[0001] The present invention relates to a unit for sterilizing a web of packaging material
for a machine for packaging food products.
[0002] As is known, many food products, such as fruit juice, UHT milk, wine, tomato sauce,
etc., are sold in packages made of sterilized sheet packaging material.
[0003] A typical example of this type of package is the parallelepiped-shaped package for
liquid or pourable food products known as Tetra Brik Aseptic (registered trademark),
which is made by folding and sealing laminated strip packaging material.
[0004] The packaging material has a multilayer structure substantially comprising a base
layer for stiffness and strength, which may be defined by a layer of fibrous material,
e.g. paper, and a number of layers of heat-seal plastic material, e.g. polyethylene
film, covering both sides of the base layer.
[0005] In the case of aseptic packages for long-storage products, such as UHT milk, the
packaging material also comprises a layer of gas- and light-barrier material, e.g.
aluminium foil or ethyl vinyl alcohol (EVOH) film, which is superimposed on a layer
of heat-seal plastic material, and is in turn covered with another layer of heat-seal
plastic material forming the inner face of the package eventually contacting the food
product.
[0006] As is known, packages of this sort are produced on fully automatic packaging machines,
on which a continuous tube is formed from the web-fed packaging material. The web
of packaging material is unwound off a reel and fed through a sterilizing unit, where
it is sterilized, e.g. by immersion in a chamber of liquid sterilizing agent, such
as a concentrated solution of hydrogen peroxide and water.
[0007] The web is then fed into an aseptic chamber where the sterilizing agent is evaporated
by heating. The web is then folded into a cylinder and sealed longitudinally to form
in known manner a continuous vertical tube, which in effect forms an extension of
the aseptic chamber. The tube of packaging material is filled continuously with the
food product by pouring and then fed to a form-and-seal unit, where it is gripped
between pairs of jaws which seal the tube transversely to form pillow packs. The pillow
packs are then separated from one another by cutting the seal joining each two adjacent
packs, and are conveyed to a final folding station where they are folded mechanically
into the finished shape.
[0008] More specifically, the sterilizing unit comprises a chamber containing the sterilizing
agent, and into which the web is fed continuously. The sterilizing chamber conveniently
comprises two parallel vertical branches connected at the bottom to define a U-shaped
path long enough with respect to the travelling speed of the web to allow enough time
to treat the packaging material.
[0009] For effective, relatively fast treatment, e.g. in about 7 seconds, to reduce the
size of the sterilizing chamber, the sterilizing agent must be maintained at a high
temperature, e.g. of around 73°C.
[0010] Being covered with a layer of heat-seal plastic material, normally polyethylene,
the faces of the web of packaging material are completely impermeable to the sterilizing
agent. Along the edges of the web, however, the layer of fibrous material is exposed,
and tends to soak up the sterilizing agent. This is known in the trade as "edge wicking"
(edge absorption), and remains within acceptable limits providing the web is only
kept for a short time inside the sterilizing chamber, as is the case during normal
operation of the machine.
[0011] If for any reason the machine is stopped, however, the sterilizing chamber must be
emptied immediately. Otherwise, the edges of the layer of fibrous material soak up
the sterilizing agent, and edge wicking of a few millimetres in width inevitably impairs
subsequent longitudinal sealing of the web to form the tube of packaging material
as described above.
[0012] In other words, in the event the machine is stopped, the sterilizing agent is drained
rapidly into a normally double-walled hold tank. The inner walls define an inner shell
of the tank containing the sterilizing agent, and the outer walls form an outer shell
of the tank defining, with the inner shell, a normally air-filled gap which provides
for thermally insulating the sterilizing agent.
[0013] Following stoppage, and particularly when restarting the machine after a short stoppage,
normally of no more than 15-20 minutes, edge wicking tends to occur anyway, despite
emptying the sterilizing chamber.
[0014] Careful study of the phenomenon has identified several causes, foremost of which
are:
- the porosity of the fibrous material, which, however, can only be reduced so far for
paper manufacturing cost reasons;
- hydrostatic pressure, which is also difficult to reduce, on account of the height
of the U-shaped sterilizing chamber depending on the necessary processing time, and
only being reducible by altering the architecture of the sterilizing unit, thus complicating
the system as a whole; and
- the temperature of the sterilizing chamber during the stoppage, and of the sterilizing
agent when fed back into the chamber.
[0015] As regards the latter, in particular, a difference of even only a few degrees between
the temperature of the chamber during the stoppage and the temperature of the sterilizing
agent fed back into the chamber has been found to produce severe edge wicking. In
conventional machines, this difference in temperature is caused by the tendency of
the emptied sterilizing chamber to increase in temperature, on account of the inevitable
delay in response of the thermostatic control to the reduction in heat absorption
caused by emptying the chamber: the temperature inside the chamber is therefore normally
around at least 80°C. As a result, the residual sterilizing agent on the walls of
the chamber and in the packaging material tends to evaporate, thus producing a saturated-vapour
condition of the chamber, so that the pores of the layer of fibrous material contain
a saturated air/vapour mixture.
[0016] When liquid sterilizing agent is fed into the chamber, at a temperature inevitably
lower than that inside the sterilizing chamber (due to dissipation, the temperature
of the sterilizing agent fed back into the sterilizing chamber is at best a few degrees
lower than that of the sterilizing agent inside the sterilizing chamber when the machine
was arrested), the temperature of the web, and therefore of the air/vapour mixture
in the pores, is reduced. This reduction has a practically negligible effect on the
air, which undergoes a contraction in volume of only a few percent, but has a very
serious effect on the vapour, which recondenses and so assumes a much smaller volume
in the liquid state. This drastic reduction in volume has the effect of "sucking"
the sterilizing agent into the pores of the fibrous material layer, which is the major
cause of edge wicking.
[0017] By way of a solution to the problem, which is less serious during prolonged stoppages,
due to evaporation of the residual liquid sterilizing agent and a reduction in relative
humidity inside the sterilizing chamber, sterilizing units have been devised, in which,
before being fed into the sterilizing chamber, the sterilizing agent is heated by
circulating it through a heating circuit comprising a countercurrent heat exchanger
using water as the operating fluid.
[0018] More specifically, the water is fed to the heat exchanger by a circulating pump having
an inlet connected to the water mains and an outlet connected to an electric resistor
heater interposed between the pump and the exchanger. A compressed air/water tank,
for compensating the pressure of the heating circuit, and a maximum pressure valve
are branch-connected to a fill conduit in turn connecting the water mains to the pump.
[0019] Packaging machines of the above type are used widely and satisfactorily in a wide
range of food industries, and performance of the sterilizing unit, in particular,
is such as to ensure a wide margin of safety as regards regulations governing aseptic
packages and the permitted amount of residual sterilizing agent.
[0020] Some needs are felt within the industry, however, for further improvements, particularly
as regards:
- the efficiency and speed of the heat transfer to the sterilizing agent;
- the reduction of complexity and cost of the sterilizing unit;
- the independence of the heating circuit from the running of the water system (it should
be observed that possible missing of water from the water mains may determine burning
of the resistor heater of the heating circuit); and
- the reduction of the sterilizing chamber filling time, in order to further reduce
possible risks of edge wicking during restart of production after stoppage of the
packaging machine.
[0021] It is an object of the present invention to provide a sterilizing unit, designed
to meet at least one of the above needs in a straightforward, low-cost manner.
[0022] According to a first aspect of the present invention, there is provided a sterilizing
unit as claimed in claim 1.
[0023] According to another aspect of the present invention, there is provided a sterilizing
unit as claimed in claim 13.
[0024] Four preferred, non-limiting embodiments of the present invention will be described
by way of example with reference to the accompanying drawings, in which:
Figure 1 shows a schematic view in perspective of a sterilizing unit in accordance
with a first embodiment of the invention;
Figure 2 shows a larger-scale view in perspective of a heating device for heating
a sterilizing agent used in Figure 1 sterilizing unit;
Figure 3 shows a vertical section of Figure 2 heating device;
Figure 4 shows a schematic view in perspective of a sterilizing unit in accordance
with a second embodiment of the invention;
Figure 5 shows a schematic view in perspective of a sterilizing unit in accordance
with a third embodiment of the invention; and
Figure 6 shows a schematic view in perspective of a sterilizing unit in accordance
with a fourth embodiment of the invention.
[0025] Number 1 in Figure 1 indicates as a whole a sterilizing unit adapted to sterilize
a web 2 of packaging material for a packaging machine (of the known type described
above) for producing sealed packages (not shown) of food products, in particular pourable
or liquid food products, such as pasteurized or UHT milk, fruit juice, wine, etc.
[0026] Web 2 may also be used for packaging food products that are pourable when producing
packages, and sets after packages are sealed. One example of such a food product is
a portion of cheese, that is melted when producing packages, and sets after packages
are sealed.
[0027] Web 2 is fed in known manner, not shown, to unit 1 off a reel, so as to be sterilized
before being formed into a succession of sealed packages of food products. The form,
fill, and seal operations performed in known manner on web 2 (as described above)
downstream from unit 1 do not form part of the present invention, and are referred
to here purely for the sake of clarity.
[0028] Web 2 has a multilayer structure and comprises a base layer for stiffness and strength,
which may be made of fibrous material, e.g. paper or mineral-filled polypropylene
material, and a number of layers of heat-seal plastic material, e.g. polyethylene
film, covering both sides of the base layer.
[0029] In the case of aseptic packages for long-storage products, such as UHT milk, web
2 also comprises a layer of gas-barrier material, e.g. aluminium foil or ethyl vinyl
alcohol (EVOH) film, which is superimposed on a layer of heat-seal plastic material,
and is in turn covered with another layer of heat-seal plastic material eventually
contacting the food product.
[0030] With reference to Figure 1, unit 1 substantially comprises a U-shaped sterilizing
chamber or bath 3 containing a hot liquid sterilizing agent. Chamber 3 is defined
by two vertical, respectively inlet and outlet, channel-shaped branches 4, 5 having
respective top openings 6, 7 and connected to each other at the bottom by a bottom
portion 8.
[0031] By way of example, Figure 1 shows a number of horizontal rollers for guiding web
2 through branches 4, 5 and bottom portion 8 of chamber 3, and more specifically:
an input roller 9 close to top opening 6 of branch 4, an output roller 10 close to
top opening 7 of branch 5, and a return roller 11 housed inside bottom portion 8 of
chamber 3.
[0032] Inside chamber 3, web 2 therefore describes a U-shaped path, the length of which
depends on the travelling speed of web 2, and is such as to keep the packaging material
long enough inside the sterilizing agent.
[0033] Chamber 3 forms part of a sterilizing agent control circuit 15 also comprising:
- a sterilizing agent hold tank 16;
- a conduit 17 extending between tank 16 and bottom portion 8 of chamber 3 for filling/draining
the latter;
- a pump 18 immersed in tank 16 and powered by an electric motor 19; and
- a feed conduit 20 connecting pump 18 to an intermediate section of conduit 17 via
a valve 21 so as to divide conduit 17 into a bottom drain portion 22, leading to tank
16 via a valve 23, and a top drain/fill portion 24, leading to bottom portion 8 of
chamber 3.
[0034] Tank 16 provides for topping up chamber 3 to make up the loss in sterilizing agent
caused by the wet outgoing web 2, and for holding the sterilizing agent when draining
chamber 3, e.g. in the event of any stoppage of the packaging machine.
[0035] Tank 16 is connected by respective taps 12a, 12b to two different drain conduits
13a, 13b for sampling and changing the sterilizing agent respectively.
[0036] Valve 21 is preferably a two-way, two-position, normally-open type, but with a flow
on/off member (not shown) allowing leakage in the closed position (restricted flow
condition) to compensate, as stated, for inevitable sterilizing agent losses in chamber
3 during the production cycle. For this purpose, a commercial valve is sufficient,
with a suitably sized hole formed in the on/off member.
[0037] Valve 23 is also preferably a two-way, two-position, normally-open type for safety
reasons, to allow draining of chamber 3 in the event of a malfunction of the electric
system.
[0038] In view of the above, conduit 20 and portion 24 of conduit 17 define a feed line
F extending from tank 16 to bottom portion 8 of sterilizing chamber 3 and which can
be activated selectively to feed the latter with the sterilizing agent, whilst the
whole conduit 17 defines a drain line D which can be activated selectively to drain
the sterilizing agent from the sterilizing chamber 3. In other words, in the specific
embodiment shown in Figure 1, drain line D and feed line F have a part in common defined
by portion 24 of conduit 17.
[0039] Circuit 15 also comprises a recirculating conduit 25 connecting tank 16 to a known
overflow (not shown) formed in the top of inlet branch 4 of chamber 3 to determine
the maximum sterilizing agent level in chamber 3.
[0040] Unit 1 further comprises a system (known per se and not shown) for controlling the
temperature of the sterilizing agent in sterilizing chamber 3 through heating the
walls of branches 4, 5.
[0041] Unit 1 also comprises a device 26 (please see in particular Figures 2 and 3) for
heating the sterilizing agent before it is fed into chamber 3.
[0042] Advantageously, device 26 substantially comprises electric heating means 30 and a
heat exchanger 31 arranged in contact with heating means 30 and defining a serpentine-shaped
passage 32 for the sterilizing agent.
[0043] In particular, heat exchanger 31 is preferably made of stainless steel and is defined
by a box-shaped plate, i.e. a box element having a thickness strongly smaller than
the other sizes; as clearly shown in Figure 2, heat exchanger 31 is completely closed
from the outside and has an inlet 33 for receiving the sterilizing agent to be heated
and an outlet 34 for feeding the heated sterilizing agent to control circuit 15.
[0044] More specifically, in the embodiment of Figure 1, inlet 33 of heat exchanger 31 is
connected, through a conduit 27, to a portion of conduit 20 interposed between valve
21 and tank 16, whilst outlet 34 is connected, through a conduit 28, to recirculating
conduit 25.
[0045] Heat exchanger 31 is arranged in the vertically-oriented configuration shown in Figures
2 and 3, wherein its thickness extends parallel to a horizontal direction, and inlet
33 is located at a lower position than outlet 34; more specifically, heat exchanger
31 is delimited by a bottom wall 35, a top wall 36, a front wall 37, a rear wall 38,
and a pair of thin side walls 39, 40.
[0046] Heat exchanger 31 is provided internally with diverting means 41 delimiting, together
with walls 35-40, serpentine-shaped passage 32 for the sterilizing agent; in the solution
depicted in Figures 2 and 3, diverting means 41 comprise:
- a first series of baffles 42 extending substantially parallel to a horizontal direction
from side wall 39 towards side wall 40, and leaving a small-sized gap 43 with the
latter;
- a second series of baffles 44 of the same type of baffles 42, each of them extends
substantially parallel to a horizontal direction from side wall 40 towards side wall
39, leaves a small-sized gap 45 with the latter, and is vertically interposed between
a pair of relative baffles 42; and
- a third series of baffles 46 of limited length, inclined with respect to the horizontal
direction and each located close to a relative gap 43, 45.
[0047] Each baffle 42, 44 is delimited, at the top, by a ramp-shaped surface 47 rising in
the sterilizing agent flow direction; in a completely analogous way, bottom wall 35
has a ramp-shaped inner surface 48 also rising in the flow direction.
[0048] In this way, during the flow through heat exchanger 31, the sterilizing agent is
lowerly in contact with ramp-shaped surfaces 47, 48, i.e. it contacts lower ramp-shaped
parts (47, 48) of the walls delimiting serpentine-shaped passage 32.
[0049] The above-described baffles 42, 44, 46 define serpentine-shaped passage 32 as consisting
of a plurality of C-shaped portions joined to each other.
[0050] This kind of configuration of baffles 42, 44, 46 allows to avoid formation of overheated
sterilizing agent pockets within heat exchanger 31.
[0051] Heating means 30 comprise a pair of electrically-powered heating carpets 51 maintained
in close contact under pressure with respective opposite walls 37, 38 of heat exchanger
31. In particular, the sandwich structure defined by heat exchanger 31 and heating
carpets 51 is maintained pressed by a plurality of pairs of clamping bars 52 acting
on the opposite heating carpets 51 through the interposition of respective foamed
polymeric sheets 53, preferably made of silicone.
[0052] More precisely, bars 52 of each pair extend parallel to walls 36, 37, 38 of heat
exchanger 31, have opposite ends laterally protruding from the sandwich structure
formed by heat exchanger 31, heating carpets 51 and foamed polymeric sheets 53, and
are connected to each other, at their opposite ends, by respective transversal screws
54.
[0053] Unit 1 operates as follows.
[0054] When cold-starting, chamber 3 is empty, and all the sterilizing agent is inside tank
16.
[0055] Pump 18 is turned on to pump a large amount of sterilizing agent, e.g. 50 l/min,
through heating device 26.
[0056] At this stage, valve 21 is closed, but, as stated, allows a small amount of leakage
(a few liters/min) to portion 24 of conduit 17, and therefore along feed line F (restricted
flow condition). Valve 23 is open, so chamber 3 is not filled until the best production
cycle-start conditions are achieved. In the meantime, the walls of branches 4, 5 of
sterilizing chamber 3 are heated.
[0057] The cycle-start conditions are, for example, 72°C for the walls of sterilizing chamber
3, and 75°C for the sterilizing agent in tank 16 (fill temperature). In which case,
sterilizing chamber 3 and web 2 being dry, there is practically no risk of edge wicking.
[0058] At the start of the cycle, valve 21 is opened, and valve 23 is closed, so sterilizing
chamber 3 is filled rapidly with sterilizing agent; after which, valve 21 is closed.
[0059] During normal operation of the packaging machine, the sterilizing agent is maintained
at a minimum temperature of 73°C in both sterilizing chamber 3 and tank 16. If either
one of these temperatures falls below the predetermined threshold value, a heating
cycle is activated by means of the system controlling the temperature of the walls
of branches 4, 5 and heating device 26, respectively.
[0060] Pump 18 is run continually to maintain a continuous flow through heating device 25
and continuous leakage of conveniently a few liters/minute of sterilizing agent through
valve 21, to compensate for the loss in sterilizing agent from sterilizing chamber
3 caused, as stated, by the wet outgoing web 2, and to keep the bottom portion 8 of
sterilizing chamber 3 and feed line F hot. Surplus sterilizing agent overflows from
sterilizing chamber 3, and flows along recirculating conduit 25 back into tank 16.
[0061] In the event of stoppage of the packaging machine, valve 23 is opened immediately
to drain the sterilizing agent rapidly from sterilizing chamber 3 into tank 16.
[0062] In the event of a short stoppage of less than 15-20 minutes, sterilizing chamber
3 is cooled to below operating temperature, and simultaneously the sterilizing agent
is heated to the fill temperature (e.g. 75°C).
[0063] Sterilizing chamber 3 is cooled by turning off the system heating the walls of branches
4, 5, and blowing in sterile air at a lower temperature than that of sterilizing chamber
3.
[0064] The sterilizing agent is heated by electric heating carpets 51 of heating device
26.
[0065] The above conditions are achieved rapidly, normally in less than a minute, and ensure
an acceptable degree of edge wicking at the next start-up. In fact, cooling sterilizing
chamber 3 and preheating the sterilizing agent to a higher temperature prevents condensation
of the steam inside sterilizing chamber 3 when chamber 3 is filled.
[0066] In the light of the above, unit 1 permits to achieve the following advantages with
respect to the known units.
[0067] First of all, thanks to the use of electric heating carpets 51 and plate heat exchanger
31, the produced heat is directly transferred to the sterilizing agent, without passing
through an intermediate operating fluid, so reducing thermal losses and increasing
efficiency of heat transfer. In this way, also the speed of heat transfer can be increased:
in fact, in addition to allow a direct heating of the sterilizing agent, so avoiding
to heat an intermediate medium in turn designed to transfer its heat to the sterilizing
agent, new heating carpets 51 can be heated to temperatures higher than the water
boiling point (100°C), point that could not be reached in the case of the water/sterilizing
agent heat exchanger since steam and bubbles may interfere with the normal water circulation.
[0068] Moreover, the new solution allows to eliminate all the components of the water circuit
(pump, valves, etc.), so avoiding maintenance thereof and reducing complexity and
cost of sterilizing agent control circuit 15.
[0069] Last but not least, the very compact and thin structure of heating device 26 allows
a strong reduction of the overall bulk of control circuit 15 with respect to known
sterilizing agent control circuits.
[0070] Figure 4 shows a different embodiment, indicated as a whole by 1', of a sterilizing
unit in accordance with the present invention, and which is described below only insofar
as it differs from unit 1, and using the same reference numbers for parts identical
or corresponding to those already described.
[0071] Unit 1' differs from unit 1 by the fact that outlet 34 of heat exchanger 31 is connected,
through conduit 28, to portion 24 of conduit 17, i.e. to feed line F, instead of recirculating
conduit 25. It is therefore evident that leakage of sterilizing agent through valve
21 in the closed condition is useless in this case, and therefore valve 21 may be
replaced with a two-way, two-position, normally-open commercial valve 21' having no
hole formed in the on/off member.
[0072] In use, when valve 23 is in the open condition, the sterilizing agent flow exiting
from outlet 34 of heating device 26 is recirculated into tank 16 through drain line
D.
[0073] This particular solution allows to achieve the following results:
- a) when valve 21' is open and valve 23 is closed to perform filling of sterilizing
chamber 3, all the sterilizing agent delivered by pump 18 is fed to this chamber,
i.e. there is no fraction of the pumped flow which is recirculated into tank 16;
- b) during the production cycle (both valves 21' and 23 closed), the sterilizing agent
just heated by heating device 26 is immediately delivered to sterilizing chamber 3,
instead of being first recirculated to tank 16 and then delivered to chamber 3.
[0074] In this way, it is possible, on the one hand, to obtain a reduction of the filling
time of sterilizing chamber 3, so further reducing possible risks of edge wicking
during restart of production after stoppage of the packaging machine, and, on the
other hand, to further increase thermal efficiency of control circuit 15.
[0075] Figure 5 shows another different embodiment, indicated as a whole by 1" , of a sterilizing
unit in accordance with the present invention, and which is described below only insofar
as it differs from unit 1', and using the same reference numbers for parts identical
or corresponding to those already described.
[0076] In particular, unit 1" differs from unit 1' only insofar as a further valve 60",
of the same type as valve 21 of unit 1 (i.e. with an on/off member provided with a
sized hole to allow, in the closed or restricted flow condition, leakage of few liters/min
of sterilizing agent), is arranged along the portion of conduit 17 extending between
conduit 28 and sterilizing chamber 3.
[0077] In this case, during the production cycle, valve 60" is maintained in the closed
condition (with a continuous leakage of a few liters/minute of sterilizing agent)
so allowing a reduction of the sterilizing agent flow recirculated between sterilizing
chamber 3 and tank 16.
[0078] Figure 6 shows a further embodiment, indicated as a whole by 1"', of a sterilizing
unit in accordance with the present invention, and which is described below only insofar
as it differs from unit 1" , and using the same reference numbers for parts identical
or corresponding to those already described.
[0079] In particular, unit 1"' differs from unit 1" only in that the further valve 60"',
for reducing sterilizing agent flow recirculated between sterilizing chamber 3 and
tank 16 during the production cycle, is arranged along conduit 28, which has a smaller
section that that of conduit 17; therefore, it is possible to use a valve suitable
for operating with flow rates lower than those along conduit 17 and whose cost is
consequently smaller than that of valve 60".
[0080] Clearly, changes may be made to the sterilizing units 1, 1', 1", 1'" as described
herein without, however, departing from the protective scope defined in the accompanying
claims.
1. A unit (1, 1', 1", 1"') for sterilizing a web (2) of packaging material for a machine
for packaging food products, said unit (1, 1', 1", 1"') comprising:
- a sterilizing chamber (3) containing a sterilizing agent;
- conveying means (9, 10, 11) for feeding said web (2) through said sterilizing chamber
(3) before the web (2) is formed into a succession of sealed packages of food products;
- a hold tank (16) for said sterilizing agent;
- feed means (F, 18) which can be activated selectively to feed said sterilizing agent
from said tank (16) to said sterilizing chamber (3);
- drain means (D, 23) which can be activated selectively to drain said sterilizing
agent from a bottom portion (8) of said sterilizing chamber (3) into said tank (16)
in the event of stoppage of the packaging machine; and
- a heating device (26) for heating said sterilizing agent before feeding it to the
sterilizing chamber (3);
characterized in that said heating device (26) comprises electric heating means (30) and a heat exchanger
(31) arranged in contact with said heating means (30) and defining a serpentine-shaped
passage (32) for said sterilizing agent.
2. A unit as claimed in claim 1, wherein said serpentine-shaped passage (32) is defined
by a plurality of C-shaped portions joined to each other.
3. A unit as claimed in claim 1 or 2, wherein said serpentine-shaped passage (32) comprises
ramp-shaped surfaces (47, 48) lowerly contacting the sterilizing agent flow.
4. A unit as claimed in any one of the foregoing claims, wherein said heat exchanger
(32) comprises a box-shaped plate provided internally with diverting means (41) delimiting
said serpentine-shaped passage (32).
5. A unit as claimed in any one of the foregoing claims, wherein said electric heating
means (30) comprise a pair of electrically-powered heating carpets (51) maintained
in close contact under pressure with opposite parts (37, 38) of said heat exchanger
(31).
6. A unit as claimed in any one of the foregoing claims, wherein said feed means comprise
a feed line (F) extending from said tank (16) to said sterilizing chamber (3), and
said drain means comprise a drain line (D) extending from said tank (16) to said bottom
portion (8) of said sterilizing chamber (3), and wherein said feed line (F) and said
drain line (D) can be selectively connected via first valve means (23).
7. A unit as claimed in claim 6, wherein said feed line (F) and said drain line (D) comprise
a feed conduit (20) extending from said tank (16), a drain conduit (22) leading to
said tank (16) via said first valve means (23), and a common conduit (24) connecting
said feed conduit (20) and said drain conduit (22) to said bottom portion (8) of said
sterilizing chamber (3).
8. A unit as claimed in any one of the foregoing claims, wherein said sterilizing chamber
(3) and said tank (16) are further connected by a recirculating conduit (25), and
wherein said heat exchanger (31) has a sterilizing agent inlet (33) connected to said
feed means (F, 18) and a sterilizing agent outlet (34) connected to said recirculating
conduit (25).
9. A unit as claimed in claims 7 or 8, wherein second valve means (21) are arranged along
a portion of said feed line (F), interposed between said sterilizing chamber (3) and
a section of the feed line (F) connected to said inlet (33) of said heating device
(26), and can be set between a completely open condition and a restricted flow condition.
10. A unit as claimed in any one of claims 1 to 7, wherein said heat exchanger has a sterilizing
agent inlet (33) and a sterilizing agent outlet (34) both connected to said feed means
(F, 18).
11. A unit as claimed in claim 10, wherein said sterilizing agent outlet (34) of said
heating device (26) is also connected to said drain means (D, 23).
12. A unit as claimed in claim 10 or 11, wherein said outlet (34) of said heating device
(26) is connected to said sterilizing chamber (3) via said feed line (F) and third
valve means (60", 60"') which can be set between a completely open condition and a
restricted flow condition.
13. A unit (1', 1", 1"') for sterilizing a web (2) of packaging material for a machine
for packaging food products, said unit (1', 1" , 1"') comprising:
- a sterilizing chamber (3) containing a sterilizing agent;
- conveying means (9, 10, 11) for feeding said web (2) through said sterilizing chamber
(3) before the web (2) is formed into a succession of sealed packages of food products;
- a hold tank (16) for said sterilizing agent;
- feed means (F, 18) which can be activated selectively to feed said sterilizing agent
from said tank (16) to said sterilizing chamber (3);
- drain means (D, 23) which can be activated selectively to drain said sterilizing
agent from a bottom portion (8) of said sterilizing chamber (3) into said tank (16)
in the event of stoppage of the packaging machine; and
- a heating device (26) for heating said sterilizing agent before feeding it to the
sterilizing chamber (3);
characterized in that said heating device (26) has a sterilizing agent inlet (33) and a sterilizing agent
outlet (34) both connected to said feed means (F, 18).
14. A unit as claimed in claim 13, wherein said sterilizing agent outlet (34) of said
heating device (26) is also connected to said drain means (D, 23).
15. A unit as claimed in claim 13 or 14, wherein said feed means comprise a feed line
(F) extending from said tank (16) to said sterilizing chamber (3), and said drain
means comprise a drain line (D) extending from said tank (16) to said bottom portion
(8) of said sterilizing chamber (3), and wherein said feed line (F) and said drain
line (D) can be selectively connected via first valve means (23) to allow the sterilizing
agent flow exiting from said heating device (26) to be recirculated into said tank
(16).
16. A unit as claimed in claim 15, wherein said feed line (F) and said drain line (D)
comprise a feed conduit (20) extending from said tank (16), a drain conduit (22) leading
to said tank (16) via said first valve means (23), and a common conduit (24) connecting
said feed conduit (20) and said drain conduit (22) to said bottom portion (8) of said
sterilizing chamber (3).
17. A unit as claimed in claim 15 or 16, wherein said outlet (34) of said heating device
(26) is connected to said sterilizing chamber (3) via said feed line (F) and second
valve means (60", 60"') which can be set between a completely open condition and a
restricted flow condition.
18. A unit as claimed in any one of claims 13 to 17, wherein said heating device (26)
comprises electric heating means (30) and a heat exchanger (31) arranged in contact
with said heating means (30) and defining a serpentine-shaped passage (32) for said
sterilizing agent connecting said inlet (33) and said outlet (34).
19. A unit as claimed in claim 18, wherein said serpentine-shaped passage (32) is defined
by a plurality of C-shaped portions joined to each other.
20. A unit as claimed in claim 18 or 19, wherein said serpentine-shaped passage (32) comprises
ramp-shaped surfaces (47, 48) lowerly contacting the sterilizing agent flow.
21. A unit as claimed in any one of claims 18 to 20, wherein said heat exchanger (32)
comprises a box-shaped plate provided internally with diverting means (41) delimiting
said serpentine-shaped passage (32).
22. A unit as claimed in any one of claims 18 to 21, wherein said electric heating means
(30) comprise a pair of electrically-powered heating carpets (51) maintained in close
contact under pressure with opposite parts of said heat exchanger (31).