid cartridge heater. For the purpose
of the following description, the electrical resistance of the solid cartridge heater
will be treated as a constant value, R.
[0042] The amount of electrical power consumed by the solid cartridge heater is directly
related to the thermal power delivered to the heated air flow that is discharging
from the air distribution system. By controlling the electrical power and volume of
air flow, the temperature of the air flow can be controlled.
[0043] A relatively simple scheme for controlling the power to the solid cartridge heater
is to control the voltage to the solid cartridge heater. Figure 9 illustrates a voltage
controller based on a mechanically adjustable variable transformer, hereinafter referred
to as the variable transformer (45). The variable transformer (45) is a commercially
available device.
[0044] The variable transformer (45) allows simple adjustment of the output coil of the
variable transformer (45) thus effecting the voltage output ratio of the variable
transformer (45). The variable transformer (45) is typically manually adjusted to
supply a constant output voltage at the desired voltage amplitude. The output voltage
from the variable transformer (45) serves as the supply voltage for the solid cartridge
heater (12). In this fashion a constant supply voltage is applied to the solid cartridge
heater (12). Also as shown in Figure 9 multiple solid cartridge heaters (12) can be
connected in parallel across the supply voltage.
[0045] Adjusting the output voltage to one-half of the maximum output voltage will produce
one-fourth the power produced at the maximum output voltage as can be determined from
Ohm's Law
(1/
4*Pmax = ((1/
2)*Vmax)2/
R). The variable transformer is an elegant means of adjusting the output power of the
heater and the respective drying capacity of the dryer.
[0046] One advantage of using the variable transformer control system is the low cost and
low complexity.
[0047] A further advantage of using the variable transformer control system is the ability
to energize the solid cartridge heater(s) at a fraction of their rated power continuously,
even without air flow through the air distribution system. This provides a convenient
and more economical means of pre-heating the dryers by avoiding the consumption of
pressurized air.
[0048] In using the variable transformer control system as the primary electrical control
system, the variable transformer control system lacks a closed-loop temperature control.
At a constant output voltage setting a change in the air flow volume will affect the
air flow discharge temperature. Thus without an independent temperature sensor monitoring
the dryer operating temperature, the operator of this dryer will not have an accurate
measure of the effective drying temperature. Furthermore, even with a temperature
sensor feedback, a mechanically adjusted variable transformer would be very complex
to configure to automatically control to a desired dryer operating temperature.
[0049] In practical operation, depending on the product, process, and application, the air
flow settings and the variable transformer settings can be determined through trial
and error, and subsequently used as reference settings to reliably reproduce the same
dryer conditions in the future on any of the variable transformer controlled dryers
on the narrow web press.
[0050] The variable transformer control system provides an effective means for operating
the dryer, however the preferred dryer system includes a means to control to a desired
dryer operating temperature since an acceptable level of drying is more readily correlated
to a dryer temperature.
[0051] The preferred electrical control system illustrated in Figure 10 uses an electronic
controller (47) to modulate the supply voltage (49) to the solid cartridge heater(s)
(12) between an energized and de-energized state. In this scheme, the supply voltage
(49) to the solid cartridge heater(s) (12) is modulated at either the maximum supply
voltage setting or none at all. The amount of thermal power delivered by the dryer
system is related to the percentage of time the dryer is energized.
[0052] The electronic controller (47) is a commercially available device that can be obtained
in a variety of configurations and with a variety of features. In this preferred embodiment
the controller output signal (46) from the electronic controller is a low voltage,
low power signal incapable of energizing the solid cartridge heater(s) (12) directly.
However, this low voltage, low power controller output signal (46) can be used to
activate a secondary device such as a mechanical relay or solid state relay to energize
the supply voltage to the solid cartridge heater (12). In this preferred embodiment
as shown in Figure 10 a solid state relay (48) is used to energize the supply voltage
(49) to the solid cartridge heater(s) (12) when the solid state relay (48) is commanded
by the electronic controller (47) via the controller output signal (46).
[0053] The electronic controller (47) utilizes an external temperature measurement and compares
it to a pre-set temperature as established by the operator of the narrow web press.
The pre-set temperature settings depend on the product, process, and application.
If the external temperature measurement is lower than the pre-set temperature, the
electronic controller (47) commands the solid state relay (48) to energize the supply
voltage (49) to the solid cartridge heater(s) (12). If the external temperature measurement
is higher than the pre-set temperature, the electronic controller (47) commands the
solid state relay (48) to de-energize the supply voltage (49) to the solid cartridge
heater(s) (12).
[0054] A potential problem of this scheme is that the electronic controller continues to
command an energized state of the supply voltage whenever the external temperature
measurement is below the pre-set temperature. This condition can exist when the air
flow to the dryer system is shut-off either intentionally or mistakenly. Since this
control scheme will only supply the maximum supply voltage when energized, the above
condition can place the solid cartridge heater(s) at a severe risk of failure from
reaching excessive temperatures.
[0055] A solution to this problem is the integration of an electro-mechanical pressure switch
or pressure transducer to monitor the pressure and thus flow of air through the air
distribution system. The electro-mechanical pressure switches and pressure transducers
are commercially available devices. In this preferred embodiment, an electro-mechanical
pressure switch (50) monitors the air pressure of the air distribution system and
allows the controller output signal (46) to activate the solid state relay (48) as
long as the system is operating with adequate air pressure. Without adequate air pressure
the electro-mechanical pressure switch (50) will electrically ground the solid state
relay (48) and insure the supply voltage (49) is not energized to the solid cartridge
heater(s) (12).
[0056] A temperature sensor (51) is located to monitor the effective temperature of the
dryer system, and to provide the external temperature measurement signal to the electronic
controller (47). The temperature sensor (51) can monitor the temperature of: the air
distribution system's component; the air within the air distribution system; the air
discharging from the air distribution system; a component that is in contact with
the product being dried; etc. Depending on the location of the measurement point,
the control response of the system and the maximum achievable temperature can vary
greatly. To overcome this, the operational control gains of an electronic temperature
controller can be adjusted to establish acceptable system controllability.
[0057] A circuit breaker (52) is incorporated as a switch and safety device for the control
system of either the variable transformer control system or the electronic control
system as shown in Figure 9 and 10 respectively.
[0058] The above text has described in detail the three basic subsystems of the forced air
dryer including the air heating and distribution system, the air flow control system,
and the electrical power control system. According to the preferred embodiment of
the invention the three subsystems are combined into a singular compact unit for ease
of integration with the web and into the narrow web press.
[0059] An advantage of the preferred embodiment of the invention is that by housing all
of the air flow and electrical controlling components of the dryer into a control
box enclosure the components from the environment. These components include the electronic
temperature controller, air flow regulator, pressure switch, solid state relay, and
circuit breaker, all of which have already been described above.
[0060] Enclosing the air flow and electrical control components is an advantage of the invention
since dryers will typically reside in hazardous environments caused by flammable solvent
vapors evaporated from the inks. When the dryer system is operated in a hazardous
environment, the control box enclosure can be gasket sealed and lightly pressurized
to achieve a purged environment within the control box enclosure allowing the safe
operation of the electrical components. The lightly pressurized air is provided as
a natural by-product of the relieving pressure regulator under normal operating conditions.
[0061] Enclosing the air flow and electrical control components is also an advantage of
the invention in that all of the controlling components are substantially shielded
from incidental debris generated by normal operation of the printing press. The debris
includes ink spills, cleaning solvent, lubrication, etc.
[0062] It is also an advantage of this invention that the air flow lines and electrical
lines to and from the control box enclosure are connected and sealed such that the
control box enclosure is sealed and capable of being lightly pressurized. ,
[0063] It is an advantage of the invention that the operational controls are located such
that they are accessible to operators of the narrow web press.
[0064] It is an advantage of this invention that the solid heater cartridge is enclosed
within the air distribution system such as to result in acceptably low external surface
temperatures of the air distribution system. This combined with the proper accommodation
of air flow lines and electrical lines permits the dryer to reside in a hazardous
environment.
[0065] The air distribution system is advantageously designed to accommodate the maximum
web width of the printing press and to provide the desired residence time of the dryer.
This is accomplished by appropriate layout of the manifold and air distribution system(s)
within the dryer as described in detail earlier in the patent.
[0066] It is well known that drying capacity decreases as the distance between the web and
the discharge orifices of the dryer increase. It is also well known that uniform drying
will result when the web is held uniformly and at a constant distance from the dryer
across both the length and width of the dryer, given that the discharging air flow
and temperature are uniform across the same. It is an advantage of the invention that
the web is held in the dryer at a close and even distance from the discharging air
to achieve proper drying.
[0067] In consideration of retrofitting the dryer onto a narrow web press, the integration
of the web support into the dryer will minimize press modifications and dryer design
variations with respect to web handling as the web passes through the dryer. The web
support that is incorporated into the dryer must provide an even support across both
the width and the length of the dryer, such that the web is prevented from being deflected
when subjected to the discharging air from the air distribution system(s). It is also
an advantage of the invention that the web support is a simple device in that it provides
the operator easy access for web threading and dryer cleaning
[0068] It is an advantage of this invention that all components and subsystems of the dryer
can be housed into a single compact unit that can be mounted in an area where space
is limited.
[0069] It is also an advantage of the invention that the installation time of the dryer
unit is minimized. By including provisions into the dryer design, only mounting the
dryer to the press and connecting to the electrical power and compressed air sources
to the dryer will be required for installation.
[0070] The air flow regulator (42), pressure switch (50), electronic controller (47), solid
state relay (48), and circuit breaker (52) are housed in a dedicated control box enclosure
(53). It is also an advantage of this invention to include the control box enclosure
(53), manifold (39), air distribution systems (13), and all interconnecting components
inside the dryer enclosure (62).
[0071] As illustrated in Figures 11 and 12, an external compressed air supply line is connected
to the dryer through a single air supply port (54) on the control box enclosure (53).
The air supply port (54) can be achieved by a number of means including a quick air
disconnect, a push-to-connect fitting, a hose barb fitting, threaded pipe fitting,
etc. The preferred means is to use a push-to-connect fitting, which provides a convenient
and tool-less means of connecting and disconnecting the dryer from the external pressurized
air supply line.
[0072] The air supply port (54), which is rigidly joined to the air flow regulator (42),
passes the supply air through the wall of the control box enclosure (53) and into
the inlet port of the air flow regulator (42).
[0073] The air flow regulator (42) must be accessible for manual adjustment by the press
operator during normal operation of the dryer. The air flow regulator (42) is mounted
inside the control box enclosure (53) such that the control dial (55) of the air flow
regulator (42) passes through an opening in the control box enclosure (53) thus allowing
convenient manual adjustment of the air flow in the dryer.
[0074] Air flow exiting the outlet port of the air flow regulator (42) passes through a
specially designed air flow block (56) which is then connected to an air outlet port
(57) mounted to the wall of the control box enclosure (53). The air flow block (56)
is connected to the air outlet port (57) by tubing. Outside of the control box enclosure,
the air outlet port (57) is connected to the inlet port on the manifold (39) by tubing.
[0075] The air flow block (56) also provides an air pressure sensing port for the electro-mechanical
pressure switch (50). The air flow block (56) also provides holes (58) for mounting
the solid state relay (48) firmly against the air flow block (56). This firm surface
contact between the solid state relay (48) and the air flow block (56) provides a
means for heat generated by the solid state relay (48) to be transferred to air passing
through the air flow block (56). The solid state relay (48) must shed this heat in
order to operate safely and reliably, and the transfer of thermal energy to the air
is an efficient use of the available thermal energy for the purpose of drying.
[0076] The electronic controller (47) is accessible for manual adjustment by the press operator
during normal operation of the dryer. The electronic controller (47) is mounted inside
the control box enclosure (53) such that the temperature display and temperature controller
keys are presented outside the control box enclosure (53) thus allowing convenient
manual adjustment of the dryer temperature setting.
[0077] The circuit breaker (52) operates as an electrical safety device and as a switch
for energizing the control system of the dryer. The circuit breaker (52) is mounted
such that the switch can be manually switched from outside the dryer.
[0078] The electrical power supply to the dryer is provided by an electrical cable that
penetrates the wall of the control box enclosure (53) utilizing a sealed electrical
bushing (59). The sealed electrical. bushing (59) is used to have the capability to
lightly pressurize the internal volume of the control box enclosure (53).
[0079] The electrical power supply is connected to the circuit breaker (52) and then distributed
internally to the electronic controller (47) and the solid state relay (48). The control
signal from the electronic controller (47) is connected through the pressure switch
(50) and then to the solid state relay (48). The pressure switch (50) is mounted to
the pressure sensing port of the air flow block (56). When air flows through the air
flow block (56), air pressure activates the pressure switch (50) and closes the electrical
signal path between the electronic controller (47) and the solid state relay (48).
[0080] The electrical power is switched on by the solid state relay (48) and then made available
for connection to the solid cartridge heaters (12). The controlled electrical power
output to each of the solid cartridge heaters (12) is achieved by utilizing a sealed
electrical bushing (60) for each of the solid cartridge heater power cables (61).
The heater manufacturer seals the power cables (61) to the end of the solid cartridge
heaters (12) as part of the standard design.
[0081] The temperature sensor feedback signal cable also passes through the control box
enclosure wall utilizing a sealed electrical bushing (not shown). The temperature
sensor feedback signal is connected to the electronic controller (47).
[0082] As illustrated in Figure 13 and 14, the control box enclosure (53) is mounted to
the dryer enclosure (62). The manifold (39) and air distribution system(s) assembly
is mounted to the dryer enclosure (62)
[0083] As shown in Figure 15, the solution for supporting the web is accomplished with a
slide plate (63). The slide plate (63) is of a sheet metal construction, and is attached
to back side of the dryer enclosure (62) by use of a hinge allowing the slide plate
(63) to function as a door. Mechanical latches (65) are located towards the front-side
of the dryer enclosure providing a convenient means for the press operator to open
the slide plate for manual threading of the web through the dryer during machine set
up, or for maintenance access to clean the air distribution systems (13). The slide
plate (63), hinge, latches (65) and supporting structure of the enclosure are designed
to ensure that when closed, the slide plate (63) provides a firm web support that
is positioned approximately %" from the discharge orifices of the air distribution
system. The mechanisms described above also ensure that the location of the slide
plate (63) relative to the air distribution systems (13) is held evenly across the
length and width of the dryer.
[0084] Normal operation of the dryer discharges significant volumes of air into the area
where the product is being dried. As the product dries, significant volumes of solvent
vapor are evaporated into the area where the product is being dried. It is an advantage
of the invention that the mixture of discharged air and evaporated solvent vapors
are removed. This is achieved by enclosing the area where the product is being dried
by a plenum (66) and then exhausting the internal volume of the plenum (66).
[0085] The dryer enclosure (62) and control box enclosure (53) form five of the six sides
of the box type construction of said plenum. The slide plate (63) and web provide
the sixth side of the plenum (66). It is an advantage of the invention that minimal
slot openings (67) and (68) are provided for the web to enter and exit the plenum
(66) respectively. An external exhaust system provides the light suction necessary
to draw the air and solvent vapors from inside the plenum, and is connected to an
exhaust port (69) located on the dryer enclosure to remove air and solvent vapors
from inside the plenum (66).
[0086] Mounting holes (70) for attaching the dryer to the narrow web press structure are
provided in the back plate (71) of the dryer enclosure (62) of the dryer.
[0087] As briefly discussed earlier, dryer systems monitor and control a temperature of
an element of the dryer system. It is most desirable to measure the actual product
temperature of the product being dried since the product temperature is indicative
of the level of drying that has been achieved. Historically, the means of measuring
the actual product temperature has been very difficult to implement.
[0088] In lieu of measuring the temperature of the product being dried, a common practice
has been to measure the temperature of the forced air of the dryer with the general
assumption that the product achieves the substantially equivalent temperature of the
forced air. Depending on the product, process, and application this assumption may
be invalid.
[0089] It is an advantage of the invention that a means is provided that will more accurately
represent the actual temperature of the product being dried. Figure 15 illustrates
the preferred embodiment of this means.
[0090] A commercially available temperature sensor (51) is mounted onto the backside of
the metallic slide plate (63), near the end of the metallic slide plate (63) where
the web (1) exits the dryer (72). The temperature of the metallic slide plate (63)
in this area will essentially stabilize at the temperature of the web due to the close
and constant proximity with the heated web (1).
[0091] Additional heat loads in the slide plate (63) may be generated due to the friction
of the web (1) sliding over the slide plate (63). The additional heat loads from friction
are considered negligible due to the low contact force of the web (1) against the
slide plate (63). To minimize any other interference from the environment to the temperature
sensor (51), insulation (64) is added onto the backside of the slide plate (63) and
the temperature sensor (51). The thermocouple wire leads are then routed back to the
input of the dryer's temperature controller.
[0092] The foregoing dryer system includes the following features:
- 1. All components and subsystems of the dryer are combined into a single unit that
can be mounted in an area where space is limited.
- 2. Provisions have been made to minimize the installation time of the dryer unit so
that only mounting the dryer to the press and connecting the dryer to the electrical
power and compressed air sources will be required for installation.
- 3. An air distribution system that maintains cool external surface temperatures while
simultaneously integrating the heat source directly into the air distribution system
at the immediate vicinity of the discharging forced air. The external surface temperature
of the air distribution system is maintained at sufficiently low temperatures such
that the air distribution system can operate in solvent laden environments without
the risk of spontaneously igniting the flammable air and solvent vapor mixture.
- 4. A control system for both air flow and air temperature that is integrated directly
with the dryer system so as to provide a convenient means for the operator to make
adjustments to either the air flow setting or temperature setting or both at the dryer
location. The integration of the control system into the dryer eliminates the need
for the operator to make said adjustment(s) from an inconvenient remote location.
- 5. The heat source is mounted within the air distribution plenum providing the most
efficient means of utilizing the power from the heat source for the purpose of drying.
The air is heated just before it is dispersed through the air release orifices onto
the web. By combining the heat plant into the air distribution plenum, the unit is
very compact, requires fewer parts, and is less expensive to manufacture.
- 6. When the dryer system is operated in a hazardous environment, the control box enclosure
can be gasket sealed and lightly pressurized to achieve a purged environment within
the control box enclosure allowing the safe operation of the electrical components.
The lightly pressurized air is provided as a natural by-product of the relieving pressure
regulator under normal operating conditions.
- 7. A slide plate is used to provide even support to the web as the web passes through
the dryer. The slide plate has a hinge and latch configuration that allows the press
operator a convenient means to rock the slide plate back out of the way for manual
threading of the web through the dryer during machine set up, or for maintenance access
to clean the air distribution assemblies.
- 8. Solid cartridge heaters are available with various power levels in the same cylindrical
geometry. A conveniently located bulkhead plate with a threaded port is used to mount
the solid cartridge heater in the air distribution system. This provides the press
operator with a means to readily change out solid cartridge heaters with different
power levels for different processes and application.
- 9. The effective drying temperature of the dryer is measured using a temperature sensor
that is mounted to a metallic slide plate that is in contact with the web. The temperature
of the metallic slide plate essentially stabilizes at the temperature of the web,
due to the contact with the web, and will provide the operator with a more accurate
measurement of the effective drying temperature of the process. This can greatly reduce
set up time and maintain quality on repeat jobs.
- 10. Solid cartridge heaters are available with variable power densities along the
axial length of the solid cartridge heater. The variable power densities can be used
to create hot or cold spots in specific intervals or in specific areas along the width
of the dryer to counteract uneven flow patterns past the solid cartridge heater or
to meet specific process or application requirements.
1. An air distribution system (13) for a forced hot air drying unit (7, 9), comprising:
a) a housing (15) forming an air distribution plenum with an air inlet (20) to allow
air to enter said housing (15);
b) a heat exchanger (14) being placed inside said housing and being designed with
an internal cavity (16, 38), the heat exchanger having multiple heat fins (18) that
extend outwardly from the internal cavity (16, 38);
c) an air outlet (25, 27) to allow air to pass to the exterior of said housing (15);
and
d) an electrical heater (12) mounted within said internal cavity (16, 38) of said
heat exchanger (14),
characterized in that
e) the outer geometrical profile of the heat exchanger compliments the internal geometry
of the air distribution plenum so as to form circuitous air passages (19) between
the multiple heat fins (18) and inner wall of the housing (15).
2. The system (13) according to claim 1, wherein said outlet (25, 27) comprises a plurality
of orifices (27).
3. The system (13) of claim 1, in which said heater (12) comprises of a solid cartridge
type heater (12) that may vary in material composition, diameter, length and wattage.
4. The system (13) according to claim 1, wherein said housing (15) comprises:
a) an inlet cavity (20),
b) a baffle (21),
c) said air passages (19),
d) a single or multiple orifice chamber(s) (25), and
e) a series of orifices (27) allowing air to pass from said orifice chamber(s) (25)
to the exterior of said housing (15) of said air distribution system (13), and
f) an internal construction capable of accepting said heater (12) which allows heat
to be efficiently conveyed from said heater (12) through said internal construction
to the air as the air passes from said baffle (21) to said orifices (27);
g) said electrical heater (12) mounted within said internal construction of said housing
(15) of said air distribution system (15).
5. The system (13) of claim 1, in which said heater (12) is constructed with variable
power density to provide an equal temperature profile along the axial length of said
housing (15).
6. The system (13) of claim 1, further comprising:
a) a means (44) for receiving pressurized air;
b) a means (49) for generating heat receiving electrical power;
c) single or multiple air distribution system(s) (13) that receive, heat, and disperse
said pressurized air (44);
d) a means (42) of controlling the flow of said pressurized air (44) passing through
said air distribution system (13), said controlling means (42) includes an air flow
regulator (42); and
e) a means (47) of controlling the temperature of the air passing through said air
distribution system (13), said means (47) includes a modulating power electronic temperature
controller, wherein said air distribution system (13), said means (42) of controlling
the flow, and said means (47) of controlling the temperature are located in a single
enclosure (53).
7. The system (13) of claim 1, further comprising of:
a) a thermocouple (51) mounted to a thermal conducting slide plate (63) in contact
or supporting the materials being dried,
b) the thermocouple (51) mounted in a location where the material being dried has
already been exposed to the majority of the resident time of the drying unit (7, 9);
and
c) the thermocouple (51) being capable of attaining the temperature of the material
being dried.
8. The system (13) of claim 1, further comprising:
a) an enclosure (62);
b) one or more housings (15), each housing (15) forming an air distribution plenum
and having
b1) an air inlet (20) to allow air to enter said housing (15),
b2) an internal cavity (16, 38), and
b3) an air outlet (25, 27) to allow air to pass to the exterior of said housing (15);
c) an electrical heater (12) mounted within said internal cavity (16, 38) of each
said housing (15);
d) at least one control (42, 47) for influencing the amount of forced air drying;
and
e) wherein said one or more housings (15) and said control (42, 47) are contained
within said enclosure (62).
9. The system (13) according to claim 8, wherein said control (42, 47) comprises a heater
control (47) for controlling air temperature.
10. The system (13) according to claim 8, wherein said control (42, 47) comprises an air
flow control (42).
11. The system (13) of claim 1, further comprising:
a) a plurality of housings (15), each housing (15) forming an air distribution plenum
and having
a1) an air inlet (20) to allow air to enter said housing (15),
a2) an internal cavity (16, 38),
a3) an air outlet (25, 27) to allow air to pass to the exterior of said housing (15);
and
b) an electrical heater (12) mounted within said internal cavity (16, 38) of each
said housing (15); and
c) an air distribution path (19) connected to said housings (15).
1. Luftverteilungssystem (13) für eine Zwangsheißlufttrocknungseinheit (7, 9) aufweisend:
a) ein Gehäuse (15), das eine Luftverteilungskammer mit einem Lufteinlass (20) bildet,
um es Luft zu ermöglichen, in das Gehäuse (15) einzutreten;
b) einen Wärmetauscher (14), der innerhalb des Gehäuses angeordnet und mit einem inneren
Hohlraum (16, 38) ausgeführt ist, wobei der Wärmetauscher mehrere Wärmerippen (18)
aufweist, die sich von dem inneren Hohlraum (16, 38) nach Außen erstrecken;
c) einen Luftauslass (25, 27), um es Luft zu ermöglichen, in das Äußere des Gehäuses
(15) durchzudringen; und
d) eine elektrische Heizung (12), die innerhalb des inneren Hohlraums (16, 38) des
Wärmetauschers (14) montiert ist,
gekennzeichnet, dass
e) das äußere geometrische Profil des Wärmetauschers die innere Geometrie der Luftverteilungskammer
komplimentiert, um Umwegluftpassagen (19) zuwischen den mehreren Wärmerippen (18)
und der Innenwand des Gehäuses (15) zu bilden.
2. System (13) gemäß Anspruch 1, wobei der Auslass (25, 27) eine Vielzahl von Öffnungen
(27) aufweist.
3. System (13) gemäß Anspruch 1, bei dem die Heizung (12) durch eine Heizung (12) vom
Festkartuschentyp gebildet wird, die in Materialzusammensetzung, Durchmesser, Länge
und Wattzahl schwanken kann.
4. System (13) gemäß Anspruch 1, wobei das Gehäuse (15) aufweist:
a) einen Einlasshohlraum (20),
b) eine Blende (21),
c) die Luftpassagen (19),
d) eine oder mehrere Öffnungskammern (25), und
e) eine Reihe von Öffnungen (27), die es Luft ermöglichen, von der oder den Öffnungskammer(n)
(25) in das Äußere des Gehäuses (15) des Luftverteilungssystems (13) überzutreten,
und
f) eine interne Konstruktion, die in der Lage ist, die Heizung (12) aufzunehmen, was
es der Wärme ermöglicht, effizient von der Heizung (12) durch die interne Konstruktion
auf die Luft überzugehen, wenn die Luft von der Blende (21) auf die Öffnungen (27)
übergeht;
g) wobei die elektrische Heizung (12) innerhalb der inneren Konstruktion und des Gehäuses
(15) des Luftverteilungssystems (15) angebracht ist.
5. System (13) gemäß Anspruch 1, bei dem die Heizung (12) mit einer variablen Leistungsdichte
konstruiert ist, um ein gleiches Temperaturprofil entlang der axialen Länge des Gehäuses
(15) zu liefern.
6. System (13) gemäß Anspruch 1, weiterhin aufweisend:
a) ein Mittel (44) zum Aufnehmen von Druckluft;
b) ein Mittel (49) zum Erzeugen von wärmeaufnehmender elektrischer Leistung;
c) ein oder mehrere Luftverteilungssysteme (13), die Wärme aufnehmen und die Druckluft
(44) verteilen;
d) ein Mittel (42) zur Steuerung der Strömung der Druckluft (44), die durch das Luftverteilungssystem
(13) durchtritt, wobei das Steuermittel (42) einen Luftströmungsregler (42) enthält;
und
e) ein Mittel (47) zum Steuern der Temperatur der durch das Luftverteilungssystem
(13) durchtretenden Luft, wobei das Mittel (47) einen leistungsmodulierenden elektronischen
Temperaturcontroller enthält, wobei das Luftverteilungssystem (13), das Mittel (42)
zur Steuerung der Strömung und das Mittel (47) zur Steuerung der Temperatur in einem
einzigen Gehäuse (53) angeordnet sind.
7. System (13) gemäß Anspruch 1, weiterhin aufweisend:
a) einen Wärmefühler (51), der an einer wärmeleitenden Schiebeplatte (63) in Kontakt
mit oder die zu trocknenden Materialien abstützend montiert ist,
b) wobei der Wärmefühler (51) an einer Stelle montiert ist, wo das zu trocknende Material
bereits dem Großteil der Aufenthaltszeit der Trocknungseinheit (7, 9) ausgesetzt ist;
und
c) wobei der Wärmefühler (51) in der Lage ist, die Temperatur des zu trocknenden Materials
zu erlangen.
8. System (13) gemäß Anspruch 1, weiterhin aufweisend:
a) ein Gehäuse (62);
b) eines oder mehrere Gehäuse (15) wobei jedes Gehäuse (15) eine Luftverteilungskammer
bildet und aufweist:
b1) einen Lufteinlass (20) um es Luft zu ermöglichen, in das Gehäuse (15) einzutreten,
b2) einen inneren Hohlraum (16, 38) und
b3) einen Luftauslass (25, 27), um es Luft zu ermöglichen, in das Äußere des Gehäuses
(15) überzutreten;
c) eine elektrische Heizung (12), die innerhalb des Inneren Hohlraums (16, 38) des
Gehäuses (15) montiert ist;
d) mindestens eine Steuerung (42, 47) zum Beeinflussen der Menge der Zwangslufttrocknung;
und
e) wobei das eine oder mehrere Gehäuse (15) und die Steuerung (42, 47) innerhalb des
Gehäuses (62) eingeschlossen sind.
9. System (13) gemäß Anspruch 8, wobei die Steuerung (42, 47) eine Heizungssteuerung
(47) aufweist zum Steuern der Lufttemperatur.
10. System (13) gemäß Anspruch 8, wobei die Steuerung (42, 47) eine Luftströmungssteuerung
(42) aufweist.
11. System (13) gemäß Anspruch 1, weiterhin aufweisend:
a) eine Vielzahl von Gehäusen (15), wobei jedes Gehäuse (15) eine Luftverteilungskammer
bildet und aufweist:
a1) einen Lufteinlass (20), um es Luft zu ermöglichen, in das Gehäuse (15) einzutreten,
a2) einen inneren Hohlraum (16, 38),
a3) einen Luftauslass (25, 27), um es Luft zu ermöglichen, in das Äußere des Gehäuses
(15) überzutreten; und
b) eine elektrische Heizung (12), die innerhalb des inneren Hohlraums (16, 38) des
Gehäuses (15) montiert ist; und
c) einen Luftverteilungspfad (19), der mit den Gehäusen (15) verbunden ist.
1. Système de distribution d'air (13) pour une unité de séchage à air chaud forcé (7,
9), comprenant :
a) un boîtier (15) formant un plénum de distribution d'air avec une entrée d'air (20)
pour permettre à l'air d'entrer dans ledit boîtier (15) ;
b) un échangeur d'air (14) qui est placé à l'intérieur dudit boîtier et étant conçu
avec une cavité interne (16, 38), l'échangeur de chaleur ayant plusieurs ailettes
thermiques (18) qui s'étendent vers l'extérieur à partir de la cavité interne (16,
38) ;
c) une sortie d'air (25, 27) pour permettre à l'air de passer à l'extérieur dudit
boîtier (15) ; et
d) un dispositif de chauffage électrique (12) monté à l'intérieur de ladite cavité
interne (16, 38) dudit échangeur de chaleur (14),
caractérisé en ce que :
e) le profil géométrique externe de l'échangeur de chaleur complète la géométrie interne
du plénum de distribution d'air afin de former des passages d'air indirects (19) entre
la pluralité d'ailettes thermiques (18) et une paroi interne du boîtier (15).
2. Système (13) selon la revendication 1, dans lequel ladite sortie (25, 27) comprend
une pluralité d'orifices (27).
3. Système (13) selon la revendication 1, dans lequel ledit dispositif de chauffage (12)
comprend un dispositif de chauffage de type à cartouche solide (12) qui peut varier
du point de vue de la composition du matériau, du diamètre, de la longueur et du wattage.
4. Système (13) selon la revendication 1, dans lequel ledit boîtier (15) comprend :
a) une cavité d'entrée (20),
b) un déflecteur (21),
c) lesdits passages d'air (19),
d) une chambre (des chambres) à orifice unique ou à plusieurs orifices (25), et
e) une série d'orifices (27) permettant à l'air de passer de ladite (desdites) chambre(s)
à orifice(s) (25) à l'extérieur dudit boîtier (15) dudit système de distribution d'air
(13), et
f) une construction interne capable d'accepter ledit dispositif de chauffage (12)
qui permet à la chaleur d'être efficacement transportée à partir dudit dispositif
de chauffage (12) en passant par ladite construction interne jusqu'à l'air lorsque
l'air passe dudit déflecteur (21) auxdits orifices (27) ;
g) ledit dispositif de chauffage électrique (12) monté à l'intérieur de ladite construction
interne dudit boîtier (15) dudit système de distribution d'air (15).
5. Système (13) selon la revendication 1, dans lequel ledit dispositif de chauffage (12)
est construit avec une densité de puissance variable afin de fournir un profil de
température identique le long de la longueur axiale dudit boîtier (15).
6. Système (13) selon la revendication 1, comprenant en outre :
a) des moyens (44) pour recevoir de l'air sous pression ;
b) des moyens (49) pour générer de la chaleur recevant la puissance électrique ;
c) un seul ou plusieurs systèmes de distribution d'air (13) qui reçoivent, chauffent
et dispersent ledit air sous pression (44) ;
d) des moyens (42) pour contrôler l'écoulement dudit air sous pression (44) passant
par ledit système de distribution d'air (13), lesdits moyens de contrôle (42) comprennent
un régulateur d'écoulement d'air (42) ; et
e) des moyens (47) pour contrôler la température de l'air passant par ledit système
de distribution d'air (13), lesdits moyens (47) comprennent un contrôleur de température
électronique à modulation de puissance, dans lequel ledit système de distribution
d'air (13), lesdits moyens (42) pour contrôler l'écoulement, et lesdits moyens (47)
pour contrôler la température sont positionnés dans une seule enceinte (53).
7. Système (13) selon la revendication 1, comprenant en outre :
a) un thermocouple (51) monté sur une plaque coulissante à conduction thermique (63)
en contact ou supportant les matériaux qui sont séchés,
b) le thermocouple (51) étant monté à un emplacement où le matériau qui est séché
a déjà été exposé pendant la majeure partie du temps de séjour de l'unité de séchage
(7, 9) ; et
c) le thermocouple (51) étant capable d'atteindre la température du matériau qui est
séché.
8. Système (13) selon la revendication 1, comprenant en outre :
a) une enceinte (62) ;
b) un ou plusieurs boîtiers (15), chaque boîtier (15) formant un plénum de distribution
d'air et ayant :
b1) une entrée d'air (20) pour permettre à l'air d'entrer dans ledit boîtier (15),
b2) une cavité interne (16, 38), et
b3) une sortie d'air (25, 27) pour permettre à l'air de passer à l'extérieur dudit
boîtier (15) ;
c) un dispositif de chauffage électrique (12) monté à l'intérieur de ladite cavité
interne (16, 38) de chacun desdits boîtiers (15) ;
d) au moins une commande (42, 47) pour influencer la quantité de séchage à air forcé
; et
e) dans lequel lesdits un ou plusieurs boîtiers (15) et ladite commande (42, 47) sont
contenus à l'intérieur de ladite enceinte (62).
9. Système (13) selon la revendication 8, dans lequel ladite commande (42, 47) comprend
une commande de dispositif de chauffage (47) pour contrôler la température de l'air.
10. Système (13) selon la revendication 8, dans lequel ladite commande (42, 47) comprend
une commande d'écoulement d'air (42).
11. Système (13) selon la revendication 1, comprenant en outre :
a) une pluralité de boîtiers (15), chaque boîtier (15) formant un plénum de distribution
d'air et ayant :
a1) une entrée d'air (20) pour permettre à l'air d'entrer dans ledit boîtier (15),
a2) une cavité interne (16, 38),
a3) une sortie d'air (25, 27) pour permettre à l'air de passer à l'extérieur dudit
boîtier (15) ; et
b) un dispositif de chauffage électrique (12) monté à l'intérieur de ladite cavité
interne (16, 38) de chacun desdits boîtiers (15) ; et
c) une trajectoire de distribution d'air (19) raccordée auxdits boîtiers (15).