A Plant for Solid State Fermentation
Brief description of the invention
The object of the invention relates to a Solid State
Fermentation plant for the production of biomass and/or
metabolites, which shows interesting characteristics as to its
design, implementation and costs are concerned.
Background of the invention
The Solid State Fermentation (SSF) involves the microorganism
growth of different genera, mainly fungi, on humid substrates;
this kind of process has a considerable economic strength for
the production of products in the agro-food and pharmaceutical
industries. Some typical applications of the SSF include
bakery and oven product production, fermented foods, cheeses
and starters for the beer, sausage and compost industry.
The SSF most recent applications include the protein
enrichment of the agro-food residues, the production of
enzymes, organic acids, metabolites and fungi spores. SSF
presents several advantages versus the submerged fermentation
due to its higher substrate concentration, process energy
saving and technology simplicity.
The two SSF main techniques foresee the culture of
microorganisms on a substrate formed by cereals, such as corn,
rice, barley, etc. or on a substrate of a suitable liquid
growth medium absorbed on inert.
Description of the invention
The object of the present invention is a Solid State
Fermentation (SSF) plant which presents interesting
characteristics due to its simple design, implementation and
cost saving.
In particular, the SSF plant of the invention is formed by a
suitable number of transparent plastic bags, scaffoldings, an
air treatment and distribution system and a growth medium
preparation equipment. The plant is also provided with an
usual instrumentation system for the automatic control and
record of all the plant operation parameters (temperature,
pressure, air humidity and flow-rate and safety) .
More specifically, the plastic bag of the plant of the present
invention is made of a suitable transparent plastic material
and is internally, longitudinally divided by a sheet, made of
the same plastic material as the bag, into an upper chamber
and a lower chamber. The longitudinal sheet crossing the bag
has a central porous or micro-perforated zone, which may also
be called porous or micro-perforated baffle.
on the external wall of the bag lower chamber is fixed an air
sterilizing filter which allows the sterilized air to flow
under the porous or micro-perforated baffle. On the external
wall of the bag upper chamber is fixed a metallic nozzle
having a diameter from 1 to 20cm, preferably from 5 to 6cm.
During the fermentation, the metallic nozzle is closed by an
air sterilizing porous plug which allows the air and the
fermentation gases to be discharged from the upper chamber or
to take samples of the growth fermented substrate or to allow
the flame sterile inoculation. Said nozzle is plugged by a
removable filtering and sterilizing plug for microbiology. The
bag is filled with the growth medium in the upper chamber,
over the porous or micro-perforated baffle, ready to be sent
to the sterilization performed by non thermal technologies.
The transparent plastic material, the plant bag is made with,
makes possible a visual control of the fermenting mass from
the outside, characteristic which renders easier to the plant
operator the control of the development of the fermentation
process .
A convenient bag size ranges from about 50x20cm to about
200xl00cm.
The rack for supporting the transparent plastic bag is formed
by a normal scaffolding having shelves of the same size as the
bag and being the vertical distance between each other ranging
from 15 to 80cm, preferably 40cm. The rack is suitable for the
installation of pipes and air distributors.
The air supply and distribution system is formed by a blower,
having a pre-filter on the suction and by an air conditioning
system providing a, flow-rate of from 0.05 to 5L/min per
kilogram of the growth medium, preferably Q.2÷0.8L/min per
kilogram of the growth medium, at a suitable pressure,
preferably from 5-30mbar, more preferably 15÷20mbar.
The system can provide two different types of air: one for the
dry air and one for the humid air.
The air from the blower or from the air treatment flows to two
separate general distribution pipe systems; for dry air and
for humid air. Therefrom minor pipes derive, which may be shut
off by valves (generally one or two for every rack) , from
which pipes derive which are shut off by valves or pliers for
every shelf and therefore for every bag. These last pipes are
connected to the bag filters at the time these are placed on
the shelves to start the fermentation process .
The growth medium preparation equipment is formed by a
jacketed vessel with cover and by a strong, slow mixer, which
can be lifted to allow complete access to the vessel with the
possibility of steam injecting into the substrate mass and
jacket heating while the mixer is on. The preferred growth
medium preparation vessel has the geometrical capacity from
about 0.5 to Im3, a mixer power of 15-20Hp, a hydraulic lifter
of the mixer, so as to leave the vessel totally free and over-
turnable .
Depending from the quantity of the growth medium to be
cultivated one or more transparent plastic bag may be used
and, consequently, may vary the number of scaffoldings used.
The attached drawings are given for better illustrating the
plant of the invention.
Figure 1 represents a perspective view of the transparent
plastic bag of the plant of the invention;
Figure 2 represents a frontal view of the bag of Figure 1
according to the direction of arrow A;
Figure 3 represents the air supplying and distribution system
to the bags of Figure 1;
Figure 4 represents a sketch of the growth medium preparation
of the plant of the invention.
In the above mentioned Figures are shown the components of the
plant which are: the transparent plastic bag (1) divided by a
porous or a micro-perforated baffle (2) into two parts, the
upper chamber (3) and the lower chamber (4), the metallic
nozzles (5) with the air sterilizing porous plug (6) on the
external wall of the upper chamber (3), the air sterilizing
filter (7) on the external wall of the lower chamber (4),
being the metallic nozzle (5) and the sterilizing filter (7)
located in a diagonally opposite position as per in Figure 1;
the dry air line (8), the humid air line (9), the tube/s (10)
connecting the dry air line (8) and the tube/s (11) connecting
the humid air line (9) to the bag or to the bags (1), being
the tubes (10) and (11) preferably made of rubber, various
racks (12) , (13) , (14) and (15), a bag support (16), the growth
medium preparation equipment (17) composed by the jacketed
vessel (18), the mixer (19) and the hydraulic mixer lifter
device (20) .
The growth medium is prepared in the jacketed vessel (18) of
the growth medium preparation equipment (17) while the stirrer
(19) is on and steam injection is provided and then
transferred into the bag (1) over the porous or micro-
perforated baffle (2) where it is indicated by the reference
number (21) in Figure 2. Dry or humid air is supplied through
the pipes (8) and (9), and the rubber tubes (10) and (11) to
the plastic bag (1) through the sterilizing filter (7) . The
air and fermentation gases flow to the atmosphere through the
nozzle (5) provided with the porous sterilizing plug (6) .
The air supply and distribution system is provided by an
appropriate number of valves (22) in order to send, even
contemporarily, dry and humid air to different bags.