STATE OF THE ART
[0001] In the recent years, industrial countries devoted particular attention to problems
concerning the handling of polymeric wastes.
[0002] The specific chemical-physical characteristics aimed all the efforts of industrial
operators to the recycling of such materials that in some cases can be considered
as economical resource. In fact, recycled polymer can be used in energy production
in different industrial and/or civil sectors as: cement factories, lime factories,
paper factories, power station, incinerators, foundry district heating etc. In all
cases, relating to different specific application, it is important to optimise the
air/fuel ratio to increase the combustion efficiency and minimize pollutants in flue
gas.
[0003] The control of the fuel flow rate is particularly difficult in actual systems mainly
due to granulometric and morphologic characteristics of polymeric materials.
DESCRIPTION
[0004] The present invention refers to the device and related equipments for supplying a
solid polymeric material used as fuel in most systems for energy production and/or
for thermodestruction.
The device is designed to operate using of polymeric combustible coming from a specific
production or from industrial scrap, plastic recycling after suitable pre-treatments.
The combustible, thermoplastic or thermosetting polymeric material, can be used as
a continuous element of a suitable size and shape ( circular, square cross-section).
The continuous element, relating to operating regimes of the combustor and to chemico-physical
characteristics of the material used, can be used or as discrete bars (of suitable
length) or as continuous wire (in roll) or suitably thermoformed with a dedicated
apparatus before the supply of the combustible to the device.
The feeding device of the polymeric combustible is made by specific injectors that
are generally formed by two sections: the first one to feed the material, the second
one to control the temperature and the physical state of the combustible.
The combustible flow rate to the combustion chamber, i.e. the feeding velocity is
controlled by mechanical and/or pneumatic system.
The feeding device can utilise two type of combustible material:
1. Homogeneous (Fig. 1,a)
2. Charged (Fig. 1,b,c)
Homogeneous
[0005] The homogeneous material (fig. 1, a) is made by polymers of the same type or by a
blend of different type with a chemical and/or a mechanical cohesion of polymer particles.
This kind of material can be divided in two categories: thermoplastic or thermosetting.
Charged
[0006] The charged material can be produced by a homogeneous polymer adding a suitable amount
of solid and/or liquid chemical compounds able to enhance the following combustion
limiting the emission and the production of noxious compounds. The additives can be
blended homogeneously in the polymer matrix (Fig. 1,b) or located in one or more cavities
inside of the continuous element (Fig. 1 c).
[0007] The material, homogeneous or charged, of suitable size and shape is feed into combustion
chamber by the devices illustrated in fig. 2 and fig. 3 referred as injector 1 (
I1), and injector 2 (
I2).
The injector I1 can be used with thermoplastic polymers obtaining a supply of the
polymeric material to the combustor in plastic, liquid or gaseous state.
As shown in figure 2 the injector
I1 is designed with a guide chamber (1) in order to obtain a suitable supply of the
material to the nozzle; the feed of solid polymer is obtained by means the device
(2). The injector I1 is equipped with the section (3) to control polymer temperature
and hence for supplying to combustors the material in solid, or liquid or gaseous
state in relation to the relative temperature level and optimising the combustion
process. At the end of the section (3) is located a converging zone in which a suitable
amount of liquid polymer, due to a higher temperature level, control the pneumatic
sealing between the material and the injector. The complete pneumatic sealing and
the pneumatic uncoupling between the combustion chamber and the injector is obtained
by a security valve. This valve preserves the feeding device by possible over-pressure
phenomena that can be produced in the combustion chamber (5).
[0008] The injector
I2 can work with both solid or liquid polymer.
As shown in figure 3, the injector
I2 has a guide chamber (6) with, at the end, a heating/cooling device (7) to control
the combustible temperature.
The sealing between the combustible bar and the injection device is obtained by a
suitable sealing system (8).
The injector type has to be optimised relating to specific combustor. In the following,
explanatory examples are shown.
Example N°1
Bubbling Fluidised Bed Combustor, Circulating Fluidised Bed Combustor
[0009] Both injector types can be used with these combustors. Combustible temperature is
controlled at a level in order to supply to the fluidised bed polymer droplets, by
means the injector
I1, or solid polymer, by means the injector 12. The material burns in contact with the
powder at high temperature. In this case, in respect to actual feeding devices, a
higher control of the polymer flow rates can be obtained, avoiding the undesired under/overfeeding
of combustible to the combustor. This control can be obtained controlling the feeding
velocity of solid polymer bar and optimising the nozzle size and shape in relation
to process conditions.
Example N°2
Boiler Combustor
[0010] The injector
I1 is used in this case. A gas of polymer is fed to the combustor. The nozzle temperature
must be controlled at level so high to obtain the gasification of polymeric combustible.
The mixing of this polymeric gas with the air allows to obtain a very controlled and
efficient combustion with a very low production of combustion products. The polymeric
flame can be activated for example by a driving-flame or by an electric igniter.
1. Device to supply polymeric material to combustor for energy production.
2. Device, claimed at n° 1, to supply plastic material to thermodestruction plants.
3. Supplying system, as described in previous claims, to supply thermoplastic polymer.
4. Supplying system, as described in previous claims, to supply thermosetting polymer.
5. Supplying system, as described in previous claims, to supply polymeric material as
a continuous element of suitable size and shape.
6. Supplying system, as described in previous claims, to supply polymeric material as
bars of suitable length, size and shape.
7. Supplying system, as described in previous claims, provided with a thermoforming device.
8. Supplying system, as described in previous claims, to supply polymeric material as
continuous wire in roll.
9. Supplying system, as described in previous claims, using specific injectors to obtain
a controlled supplying of polymeric combustible.
10. Injectors, as described in claims n° 9, with two different sections. First one to
feed the continuous combustible elements and control the combustible flow rate; the
second one to control the physic characteristics of polymeric combustible by means
of the control of the operating temperature of the continuous elements.
11. Supplying system, as described in previous claims, to supply homogeneous and charged
polymeric material.
12. Supplying system, as described in previous claims, to supply at combustion chambers
homogeneous polymeric materials of similar chemical structure or blends of polymeric
materials with a suitable chemical and/or a mechanical cohesion of polymer particles
to form a continuous element.
13. Supplying system, as described in previous claims, to supply at combustion chambers
charged polymeric material, i.e. homogeneous polymeric materials charged with solid
or liquid compounds able to enhance the combustion and to limit the production of
noxious compounds during combustion process.
14. Supplying system, as described in previous claims, to supply at combustion chambers
charged polymeric material of thermoplastic type or thermosetting type.
15. Supplying system, as described in previous claims, that can be equipped by two different
type of injectors: injector I1 and injector I2 respectively shown in figure 2 and figure 3.
16. Supplying system, as described in previous claim n° 15, that can use injector I1 with thermoplastic or thermosetting polymers.
17. Injector, as described in claims n° 15 and n° 16, that allows the supply of polymeric
combustible in solid, liquid and gaseous phase.
18. Supplying system, as described in previous claim n° 15, that can use injector I2 with thermosetting polymers.
19. Injector, as described in claims n° 15 and n° 18, that allows the supply of polymeric
combustible in liquid and gaseous phase.
20. Supplying system, as described in previous claims, that can be used to supply polymeric
material to different type of combustor, i.e.: Bubbling Fluidised Bed Combustors,
Circulating Fluidised Bed, Heating Boiler Combustors, Boiler Combustor for energy
production.