[0001] The present invention has as object a plant and a method for pelletizing powder or
granular material providing in particular a process for drying the pellets for eliminating
a water excess existing in the starting material and/or added subsequently to allow
the step of producing the pellets.
[0002] The pellet production involves several technological fields: it is used to make usable
the products which otherwise would be available in forms difficult to be used, such
as powders, granules or even as muds, sewages, organic material, molasses and so on.
[0003] The pellets, small tablets of compressed material, represent a possible use form
of a material characterized by great easiness in treatment, storage and use.
[0004] They are tablets with generally cylindrical shape, with sizes in the order of some
millimetres, with high density and low humidity content, generally lower than 10%.
[0005] Thanks to the substantially granular shape, huge quantities of pellets can be kept
in tanks, made to flow in ducts by gravity or thanks to pushing devices, for example
screw devices, they can be easily stored in sacks, they can be dispersed inside restricted
environments or in the outer environment.
[0006] Thanks to the their compactness, the pellets are self-supporting, they do not release
powders and remain compact even during treatment steps such as transport, storing,
supply and so on.
[0007] A common example of pellets is represented by the organic or organic-mineral fertilisers
which are the result of compressing and drying biological and synthetic raw materials.
[0008] The fertiliser produced in this way is kept and distributed in bags and it can be
easily supplied in the environment by mechanical spreading, without dispersion of
organic powder which could hinder the spreading operation.
[0009] Another example of using the pellets is the one concerning the wood combustion, in
particular for domestic heating. In this case, sawdust, for example the residues of
the wood processing, is compacted in pellets to be able to be used in automatic systems
for supplying fuel in ovens, boilers, stoves.
[0010] Another example of use is represented by animal feed or by the additives for feeding
livestock, wherein various types of organic foods under the form of flours are compacted
in pellets to be able to be distributed, even with automatic systems, in the feeders.
[0011] A last example is represented by the waste treatment, in particular with the purpose
of recycling. In this case, a wide range of waste (for example wood, paper and cartons,
biomasses, organic materials) can be at first minced and broken into small pieces
and then collected in pellets for a greater easiness in storage, transport and use.
[0012] However it is meant that the above-mentioned list of uses is not exhaustive and it
is provided by way of example only.
[0013] The pellets are manufactured by special extruding devices, wherein a mixture under
the form of purée, pulp or of farinaceous type, with a certain humidity content, is
compressed by a mould comprising a plurality of holes, therethrough the mixture is
extruded.
[0014] In the extrusion, a high pressure is exerted which, locally, can reach values in
the order of 1500 atmospheres and which involves even a high heating of the forming
pellet.
[0015] With the purpose of making the extrusion possible, the starting material must have
a humidity content in the order of 25÷30%. If the starting powder and/or granular
material does not represent this humidity content, it must be enriched with water.
[0016] However, at the extruding press outlet the humidity quantity in the pellets is not
compatible with the subsequent treatment and storage steps. In fact, the existing
humidity could easily cause the pellet agglomeration which would vanish the above-described
advantages.
[0017] However, at the extruding press outlet, the pellets must be subjected to a drying
process, aimed at eliminating the water excess. This process requests that the pellet
flow is struck by an air current drying the pellets.
[0018] However, this step is critical as such air current inevitably enriches with powders
and/or micro - powders (fine dust with particles with sizes in the order of 1÷10 µm)
caused by a minimum surface disintegration of pellets, by the friction between and
pellet and by the air current force.
[0019] These powders and micro - powders, if released in the environment, could cause pollution
and cause possible bad odours. Furthermore they would represent a danger if inhaled
directly, above all if the starting material was a potentially toxic material.
[0020] Furthermore, the quantity of powders and fine dust in the environment wherein a plant
for manufacturing pellets is localized is subjected to strict rules limiting the presence
thereof.
[0021] For this reason, the drying apparatus must include a complex system of filters to
depurate the air current outgoing from drying. The filters, whichever type they are,
represent an additional cost for the pelletizing process and request a huge energy
consumption to implement the air circulation.
[0022] Furthermore, although depurated, the release in the environment of the air used for
drying always represents a risk, both for a filtration which eliminates any impurity
with difficulty and for the possibility of a malfunction of the filters.
[0023] On this matter systems are known for cleaning an air flow transporting a dry residue
by means of so-called rain filters, wherein one tries to capture said dry residue
by trapping it in water sprayed in the air flow.
[0024] However, in the known systems, this requires an additional water consumption and
a subsequent disposal of the polluted water, without solving radically the problem
of disposing the air flow in the environment itself.
[0025] The technical problem underlying the present invention is to provide a pelletizing
plant and a related method which allow obviating the drawback with reference to the
known art.
[0026] Such problem is solved by a pelletizing plant as specified above characterized in
that it comprises:
a closed circuit, for the circulation of a drying air flow, wherein a flow of pellets
to be dried is inserted, said closed circuit being constructed so as to have:
- an air flow pumping device;
- an air cooling device;
- a device for condensing the humidity transported by the air flow and for extracting
the resulting water, so as to obtain an air flow with reduced water content; and
- a drying tract, wherein the air flow with reduced water content, intersects said flow
of pellets to be dried.
[0027] The above-mentioned problem is also solved by a pelletizing method as specified above,
comprising the production of an air flow in a closed circuit and the steps of:
● pressurizing said air flow;
● refrigerating said air flow;
● condensing and extracting residual air from the humidity contained in said air flow;
and
● drying a flow of pellets outgoing from an extruding press, by intersecting the flow
of pellets with said air flow downwards said condensing and extracting step.
[0028] The main advantage of the plant and method according to the present invention lies
in allowing the drying of pellets without the fact that the air used to this purposes
is spread in the environment, by making then useless the use of any filter and by
eliminating the risk dispersing in the environment powders, micro-powders, polluting
substances and possible bad odours.
[0029] In fact, said powders or micro-powders remain trapped in the drying closed circuit:
they dissolve or remain trapped in the condensed water. The volatile portion will
reach a certain value of equilibrium in the plant and however will remain confined
in the closed circuit.
[0030] According to a preferred version of the plant and of the related method, the water
recovered by the condensation step is re-entered upwards of the extruding press to
humidify the powder and/or granular material.
[0031] In this way, the residues removed during the drying step cannot in any case dispersed
in the environment and they return to be involved in the pellet-forming step, thus
by allowing a saving of water and starting material.
[0032] The present invention will be described hereinafter according to a preferred embodiment
example thereof, provided by way of example and not with limitative purpose with reference
to the enclosed drawings wherein:
- figure 1 shows a functional scheme of a pelletizing plant according to the invention;
and
- figure 2 shows a schematic and partial view of the pelletizing plant of figure 1.
[0033] By referring to the figures, the plant and the method for pelletizing defined above
will be described by referring to a plant for producing fertilizing pellets of organo-mineral,
dehydrated, cooled and therefore ready-for-package type.
[0034] It is meant however that what described in the specific case could be adapted to
any pelletizing plant, for producing different pellets, for example fuel pellets,
feed, waste to be recycled and so on.
[0035] In this example, the starting material is constituted by a set of raw materials suitable
for producing fertilizers, for example but not exclusively powder nitrogenous material.
[0036] Such raw materials are loaded on dosing hoppers and, by means of an extracting belt,
they are introduced into homogenizing mills.
[0037] In these mills the raw material is mixed so as to reach the requested homogenization
and a water quantity is added thereto so that the whole humidity, in the present example,
reaches a percentage of 8÷10%.
[0038] This step of the plant and of the process is not represented in the figures and it
is of substantially conventional type.
[0039] The so-treated compound is extracted and sent, through a hopper 1, to an extruding
press 2, of conventional type too and composed of rotating cylinders compressing the
compound and they extrude it through suitable holes. The mutual motion of the cylinders
3, 4 and the pressure implemented between the surfaces compressing the compound produces
pellets with small cylinders with standard sizes, with diameter in the order of some
millimetres.
[0040] The pellets produced in this step are hot, due to the effect of compression and extrusion,
and they have high humidity content. They must be then dried in order to be subsequently
packaged without forming lumps.
[0041] According to the processes known in the state of art, the drying process usually
is performed by inletting hot air which eliminates humidity in form of vapour, which
is ejected outside the factory. However, it contains fine dust the density thereof
in the area surrounding the factory has to be kept under control and remain below
levels well defined by the rules in force.
[0042] In the so-described plant, the pellets outgoing from the extruding press 2 are introduced
into a drying chamber 5 through a non-return valve 6. Inside said chamber 5 the pellets
are spread over a series of ring-like conveyor belts 7 or other equivalent transportation
systems, arranged one onto the other one, with the aim of spreading the pellets on
the widest possible surface.
[0043] The belts 7 are arranged one onto the other one, and the pellets pass from to the
other one by fall at the end of each belt 7. In this way a flow of pellets descending
inside the drying chamber 5 is implemented.
[0044] The latter is inserted inside a closed circuit, designated as a whole with 10. To
this purpose, the chamber 5 is crossed by an ascending air flow entering form a lower
door 8 and outgoing from an upper door 9.
[0045] In order to ease the air passage or the drying of pellets, the carpets can have a
weft, of other type of passage, allowing them to be crossed by the air.
[0046] The closed circuit 10 is implemented by a duct 11 connected to said doors 8, 9. Upon
observing the circuit clockwise, it comprises a device 12 for pumping the air flow
which introduces it in an air cooling device, designated as a whole with 13.
[0047] The purpose of the cooling device 13 is to cool down the humid and hot air which
has passed in countercurrent inside the drying chamber 5.
[0048] It also includes the device 14 condensing the humidity transported by the air flow
and extracting the resulting air, so as to obtain an air flow with reduced water content
and with low temperature (3°÷6°C) which, through the duct 11 of the closed circuit
10, is made to run in countercurrent into the hot and humid pellets inside the drying
chamber 5.
[0049] It is meant that the two above-mentioned devices, the cooling and condensing devices,
can physically coincide as in the present example.
[0050] The condensation takes place thanks to the presence of coils crossed by a coolant
properly cooled by a cooling apparatus F. This determines the formation of rain-like
condensate, wherein the impurity particles existing in the air constitute themselves
the first condensation nucleus.
[0051] In this way, at the end of the route, the pellets outgoing from the drying chamber
5 have been cooled and dried, from an extracting door 15.
[0052] On the contrary, in the cooling device 13, the humidity contained in the air extracted
by the chamber 5 gathers inside the condensing device 14. Condensate results therefrom,
containing fine dust in suspension, which is wholly recovered through a recovery line
16 to be then re-introduced upwards of the extruding press 2, thus performing an integration
of the water coming from outside.
[0053] In this way, a considerable saving in the starting material and an increase in the
performance of the producing cycle is obtained, also avoiding to dispose such dried
residue in the environment.
[0054] Said recovery line 16 constitutes a device for extracting condensate in the here
described plant.
[0055] In this way, two virtuous circuits are activated, both closed and therefore without
emissions outwards of fine dust, with the re-utilization of the components in a closed
cycle A and a half-closed cycle B towards the production (figure 1).
[0056] The closed circuit A is the air circuit comprising hot and humid air with powders
between the chamber 5 and the cooling device 13, and cold air between the cooling
device 13 and the chamber 5.
[0057] The half-closed circuit B is the circuit of the water which is extracted from the
condensing device 14, is re-introduced in the extruding press and ends up in the semi-processed
humid and hot pellets, therefrom it is then extracted form the cold and dry air current
which becomes hot and humid.
[0058] By way of example, the main technical features of said circuits are:
cooler yield |
103 kW |
room temperature |
+18 °C |
water temperature (in/out) |
-7/+12 °C |
water flow rate |
15 m3/h |
flow rate of fans |
21600 m3/h |
electric power of fans |
2 x 4 kW |
compressors |
35 kW |
[0059] It is to be noted that the cooling fluid used in the condensing device 14 is water,
in case added with an antifreeze agent. The temperature of the cooling fluid will
be chosen based upon the air temperature in the closed circuit and in particular based
upon the content of air humidity subsequent to the drying step.
[0060] The temperature at the cooling device conveniently will be below the dew-point temperature,
which is function of the absolute humidity.
[0061] It is further meant that the air temperature inside the closed circuit will also
depend upon the outer temperature.
[0062] With reference to the above-described plant, a method for pelletizing powder and/or
granular material is implemented, providing the steps of homogenizing the starting
material and a possible step of adding water to the mixture to get started with the
real pelletizing step.
[0063] The quantity of water to be added obviously depends upon the operating parameters
provided for the extruding press and upon the quantity of water already existing in
the starting material. It is meant then that the added water fills-up the difference
between already existing water and the requested water content for the extruding press
good operation wherein, basically, the water acts as lubricant.
[0064] The extruding step involves a compression of the starting material and a substantial
drawing, with high pressures and localized frictions which determine a general increase
in temperature thereto a limited humidity loss can correspond, however not sufficient
to avoid agglomeration phenomena.
[0065] Therefore, the hot and humid pellets are getting started with a drying process comprising
the production of a drying air flow in a closed circuit.
[0066] The production of such drying air flow comprises a step of pressurizing said air
flow, in order to allow the forced circulation thereof.
[0067] Furthermore, a step of cooling said air flow is provided, wherein there are the condensation
and extraction of water residual from the humidity contained in said air flow.
[0068] The cooled air flow, with reduced humidity content, is got started with the drying
of a flow of pellets outgoing from the extruding press, by intersecting the flow of
pellets with said air flow downwards said condensing and extracting step.
[0069] In the present method embodiment example, the intersection substantially takes place
in countercurrent, inside a drying chamber.
[0070] The water extracted in the condensing step can be re-introduced in said homogenizing
step, obviously if a water addition is requested in said step.
[0071] In this way, the volatile residue which remains trapped in the condensate is got
started again inside the producing cycle.
[0072] It is meant that the extracted water is not sufficient for an adequate lubrication
of the homogenized material and therefore the addition of further water must be then
provided.
[0073] From the method description, it results evident that, apart from the pelletizing
of the organic-mineral fertilizers, it can also be applied to other pelletizing processes,
wherein the quantity of initial humidity of the starting material and the quantity
of the humidity contained in the pellets to get started with packaging are adjusted
during the process implementation.
[0074] In particular, the quantity of initial water depends upon the type of starting material
and it can or cannot request an integration. Such integration, if requested, takes
place with the water extracted from the above-mentioned extracting device, so as to
re-introduce in the manufacturing process the residues trapped in the extracted water.
[0075] Such water is not sufficient, therefore additional water can then be added from any
feeding.
[0076] Therefore, it is possible adapting the method to dry or humid starting materials.
[0077] To the above-described plant and method for pelletizing, a person skilled in the
art, in order to satisfy additional and contingent needs, can introduce several additional
modifications and variants, all however within the protective scope of the present
invention, as defined by the enclosed claims.
1. A plant for pelletizing a granular and/or powder material, wherein said material is
possibly homogenized and subsequently extruded in order to obtain pellets to be dried,
characterized in that of comprising:
a closed circuit (10), for circulating a drying air flow, wherein a flow of pellets
to be dried is inserted, said closed circuit being created so as to have:
• an air flow pumping device (12);
• an air cooling device (13);
• a device (14) for condensing the humidity transported by the air flow and for extracting
(16) the resulting water, so as to obtain an air flow with reduced air content; and
• a drying tract (5), wherein the air flow with reduced water content intersects said
flow of pellets to be dried.
2. The plant according to claim 1, wherein said drying tract is constituted by a drying
chamber (5) wherein the flow of pellets and the air flow are in countercurrent.
3. The plant according to claim 1 or 2, wherein the water extracted with said extracting
device (16) is mixed with the starting material to get started with the extrusion.
4. The plant according to claim 3, wherein the extracted water is integrated with additional
water coming from any feeding.
5. The plant according to claim 2, wherein the drying chamber (5) is fed with pellets
through a non-return valve (6).
6. The plant according to claim 2 or 5, wherein, inside said drying chamber (5), the
pellets are spread on a series of ring-like conveyor belts (7) or on an equivalent
transport system, arranged one onto the other one, the pellets passing from one to
the other one by fall at the end of each belt (7) so as to implement a flow of pellets
descending inside the drying chamber (5).
7. The plant according to claim 6, wherein the belts (7) or the equivalent transport
system have a weft and/or passages allowing them to be crossed by the air.
8. A method for pelletizing an initial granular and/or powder material, comprising a
step of extruding said starting material and for producing a flow of pellets to be
dried, wherein the generation of an air flow in a closed circuit is provided and the
steps of:
● pressurizing said air flow;
● refrigerating said air flow;
● condensing and extracting residual water from the humidity contained in said air
flow; and
● drying said flow of pellets, intersecting the flow of pellets with said air flow
downwards said condensing and extracting step.
9. The method according to claim 8, wherein the step of homogenizing the starting material
and a step of adding water to the mixture to get started with the pelletizing step
are provided.
10. The method according to claim 8 o 9, wherein, the intersection between flow of pellets
and air flow takes place substantially in countercurrent, inside a drying chamber
(5).
11. The method according to claim 9, wherein the water extracted in the condensation step
is re-entered during said homogenization step.
12. The method according to claim 11, wherein in the homogenization step the addition
of additional water is provided based upon the humidity contained in the starting
material, upon the one requested in the extrusion step and the one requested in the
pellets at the end of the method.