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WHY AND HOW TO STERILIZE
IN COUNTERPRESSURE
The technology of moist-heat sterilization in counterpressure
has been developed specifically for the terminal treatment
of solutions in closed containers.
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Its primary aim is to "neutralize" the effects
of the overpressure which unavoidably forms inside containers
when they are sterilized using conventional saturated-steam
autoclaves.
This overpressure tends to make glass containers explode
and to lift their stoppers, irreversibly deforms flexible
-or rigid- plastic containers, expels the plungers of
prefilled-syringes, etc.
The collateral but not at all secondary aim is to perform
load cooling with a sterile fluid, either water or air,
thus complying with the CGMP of the F.D.A. for LVP.
Counterpressure autoclaves currently in use belong
to two types:
superheated water spray autoclaves
steam+air mixture autoclaves
To a certain extent, the two types are complementary
and our company has built both for several years. They
are also presented together in this brochure, highlighting
as clearly as possible the relative advantages of the
two types.
The figure above shows some typical products which
can be sterilized with these autoclaves. This presentation
is absolutely non-limitative, and new packages which
require careful use of counterpressure sterilization
are constantly being introduced in the market.
Our Customers should contact us during the development
of their new products/packages, since often modest adaptations
of these products/ packages allows optimisation of the
results of the sterilization processes.
Our Research & Development Service is at the disposal
of our Customers for this purpose.
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FOW
SUPERHEATED WATER SPRAY AUTOCLAVES
FOW autoclaves are based on an extremely straightforward
operating principle which is applied with a highly reliable
and mechanically very simple unit.
When the program begins, after the load to be sterilized
has been introduced, only the lower part of the chamber
is filled with treated water of adequate microbiological
quality. The chamber has a circular cross-section with
a single wall, but has rectangular doors inscribed in
the circle. The air inside the chamber is not removed.
The water, which is drawn from the bottom of the chamber
by a sanitary-type centrifugal pump, is circulated through
a moving-plate heat exchanger, also of the
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Distribution system for the
circulation water
Equipped with nozzles producing a "solid"
spray cone, mounted so as to avoid water stagnation in
the ducts of the sparger.
The rollers are mounted on special roll-bearings with
a cage made of stainless steel and require no lubrication. |
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sanitary type, which is indirectly heated in countercurrent
with mains steam.
The water is then fed back into the upper part of the
chamber and is distributed onto the load by a system
of solid-cone spray nozzles.
Water redistribution onto the lower layers of the load
is ensured by appropriate perforated supporting shelves.
Moving-plate heat exchanger
made of stainless steel, sanitary type, double function
(heating/cooling). Combines maximum efficiency and maximum
safety. Plate cleaning is spontaneously ensured by the
turbulence, speed and alternation of the circulation
fluids (steam and cooling water).
Sanitary type centrifugal pumps ensure an extremely
high water circulation speed, which is essential to
obtain optimum temperature uniformity.
Heating of the circulation water and thus of the load
is gradual but quite fast. The sterilization temperature
of 121°C is reached within approximately 25-30 minutes
inside 500 ml containers.
After the sterilization time (approximately 20 minutes)
has elapsed, the circulation water, which by then is
sterile as well, continues to circulate through the
exchanger, which however in this step is supplied with
top cold cooling water.
Within approximately 10 minutes, the temperature inside
the containers (again assumed to have a 500 ml capacity)
gradually drops to approximately 80° C, which is
the ideal temperature to also obtain rapid and spontaneous
drying of the load extracted from the autoclave.
The entire process therefore lasts approximately 60
minutes.
Throughout the process, an adequate counterpressure
of sterile air is maintained inside the chamber in order
to counterbalance, in the most appropriate and automatic
manner, the overpressure which is present at most times
within the containers.
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FOA
AIR+STEAM MIXTURE AUTOCLAVES
FOA autoclaves have a chamber with a circular cross-section,
generally with a single wall, and with rectangular doors
inscribed in the circle. In these autoclaves, too, the
air inside the chamber is not removed.
The program begins by introducing steam directly in
the chamber by means of the sparger located in the lower
circular sector.
One or more fans are located in the upper circular
sector; their number depends on the depth of the chamber.
The fans generally have a vertical axis: in case of
particular
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The part of the magnetically-driven fans (two in this
autoclave) located outside the chamber.
The fans eliminate the need to make holes in the chamber
and thus the presence of unreliable seals on the shaft,
but also avoid metallic bearings inside the chamber, which
unavoidably require lubrication |
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load requirements, it is also possible to install fans
with a horizontal axis which are obviously placed in
one of the lateral circular sectors of the chamber.
The action of the fans, combined with the action of
the flow deflectors, generates a continuous and rapid
homogenotion and circulation of the steam+air mixture
which forms in the chamber, in the direction shown by
the arrows in the functional diagram.
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The internal impeller of
the fan (the protection grid is removed): the vanes
are made of a plastic material accepted by the F.D.A.;
they reduce the weight of the impeller and ensure extremely
high efficiency and perfect static and dynamic balancing.
The flow deflector ensures efficient and uniform
circulation of the steam+air mixture during heating/sterilization
and of the air during cooling.
The battery of stainless steel hollow plates for
circulating the cooling water: these are definitely
preferable to tube-nest exchangers, since they produce
high turbulence in the circulating water and thus improving
heat exchange. They are also easy to disassemble and
inspect. The plates are hidden by the flow deflector.
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At equal temperature and pressure conditions, air is
in fact on the average 1.5 times denser than steam and
would tend to stratify on the bottom of the chamber,
producing unacceptable temperature gradients.
Once the heating and sterilization phases have ended,
the cooling phase begins and develops as follows:
the steam+air mixture present in the chamber
is replaced with sterile compressed air at controlled
pressure; this air continues to circulate by virtue
of the action of the fans
cold cooling water circulates in the batteries
of cooling plates located in the two lateral circular
sectors of the chamber.
However, the cooling rate is unavoidably much lower
than in FOW autoclaves, since in this case it is based
on two solid/gas heat exchanges, which notoriously have
a low efficiency. Nonetheless, we try to improve their
efficiency by keeping the air pressure in the chamber
at a high value (within the limits set by the characteristics
of the product) and by maintaining its circulation rate
at a high level.
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Throughout the phases of the program,
air counterpressure in the chamber is adjusted in the
some manner as in FOW autoclaves. The only mechanically
critical point of these autoclaves would be the tightness
of the fan shaft. This problem has been brilliantly solved
in our autoclaves which use magnetically-driven fans which
avoid holes in the chamber and shaft seals.
The pictures above show an autoclave with two peculiarities.
It is a mixed machine, i.e. suitable to run not only counterpressure
programs with steam+air mixture but also satured steam
programs. For this reason it is also equipped with a vacuum
pump and with a sparger in the upper part of the chamber
for the load water spray cooling. Its loading bed is furthermore
at floor level.
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CONSTRUCTION FEATURES
The chamber is cylindrical, usually single-wall, wich
thick insulation and an aluminum-sheet outer casing.
The construction material is class AISI 316 stainless
steel.
Either one or two rectangular doors, inscribed in the
circular cross-section.
These doors may be of two kinds:
laterally sliding and fully automatic
laterally hinged and semiautomatic; the doors
engage and disengage their clamping devices with a transverse
movement produced automatically by a geormotor, but
the opening and closing action relative to the vertical
hinges is manual.
In both cases, the gasket (made of solid silicone rubber)
slides in a special slot formed by numeric-control milling
in the frame of the chamber and it is activated by compressed
air. The gasket and the slot have specially designed
trapezoidal cross-sections to ensure perfect operation
and tightness without requiring lubrication and vacuum
for gasket retraction.
All valves and the entire hydraulic system are made
of stainless steel.
AUTOMATIC LOADING/UNLOADING SYSTEMS
When it is necessary to sterilize large and heavy loads,
it is sensible to resort to palletization systems featuring
automatic handling.
The solution we have perfected for handling is extremely
simple and efficient.
It consists of a loading bench located in front of the
autoclave, where the train of pallets is prepared.
The bench has two rows of free rollers on which the
pallets rest, and it is also provided with an underlying
rod with a rack-like movement which pushes the pallets
into the autoclave. The autoclave is also internally
equipped with two rows of free rollers and therefore
inside the chamber there are no sealed shafts, chains
or gears: this means that all risks of leaks and all
lubrication problems have been eliminated.
Usually, a second bench, arranged in front of the unloading
door of the autoclave, removes the pallets by means
of an extractor rack-roc
PROCESS CONTROL
As all the other sterilizers, also the counterpressure
autoclaves are equipped with the Thema 3 process controller,
specifically developed by our company for monitoring
and controling sterilization processes. Please refer
to the specific brochure for the desciption of this
system.
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| FOW
3 - FOA 3 |
| MODEL |
450 |
720 |
900 |
1080 |
| USEFUL
CHAMBER DIMENSIONS |
| Width
(cm) |
80 |
80 |
80 |
80 |
| Height
(cm) |
80 |
80 |
80 |
80 |
| Depth
(cm) |
130 |
210 |
250 |
310 |
| Capacity
(liters) |
830 |
1350 |
1600 |
1980 |
| Cylinder
(diam. cm) |
118 |
118 |
118 |
118 |
| Oper.
pressure (abs. bar) |
4 |
4 |
4 |
4 |
| Oper.
Temperature (°C) |
128 |
128 |
128 |
128 |
| FOW
4 - FOA 4 |
| MODEL |
1200 |
1440 |
1800 |
2160 |
2700 |
| USEFUL
CHAMBER DIMENSIONS |
| Width
(cm) |
106 |
106 |
106 |
106 |
106 |
| Height
(cm) |
115 |
115 |
115 |
115 |
115 |
| Depth
(cm) |
165 |
210 |
250 |
310 |
370 |
| Capacity
(liters) |
2010 |
2560 |
3050 |
3780 |
4510 |
| Cylinder
(diam. cm) |
158 |
158 |
158 |
158 |
158 |
| Oper.
pressure (abs. bar) |
4 |
4 |
4 |
4 |
4 |
| Oper.
Temperature (°C) |
128 |
128 |
128 |
128 |
128 |
| FOW
5- FOA 5 |
| MODEL |
2160 |
2700 |
3240 |
3600 |
4500 |
5400 |
6300 |
7200 |
8100 |
| USEFUL
CHAMBER DIMENSIONS |
| Width
(cm) |
130 |
130 |
130 |
130 |
130 |
130 |
130 |
130 |
130 |
| Height
(cm) |
150 |
150 |
150 |
150 |
150 |
150 |
150 |
150 |
150 |
| Depth
(cm) |
220 |
260 |
325 |
350 |
430 |
530 |
600 |
680 |
760 |
| Capacity
(liters) |
4300 |
5000 |
6300 |
6900 |
8300 |
10000 |
11700 |
13300 |
14800 |
| Cylinder
(diam. cm) |
200 |
200 |
200 |
200 |
200 |
200 |
200 |
200 |
200 |
| Oper.
pressure (abs. bar) |
4 |
4 |
4 |
4 |
4 |
4 |
4 |
4 |
4 |
| Oper.
Temperature (°C) |
128 |
128 |
128 |
128 |
128 |
128 |
128 |
128 |
128 |
| CRITICAL
COMPARISON |
FOW |
FOA |
| Temperature
uniformity in time |
Very good |
Very good |
| Temperature
uniformity in space |
Very good |
Very good |
| Total pressure
uniformity in time |
Very good |
Very good |
| Counterpressure
management flexibility |
Excellent |
Excellent |
| Consumption
of high-microbiological-quality water |
Yes, modest,
for initial filling |
No |
| Consumption
of tap water for cooling |
Yes, accettable |
Yes, approx.
3 times higher than FOW |
| Consumption
of compressed air |
Yes, accettable |
Yes, acceptable |
| Consumption
of industrial steam |
Yes, accettable |
No |
| Consumption
of ultraclean steam |
No |
Yes, acceptable |
| Condensate
recovery |
Possible and
easy |
Not possible |
| Cooling water
recovery |
Possible, recovered
water is initially very hot |
Possible, recovered
water is initially very hot |
| Autoclave
price |
Acceptable |
Approx. 10%
higher than FOW |
| Total process
duration |
Short |
Approx. 30%
higher than FOW |
| Autoclave
productivity/price |
High |
Approx. 30%
lower than FOW |
| Operating
principle |
Very simple
and straightforward |
More complicated
than FOW |
| Mechanical
construction |
Simple |
More complicated
than FOW |
| Qualification/Validation |
Normal |
Normal |
| Operating
flexibility according to type of load |
Suitable for
any kind of container with the following remarks: |
Suitable for
any kind of container: |
| - upward concavities
collect water |
- upward concavities
collect condensate only |
| - product is
unloaded wet |
- other kind
of container can be unloaded lighty damp |
| - PVC bags
can produce "blushing" phenomena |
- blushing
phenomena of PVC bags are limited |
| Possibility of combination with
saturated steam process |
Possible, but involves significant
and rather expensive contrivances |
Feasible and moderately expensive |
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