IT202000032600A1 - Method and plant for the disposal of waste consisting of plastic materials or biomass, and of all organic materials that contain carbon in their molecules - Google Patents

Description

Description of the Industrial Invention entitled:

Method and plant for the disposal of waste consisting of plastic materials or biomass, and of all organic materials that contain carbon in their molecules

The present invention relates to a method and plant for the disposal of solid waste, consisting of plastic materials or biomass, and liquids, particularly consisting of vegetable oils and waste fats, as well as waste of all organic materials that contain carbon in their molecules.

Waste disposal is a serious problem, as ? more and more difficult to find areas to be used for landfill and? incineration has a high cost and, if not done correctly, can? give rise to environmental pollution.

Treatment plants have established themselves, known as waste-to-energy plants, which use plastic materials as fuel to produce heat and also biomass treatment plants which, through fermentation, produce fuel gas.

In a first preferred embodiment thereof, the present invention proposes a new procedure for the disposal of plastic materials, biomass and waste vegetable oils and fats, which allows fuel gas to be obtained, through a pyrolysis treatment.

The present invention therefore proposes a method and systems for implementing said method as claimed in the respective independent claims.

The method essentially consists in subjecting the solid and liquid waste to be disposed of to a pyrolysis treatment which allows the extraction of synthesis fuel gas (syngas), obtaining an inert residue which does not give landfill disposal problems.

In this embodiment, the plant substantially comprises:

? a first section in which the pyrolysis of the waste materials takes place and synthesis gas (syngas) and residual ash are produced;

? a second section in which the fraction pi? light of said ashes, i.e. the coal or carbon black powder which is transported by the syngas, is separated from said syngas;

? a third section in which the fractional distillation of the pyrolysis products takes place, obtaining high-boiling hydrocarbons, i.e. a bituminous residue (tar);

? a fourth section in which the bituminous residue of said fractional distillation is recycled, for a further treatment, said bituminous residue being able to be mixed with said liquid waste; and

? a fifth final emergency section, which will include, in addition to the safety pumps which will intervene automatically in the event of a system failure, all the safety systems.

The pyrolysis chamber? substantially constituted by a special steel tube heated and equipped with a mechanized system for the movement and for the controlled advancement of the solid mass to be subjected to the pyrolysis treatment. The pipe ? externally insulated with ceramic fabric and, by means of a motor-reducer group, it is slowly turned around its own axis.

A characteristic of the plant consists in the fact that ? energetically self-sufficient, as it uses part of the combustible gas produced to feed an endothermic engine which drives an alternator which supplies the electricity used to heat the pyrolysis chamber and to operate all the devices necessary for the operation of the plant.

The use of the method and of the plant according to the invention finally allows to transform the solid and liquid waste into a combustible gas and into inert residues. Part of the combustible gas is used to produce the energy necessary for the functioning of the entire plant, while the residual inert fraction, with a much smaller volume than that of the initial mass of waste, can be disposed of in landfills without particular problems, both for the reduced quantity? of these ashes, both because? they are not polluting.

In a second preferred embodiment, the present invention relates to a method and to an industrial plant for the production of methane gas from materials containing organic carbon.

The plant and the method are capable of gasifying all organic materials, essentially realizing a new type of slow wet pyrolysis in an electromagnetic field and without any emissions into the atmosphere.

Pyrolysis? a process of thermochemical decomposition of the organic substance without external oxygen supply which occurs solely due to the effect of temperature.

The operation of the plant and of the method of this embodiment is based on the principle that when a molecule is placed in an electric field it orients itself according to its dipole and, if the electric field is repeatedly reversed, the molecule ? forced to reposition itself at each reversal of the field and this causes a heating of the molecules all the more? efficient as much as ? close to the resonance frequency of the molecule, but heating still occurs even when the frequencies are different from the resonance ones.

Also in this embodiment, the plant? consisting of five sections and is initially based, in the first sector, on the heating of the molecules within an electric field, until their splitting with the formation of a synthesis gas (syngas) mainly composed of CO-CO?-H?-O ?; subsequently, in the second section, the cylinder of the first section acts as a directional antenna due to the effect of the induced electromagnetic field, the molecular disorder generated by the temperature undergoes an energetic contribution made by the radiofrequency waves and the components of the syngas are strongly ionised, interacting with the superheated steam and create new ordered structures which are addressed by the PLC control of the radio frequency originating predominantly CH?. The plant? contained in a Faraday cage which isolates it from the outside.

The main feature of the plant, in addition to not having any emissions into the atmosphere, consists in the fact that ? energetically self-sufficient as it uses a part of the gas produced to feed an endothermic engine or a turbine which, by activating an alternator, supplies the electrical energy used to heat the pyrolysis chamber and to activate all the devices necessary for the functioning of the plant.

The invention will come now described, by way of non-limiting example, according to a preferred embodiment and with reference to the attached fig. 1, which shows the functional scheme of the pyrolysis plant.

With reference to fig. 1, with (1) ? indicated is a pyrolysis plant, according to a first embodiment of the invention, heated with high-frequency currents. Said pyrolysis plant (1) comprises: ? a first section (100), in which the pyrolysis of the waste materials takes place, the synthesis gas (syngas) is produced and the residual ash from the treatment is discharged;

? a second section (200), in which the fraction pi? light of said ashes (coal dust or carbon black) which is carried by the syngas, is separated from said syngas;

? a third section (300), in which the fractional distillation of the pyrolysis products takes place, obtaining high-boiling hydrocarbons or bituminous residue, (tar);

? a fourth section (400), in which the bituminous residue of said fractional distillation is recycled, for a further treatment; and

? a fifth final emergency section (not shown): this final section will include, in addition to the safety pumps which will intervene automatically in the event of a system failure, all the safety systems.

Said first section (100) comprises a cylinder (2), or pyrolysis chamber, rotating around its own axis, externally provided with insulation, for example in ceramic fibre. In the cylinder? welded Archimedean screw fins (3) with surface hardened by nitriding.

The cylinder (2) ? placed in rotation by a first motor-reducer unit (4) and ? internally heated by heating means (5), in such a way as to bring the solid mass to be pyrolysed to a temperature of 680?750?C.

According to a preferred embodiment, the internal diameter of the pyrolysis chamber (2) will be preferably between 650 and 950 mm, while the length sar? preferably between 6000 mm and 8000 mm, with a rotation at one speed? for example between 1 and 3 rpm. Furthermore, said heating means (5) comprise two induction generators (6) with variable radio frequency between 1.5 kHz and 2.5 kHz and with a power of between 80 and 120 kW each, each of which ? connected to a coil (7), inside which the pyrolysis cylinder (2) rotates slowly. The two coils transmit the high-frequency induced current created by the two generators in such a way that the cylinder (2) becomes the seat of parasitic currents which heat it by the Joule effect.

Temperature control? carried out by means of two laser probes (not shown) placed at the entrance and in the middle of the pyrolysis chamber (2). The two control points each consist of three sequential survey points.

Does the loading of the cylinder (2) take place at the first end? (2a) of the cylinder (2), by means of a hopper (8) which feeds a screw feeder (9) rotated by a second motor-reduction unit (10).

The material is loaded at the inlet of the pyrolysis chamber (2). If the waste to be treated ? solid is first shredded into pieces of about 1 cm in size and loaded by means of the auger (9) with a compression ratio preferably from 1:150 to 1:250 and with speed? adjustable. What if the refusal? liquid, is loaded into the recycling section (400), as better specified below.

The material loaded into the hopper (8) and inserted under pressure by the auger (9), reaches inside the cylinder (2) whose rotation, combined with the Archimedean screw (3), pushes it towards the second end. (2b) of the cylinder (2).

Along the way along the cylinder (2), at a temperature of 680?750?C, the solid waste, mainly made up of plastic materials such as polyethylene, polypropylene, ABS, PET, polystyrene, polyurethanes or biomass (wood, sewage sludge, straw of rice etc.), undergoes pyrolysis producing solid and gaseous compounds. The gaseous fraction, called syngas, comprises a mixture of H2, CO, CO2 CH4 (volatile fraction at room temperature) and carries high-boiling hydrocarbons, oxygenated products of various molecular weights in the form of vapor and carbon powder (carbon black), while the solid includes quantity extremely low in residual ash.

Through an opening (11), the syngas enters a stilling chamber (12), while the residual ash is discharged, through a duct (13), into a container (14).

The second section (200) comprises said stilling chamber (12) from which the syngas is conveyed, through a first duct (15) and a second duct (16), towards a first cyclone (17) and, respectively, a second cyclone (18). Inside said cyclones (17) and (18), the syngas is treated so as to complete the separation from the coal dust (carbon black) it carried, said dust being discharged through a lower opening (17a, 18a) of said first and second cyclone (17, 18), while from the upper part (17b, 18b) the syngas is released so? cleaned of carbon black.

The third section (300), in which the fractional separation of the pyrolysis products takes place, comprises a fractional distillation column (19) composed of various superimposed elements equipped with condensation plates and a cooling coil with regulation of the quantity? of water necessary to maintain each module at the condensation temperature of the high-boiling mixtures that leave so? the syngas. All the condensed high-boilings are carried to the bottom of the column.

The syngas coming from the cyclone separators (17) and (18) enters the lower part of the fractional distillation column (19) through the ducts (20) and (21). In column (19) the volatile fraction of the syngas separates from the high-boiling hydrocarbons, which form said bituminous residue (tar) and comes out from the upper outlet (22), while from the lower outlet (23) said high-boiling hydrocarbons come out. The syngas is conveyed towards a blower (not shown) which creates a slight depression in the pyrolysis chamber (2) and sends the syngas towards the basic and acid washing columns (not shown).

Cooling water is passed through a duct (24), which enters the upper part of the column (19), said inlet being controlled by a valve (25) and an electronic meter (not shown). The water then passes through a coil (26) and exits, in the form of superheated steam, from a duct (27).

In the fourth section (400) the recirculation of the outgoing high-boiling hydrocarbons takes place, through the duct (23), from the lower part of the fractional distillation column (19), and of the coal powder (carbon black) extracted by the separator cyclones (17) and ( 18) placed at the exit of the still room (12).

Said fourth section (400) comprises a pump (28) which introduces said high-boiling hydrocarbons into a turbomixer (29), operated by a third motor-reduction unit (30), the flow of said high-boiling hydrocarbons being regulated by a valve (31) .

The carbon black coming from the cyclones (17) and (18) is introduced into the turbo-mixer (29) through a duct (32), the flow of said carbon black being regulated by a valve (33).

Through a duct (34), liquid waste (vegetable oils and waste fats) are also introduced into the turbo-mixer (29), said liquid waste being introduced into a hopper (35) and their flow being regulated by a valve (36) .

In the turbo-mixer (29) an emulsion is produced which, traveling through a duct (37), reaches a pump (38) which introduces it into the pyrolysis chamber (2) through a duct (39). Through a duct (40), the superheated steam leaving the fractional distillation column (19) is introduced into the pyrolysis chamber (2) through the duct (27), the steam flow being regulated by a valve (41).

The turbo-mixer (29) ? capable of intimately mixing the carbonaceous product that comes out of the separating cyclones and the tar extracted at the base of the fractional distillation column (19). Said mixing is reintroduced to the inlet of the pyrolysis chamber together with the superheated steam coming from the coils of the fractional separation column. The quantity? of steam ? variable between 10% and 15% by weight of the waste loaded at the inlet of the pyrolyzer. This variation? attributable to the nature of the treated waste. This mixing becomes very efficient with the addition of waste vegetable oil, inserted in the hopper (35), coming from differentiated collection, as it has excellent oil properties. dissolving properties of hydrocarbons, even at high concentrations.

The percentage of oxygen present in the pyrolysis chamber? continuously controlled and recorded by an analytical instrument such as SYN 100 capable of also verifying the percentage of CO, CO2, H2 and CH4 in the syngas produced. To avoid both syngas leaks and oxygen infiltrations in the pyrolysis chamber, the feeding of the solid waste is ? carried out with said auger (9) at high compaction pressure and preheated to a suitable temperature (depending on the type of waste) to allow the formation of a plug such as to guarantee the tightness of the system against the entry of air and therefore of oxygen into the chamber pyrolysis (2). Between the loading hopper and the auger ? a rotary valve has been inserted to avoid infiltration of air and therefore of oxygen harmful to the pyrolysis process.

The pyrolysis chamber (2) ? maintained in slight depression by said blower which sends the syngas towards the basic and acid washing columns, said depression being equal to about 0.7 mbar less than the external pressure.

In case of emergency, the syngas produced, after washing, is started with an emergency torch, the induction generators are turned off and the pyrolysis chamber is washed with nitrogen gas.

According to a further preferred embodiment, the system of the invention substantially comprises:

- a waste feeding system (not shown);

- a first section (100) operatively connected to the waste feed system and consisting of a concentric bimetallic cylinder (2) equipped with an Archimedean screw (3), externally insulated and slowly rotating around its own axis;

- the cylinder (2) ends in a second section (200) in which the thermochemical reactions are completed, and the smallest fraction? light of the reaction is separated from the ashes and transported by the syngas into a third section (300) where the cooling and separation of the syngas from the high-boiling products of pyrolysis and from the bituminous residue as well as? from residual carbon;

- a fourth washing and cleaning section (400) into which the syngas enters, is washed and cleaned, and is then sent for use; and

- a fifth final emergency section (not shown), said final section comprising, in addition to the safety pumps which will intervene automatically in the event of a system failure, all the safety systems.

In particular, according to the operation of the inventive plant, the shredded solid material contained in a silo is sent to the loading section (8) equipped with a rotary valve and by means of an auger (9) rotated by a gear motor unit, the material is pressed and sent in the cylinder together with a small quantity? of water that is injected by means of a pump that inietter? if necessary also the liquid waste in the first section.

The material arrives inside the cylinder (2) equipped in the initial part with a scraping system able to prevent the formation of lumps. The rotation of the cylinder (2), achieved by means of a gearmotor unit, pushes the material towards the opposite side of the chamber, thanks to the Archimedean screw (3) contained inside, and, during the journey (300 mm each revolution of the cylinder), all the organic part is transformed into syngas leaving on the bottom of the cylinder (2) the inert ashes and any metals contained in the fed waste which, transported by the Archimedean screw (3), will reach the end of the cylinder (2) and they will fall to the bottom of the second section (200).

The first section (100) comprises a reactor heated by two or more? generators (6) of induced currents of adequate power and with a frequency between 1.5 and 5 KHz so that the cylinder becomes the seat of parasitic currents which heat it by the Joule effect and will bring the temperatures inside the reactor between 650 and 750 ?C where the pyrolysis process takes place.

The generators (6) are each connected to a coil (7) inside which the cylinder (2) rotates with a speed? determined by the PLC and calculated by the PLC according to the transformation times of the single matrices introduced.

According to this preferred embodiment, the cylinder (2) will have a diameter between 1200 and 1500 mm and a length between 9 and 12 m, sar? equipped with a system controlled by a gear motor suitable for its rotation as well as a system suitable for absorbing expansion due to temperatures.

The cylinder (2), in its extremities?, sar? isolated with a packing housed in a hollow and held under pressure by a series of springs and will have? otherwise? a second nitrogen gas safety isolation system.

Inside the cylinder (2) there is a continuous control of the temperatures by means of thermocouples and laser probes as well as a control of the internal pressures which, by means of a system of vacuum pumps, keeps the cylinder (2) and the chamber calm (12) final to a slight depression (about 0.7 mbar) with respect to the external atmospheric pressure, in order to prevent any risk of explosion.

The cylinder (2) and the heating (5) and motion and control systems are placed inside a Faraday cage (not shown) to insulate the outside from the internal induced currents.

The syngas from the cylinder (2) is sent to the second section (200) consisting of a stilling chamber (12) where the thermochemical reactions induced by the radiomagnetic waves take place and the syngas and the smaller fractions read separate from the ashes.

The chamber of calm or ionic copula (12) ? equipped with a screw system for the extraction of the ashes. The augers controlled by PLC remain constantly full of ash which acts as a stopper to prevent the gas from escaping and the outside air from entering; in the final part they will still be equipped with a one-way safety valve.

The syngas is then conveyed to a third cooling and distillation section (300) to be separated from the condensable part and the solid part by means of a distillation column (19) and a centrifugal separator (17, 18). This section (300) will be? also equipped with a refrigeration system or an ORC system for the recovery and transformation of heat into energy. The centrifugal separator (17, 18) will divide? the condensed and solid products from the cooling waters, to then send the condensed and divided products at the beginning of the cycle for a second distillation; or, the separated products will be stored for an industrial use of the same.

The syngas cooled below 80?C sar? sent to a fourth washing section (400) which, by means of two cooling towers (not shown) containing a mixture of water, the first weakly acidic and the second weakly basic, will provide, in addition to further cooling of the syngas which is in a stage of completion of the catalysis process, to do s? that the PH remains between the values of 6 and 7 throughout the process. Any condensed high-boiling hydrocarbons will be separated from the water by means of centrifugal separators and sent back to the beginning of the cycle. Subsequently the gas passes into an activated carbon filtration column to lose humidity; in addition to activated carbon, this section (400) will be? equipped with a filtering system pushed to eliminate any formation of any pollutants present.

Will the gas be then pushed by means of pumps towards use.

As regards the fifth final emergency section including, in addition to the safety pumps which will intervene automatically in the event of a system failure, all the safety systems, in the event of an emergency, the syngas produced, after washing, is sent to a emergency; the induction generators (6) are switched off automatically and the pyrolysis chamber (100) and the stilling chamber (12) are purged with a nitrogen gas.

This security section also includes? an emergency connection system equipped with appropriate valves able to convey the gas of the pyrolysis chamber (100) towards the emergency torch in case of failure.

The fifth final section also includes? a plant for the production of nitrogen by separation and the relative nitrogen storage tank.

The invention? been described, for illustrative and non-limiting purposes, according to a preferred embodiment. The expert technician of the sector can find numerous variants, all falling within the scope of protection of the attached claims.

Claims (15)

1. Pyrolysis plant for the treatment of solid and liquid waste, including: ? a first section (100), suitable for carrying out said pyrolysis of said solid and liquid waste materials, said pyrolysis producing synthesis gas, syngas, and residual ash; ? a second section (200) able to carry out the separation of the fraction pi? light of said ashes, carbon powder or carbon black, from said syngas, said fraction pi? light being carried by the syngas; ? a third section (300), suitable for carrying out the fractional distillation of said syngas, obtaining the separation of the volatile fraction of said syngas from a bituminous residue, tar; ? a fourth section (400), able to carry out the recycling of the bituminous residue of said fractional distillation, for a further treatment; and ? a fifth emergency final section, said final section comprising, in addition to the safety pumps which will intervene automatically in the event of a system failure, all the safety systems. 2. Pyrolysis plant according to claim 1, characterized in that said first section (100), able to carry out said pyrolysis of said solid and liquid waste materials, comprises a cylinder (2), or pyrolysis chamber, rotating around the own axis and equipped with: ? external insulation; ? means suitable for causing, by means of said rotation, the advancement of the material contained in said cylinder (2), said means suitable for causing, by means of said rotation, the advancement of the material contained in said cylinder (2), comprising an Archimedean screw (3); ? means of loading solid waste positioned at the first end? (2a) of the pyrolysis cylinder (2); ? heating means (5), said heating means (5) comprising at least one radiofrequency induction generator (6), each of said generators (6) being connected to a coil (7), inside which said pyrolysis cylinder ( 2) slowly rotates said coil (7) transmitting the high-frequency induced current created by said at least one generator (6) so that the pyrolysis cylinder (2) becomes the seat of parasitic currents which heat it by Joule effect; ? means for making said cylinder (2) rotate. 3. Pyrolysis plant according to claim 2, characterized in that said means for rotating said cylinder (2) comprise a first gearmotor unit (4), and said solid waste loading means, positioned at the first end? (2a) of the pyrolysis cylinder (2), comprise a screw feeder (9), fed by a hopper (8) and rotated by a second motor-reduction unit (10). 4. Pyrolysis plant according to claim 3, characterized in that said auger (9) feeds said solid waste with a compression ratio of approximately 1:200 and ? pre-heated to a suitable temperature, depending on the type of waste, to allow the formation of a cap to prevent both syngas leakage and oxygen infiltration into the pyrolysis chamber (2). 5. Pyrolysis plant according to claim 1, characterized in that said second section (200), suitable for carrying out the separation of the smaller fraction? of said ashes, coal powder or carbon black, from said syngas, comprises a calming chamber (12) in which the syngas coming out of said pyrolysis chamber (2) is collected, at least one duct (15, 16) being provided to convey said syngas towards at least one cyclone (17, 18) inside which the syngas is treated so as to carry out the separation from the coal dust (carbon black) transported by said syngas, said dust being discharged through a lower opening ( 17a, 18a) of said at least one cyclone (17, 18), while from the upper part (17b, 18b) the syngas is let out so? purified. 6. Pyrolysis plant according to claim 1, characterized in that said third section (300), suitable for carrying out the fractional distillation of said syngas, comprises a column (19), in which are provided: ? ducts (20) and (21), positioned in the lower part of said column (19), through which the syngas coming from said separator cyclones (17) and (18) enters; ? an outlet (22), positioned in the upper part of said column (19), from which the syngas comes out after separation from the bituminous residue (tar), said syngas being conveyed towards a blower capable of creating a slight depression in the pyrolysis chamber and to send the syngas towards washing columns; ? an outlet (23), positioned in the lower part of said column (19), from which said bituminous residue comes out; wherein said fractional distillation column (19) further comprises a duct (24), which enters the upper part of said column (19), in which cooling water is passed, said water passing through a coil (26) and coming out, in the form of superheated steam, from a duct (27). 7. Pyrolysis plant according to claim 1, characterized in that said fourth section (400), suitable for recycling the bituminous residue of said fractional distillation, comprises: ? a turbo-mixer (29), operated by a third motor-reduction unit (30), into which said bituminous residue is introduced; ? a duct (32), through which the carbon black coming from the cyclones (17) and (18) is introduced into the turbo-mixer (29); ? a duct (34), through which liquid waste (vegetable oils and waste fats) is introduced into the turbo-mixer (29); wherein, in the turbo-mixer (29), an emulsion is produced which is introduced into the pyrolysis chamber (2); and wherein said fourth section (400) further comprises a duct (40) through which the superheated steam coming from the fractional distillation column (19) is introduced into the pyrolysis chamber (2), through said duct (27). 8. Pyrolysis plant for the disposal of waste consisting of plastic materials or biomass, and of all organic materials which contain carbon in their molecules, said plant comprising: ? a waste feeding system; ? a first section (100) operatively connected to the waste feed system and consisting of a concentric bimetallic cylinder (2) equipped with an Archimedean screw (3), externally insulated and slowly rotating around its own axis; ? a second section (200) in which the cylinder (2) ends, in said second section (200) the thermochemical reactions are completed, and the pi? light of the reaction being separated from the ashes and transported by the syngas in ? a third section (300) in which the cooling and separation of the syngas from the high-boiling products of pyrolysis and from the bituminous residue as well as? from residual carbon; ? a fourth washing and cleaning section (400) into which the syngas enters, is washed and cleaned, and then sent for use; and ? a fifth emergency final section, said final section comprising, in addition to the safety pumps which will intervene automatically in the event of a system failure, all the safety systems. 9. Pyrolysis plant according to claim 8, characterized in that the first section (100) comprises a reactor heated by two or more? generators (6) of induced currents with a frequency between 1.5 and 5 KHz so that the cylinder becomes the seat of parasitic currents which heat it by the Joule effect and will bring the temperatures inside the reactor between 650 and 750 ?C at which the pyrolysis process, said generators (6) being each connected to a coil (7) inside which the cylinder (2) rotates with a speed? determined by the PLC and calculated by the PLC according to the transformation times of the individual dies introduced, said cylinder (2) having a diameter between 1200 and 1500 mm and a length between 9 and 12 m, will be? equipped with a system controlled by a gearmotor suitable for its rotation as well as a system suitable for absorbing expansion due to temperatures, said cylinder (2), at its ends, being insulated with packing housed in a hollow and kept under pressure by a series of springs and will have? otherwise? a second nitrogen gas safety insulation system, inside the cylinder (2) with continuous temperature control by means of thermocouples and laser probes as well as internal pressure control which, by means of a system of pumps vacuum, keeps the cylinder (2) and the final stilling chamber (12) at a slight depression, of about 0.7 mbar, with respect to the external atmospheric pressure, in order to prevent any risk of explosion, said cylinder (2) and the heating (5) and movement and control systems being placed inside a Faraday cage to isolate the outside from the internal induced currents. 10. Pyrolysis plant according to claim 8, characterized in that the second section (200), adapted to receive the syngas from the cylinder (2), is? constituted by a chamber of calm (12) where the thermochemical reactions induced by the radiomagnetic waves take place and the syngas and the fractions more? read are separated from the ashes, called stilling chamber or ion copula (12) being equipped with a system of augers for the extraction of the ashes, the augers controlled by PLC remaining constantly full of ash which acts as a stopper to prevent the leakage of gas and the entry of external air, in the final part being equipped with a one-way safety valve. 11. Pyrolysis plant according to claim 8, characterized in that the third section (300) for cooling and distilling the syngas ? designed to separate the syngas into a condensable part and a solid part by means of a distillation column (19) and a centrifugal separator (17, 18), said third section (300) also being equipped with a refrigeration system or a ORC system for recovery and transformation of heat into energy, the centrifugal separator (17, 18) dividing the condensed and solid products from the cooling water, to then send the condensed and divided products to the beginning of the cycle for a second distillation, or the separate products will be stored for industrial use of the same. 12. Pyrolysis plant according to claim 8, characterized in that the fourth washing section (400), adapted to receive the syngas cooled below 80 ?C, ? designed, by means of two cooling towers containing a mixture of water, the first weakly acidic and the second weakly basic, to provide, in addition to a further cooling of the syngas which is in a phase of completion of the catalysis process, to do yes that the PH remains between the values of 6 and 7 throughout the process, any condensed high-boiling hydrocarbons being separated from the water by means of centrifugal separators and sent back to the beginning of the cycle, while, subsequently, the gas passes into a column of activated carbon filtration to lose humidity, in addition to the activated carbons, the fourth section (400) being equipped with a filtering system pushed to eliminate any formation of any pollutants present. 13. Pyrolysis plant according to claim 8, characterized in that, in the fifth final section, in case of emergency, the syngas produced, after washing, is sent to an emergency torch, the induction generators (6) are switched off automatically and the pyrolysis chamber (100) and the stilling chamber (12) are purged with a nitrogen gas, said fifth safety section also comprising? an emergency connection system equipped with appropriate valves adapted to convey the gas of the pyrolysis chamber (100) towards the emergency torch in the event of a failure, said fifth section also comprising a plant for the production of nitrogen by separation and the relative nitrogen storage tank. 14. Method for the treatment of solid and liquid waste, characterized in that it is carried out by means of a plant according to any one of claims 1 to 7, said method providing for a pyrolysis treatment of said solid and liquid waste, from which are obtained a synthesis gas, syngas, and an inert residue, said method comprising the steps of subjecting the products of pyrolysis to fractional distillation and sending the bituminous residues, tar, of said fractional distillation to a new cycle of pyrolysis, said solid waste comprising materials plastics and biomasses and being loaded directly into the pyrolysis chamber (2) in which they undergo said pyrolysis treatment, said liquid waste comprising waste oils and fats which are introduced into said pyrolysis chamber (2) after mixing with said bituminous residues, tar, from the fractional distillation of the pyrolysis products. 15. Method for the disposal of waste consisting of plastic materials or biomass, and of all organic materials which contain carbon in their molecules, characterized in that it is carried out by means of a plant according to any one of claims 8 to 13, said method providing a pyrolysis treatment of said solid and liquid waste, from which a synthesis gas, syngas, and an inert residue are obtained, said method comprising the steps of subjecting the pyrolysis products to fractional distillation and sending them to a new pyrolysis cycle the bituminous residues, tar, of said fractional distillation, said solid waste comprising plastic materials and biomass and being loaded directly into the pyrolysis chamber (2) in which they undergo said pyrolysis treatment, said liquid waste comprising waste oils and fats which are inserted into said pyrolysis chamber (2) after mixing with said bituminous residues, tar, coming from fractional distillation of the products of pyrolysis, said method also based on the principle that when a molecule is placed in an electric field it orients itself according to its dipole and, if the electric field is repeatedly inverted, the molecule ? forced to reposition itself at each reversal of the field and this causes a heating of the molecules all the more? efficient as much as ? close to the resonance frequency of the molecule, but heating still takes place even when the frequencies are different from the resonance ones, said method initially based on the heating of the molecules within an electric field, until their splitting with the formation of a synthesis gas , syngas, mainly composed of CO-CO?-H?-O?, while, subsequently, the cylinder (2) acts as a directional antenna and, due to the effect of the induced electromagnetic field, the molecular disorder generated by the temperature undergoes an energetic contribution by the radiofrequency waves and the syngas components ionize strongly, interact with the superheated steam and create new ordered structures which are addressed by means of the PLC control of the radiofrequency originating mainly CH?.