Description:FIELD OF THE INVENTION
The present invention relates to a plasma gasification system. More specifically, the present invention relates to a plasma gasification system to generate electricity from waste material.
BACKGROUND OF THE INVENTION
Plasma gasification technology represents a cutting-edge method for converting various types of waste into clean energy. Unlike traditional incineration, which burns waste in the presence of oxygen, plasma gasification utilizes extremely high temperatures generated by a plasma arc to break down waste materials into their basic molecular components. This process produces synthesis gas (syngas), primarily composed of hydrogen and carbon monoxide, that can be harnessed for power generation. The versatility of plasma gasification allows it to handle municipal solid waste, industrial waste, agricultural waste, and hazardous materials, making it a highly adaptable and efficient solution for modern waste management challenges.
Traditional waste disposal methods, such as landfilling and incineration, present significant environmental and health risks. Landfills contribute to land pollution and the emission of methane, a potent greenhouse gas. Incineration, while reducing the volume of waste, releases harmful pollutants, including fly ash, dioxins, and furans, into the atmosphere. These pollutants can cause respiratory problems, contaminate soil and water, and contribute to global warming. Additionally, existing plasma gasification systems are often bulky, require extensive infrastructure, and involve complex manual operations, making them impractical for widespread deployment. The inefficiency and environmental hazards associated with these traditional methods underscore the urgent need for innovative solutions in waste management.
US8109218B2 discloses a process for the treatment of waste, the process comprising either a gasification step or a pyrolysis step to produce an offgas and a non-airborne, solid char material; followed by a plasma treatment step. An associated apparatus has a plasma treatment unit which is separate from the gasification unit or pyrolysis unit.
In conclusion, the present invention addresses the limitations of existing technologies by introducing a highly efficient, portable, and environmentally friendly plasma gasification system. Fully automated, it requires minimal manual intervention, reducing operational complexities and labour costs. By converting waste into electricity without pollution, the present invention not only mitigates air and land pollution.
OBJECTIVE OF THE INVENTION
The main objective of the present invention is to provide a method for removing waste materials without causing environmental pollution, thereby helping to preserve the ozone layer.
Another objective of the present invention is to provide a solution for controlling particulate matter, hazardous elements, open burning emissions, carbon and fly ashes, and harmful metals.
Yet another objective of the present invention is to provide machines with fully automated shredding, loading, and sensor controls managed by a Programmable Logic Controller (PLC).
Yet another objective of the present invention is to provide a process for generating electricity, offering a sustainable energy solution while effectively managing waste.
Yet another objective of the present invention is to provide a specially designed gas separation valve to keep incoming environmental oxygen separate from the reactor gas.
Yet another objective of the present invention is to provide a machine that is easy to transport and can be disassembled into two parts using a coupling system, eliminating the need for an RCC building.
Yet another objective of the present invention is to provide a machine customized to handle a specific amount of waste per ton per hour, designed for easy installation.
Yet another objective of the present invention is to provide a cleaner, more efficient, and versatile method for converting waste into energy, supporting both environmental sustainability and energy security.
Further objectives, advantages, and features of the present invention will become apparent from the detailed description provided herein below, in which various embodiments of the disclosed invention are illustrated by way of example.

SUMMARY OF THE INVENTION
The present invention relates to a plasma gasification system to generate electricity from waste material without pollution and incineration. The system includes a canopy type structure, a magnetic roller, an auto shredder unit, a plasma gasification chamber, a screw conveyor system, a gas turbo rotation system, a turbo water cool gasket, a high velocity air cooling fan, a fin type aluminium condenser, a syngas cycloner, a heat exchanger, a wet scrubber, a first fan, a second fan, a third fan, a fourth fan, a syngas dry filtration chamber, a turbine blower, and an electricity generation unit. The canopy type structure encloses the whole plasma gasification system. The magnetic roller segregates heavy iron metals from waste material. The auto shredder unit is connected to the magnetic roller to receive and shred the extracted heavy iron metals into small pieces. The auto shredder unit includes a gear box, and a motor. The motor is coupled with the gear box to power the auto shredder unit. The plasma gasification chamber is connected to the auto shredder unit for receiving the shredded small pieces and converting shredded small pieces into syngas using arc electrodes. The plasma gasification chamber includes a filling electrode, an ignition electrode, and an earthing electrode. The screw conveyor system connects the auto shredder unit to the plasma gasification chamber to transfer shredded small pieces from the auto shredder unit to the plasma gasification chamber. The gas turbo rotation system is mounted on top of the plasma gasification chamber for cooling the syngas using a high-velocity air cooling fan. Herein the gas pipes used in the gas turbo rotation system are seamless, and fin-type aluminium condensers and are installed on pipes to facilitate temperature control of the syngas. In the preferred embodiment, the gas turbo rotation system, circulates gas by rotating through layout pipes, ensures smooth gas flow and effective condensation. The syngas cycloner is connected to the gas turbo rotation system. The syngas cycloner separates carbon residues from the cooled syngas to obtain clean syngas. The heat exchanger is connected to the syngas cycloner for reducing the temperature of the clean syngas. The wet scrubber is connected to the heat exchanger. The wet scrubber is fitted with water nozzles to remove ash and pollutants from the cooled syngas. The first fan is mounted on the top surface of the canopy type structure. The first fan cools the plasma gasification chamber. The second fan is mounted on the top surface of the canopy type structure. The second fan cools the heat exchanger. The third fan is mounted on the top surface of the canopy type structure. The fourth fan is mounted on the top surface of the canopy type structure the third fan and the fourth fan cool the syngas dry filtration chamber. The syngas dry filtration chamber cleans the syngas. Herein the syngas dry filtration chamber has the ability to remove fine micro particles from syngas and makes the syngas moisture free & dry. The turbine blower is connected to the syngas dry filtration chamber. The electricity generation unit is connected to the turbine blower. The turbine blower compresses the filtered and dried syngas to a high pressure for efficient delivery of high-pressure syngas to the electricity generation unit to produce the electricity and distributes the produced electricity to grid connection. Herein, the system is a fully automated control system for managing the waste conversion process, including automatic segregation, shredding, and blockage clearance. Herein, the waste material is processed in the plasma gasification chamber in the absence of oxygen to prevent burning and reduce emissions. Herein, the system has two booster pumps designed for separate handling of liquid and dry slag. Herein, the system has a unique gas separation valve to maintain the separation of incoming environmental oxygen and reactor gas.
The main advantage of the present invention is that it removes waste materials without causing environmental pollution, thereby helping to preserve the ozone layer.
Another advantage of the present invention is that it controls particulate matter, hazardous elements, open burning emissions, carbon and fly ashes, and harmful metals.
Yet another advantage of the present invention is that it provides machines with fully automated shredding, loading, and sensor controls managed by a Programmable Logic Controller (PLC).
Yet another advantage of the present invention is that it generates electricity through the process, offering a sustainable energy solution while effectively managing waste.
Yet another advantage of the present invention is that it includes a specially designed gas separation valve to keep incoming environmental oxygen separate from the reactor gas.
Yet another advantage of the present invention is that it offers a machine that is easy to transport and can be disassembled into two parts using a coupling system, eliminating the need for an RCC building.
Yet another advantage of the present invention is that it customizes the machine to handle a specific amount of waste per ton per hour and is designed for easy installation.
Yet another advantage of the present invention is that it provides a cleaner, more efficient, and versatile method for converting waste into energy, supporting both environmental sustainability and energy security.
Further objectives, advantages, and features of the present invention will become apparent from the detailed description provided herein below, in which various embodiments of the disclosed invention are illustrated by way of example.
BRIEF DESCRIPTION OF DRAWINGS
The accompanying drawings are incorporated in and constitute a part of this specification to provide a further understanding of the invention. The drawings illustrate one embodiment of the invention and together with the description, serve to explain the principles of the invention.
Fig.1 illustrates the side and section view of a plasma gasification system(100).
Fig. 2 shows the roof top view of canopy type structure(104).
Fig. 3 shows the gas turbo rotation system(118).
DETAILED DESCRIPTION OF THE INVENTION
Definition
The term “a” or “an”, as used herein, is defined as one. The term “plurality”, as used herein, is defined as two as or more than one. The term “another”, as used herein, is defined as at least a second or more. The terms “including” and/or “having”, as used herein, are defined as comprising (i.e., open language). The term “comprising” is not intended to limit the present invention with such terminology rather is used in a wider sense. Any invention using the term comprising could be separated into one or more claims using “consisting” or “consisting of”. The term “comprising” may be used interchangeably with the terms “having” or “containing”. Reference in this document to “one embodiment”, “certain embodiments”, “an embodiment”, “another embodiment”, and “yet another embodiment” or similar terms, throughout the document means that a specific feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, the appearances of such phrases in various places, this specification throughout are not necessarily all referring to the same embodiment. Furthermore, the specific features, structures, or characteristics are combined in any suitable manner in one or more embodiments without limitation. The term “or” as used herein is to be interpreted as inclusive or meaning any one or more combinations. Therefore, “A, B or C” means any of the following: “A; B; C; A and B; A and C; B and C; A, B and C”. An exception to this definition will occur only when a combination of elements, functions, steps, or acts are in mutually exclusive, inherently. As used herein, the term "one or more" generally refers to, but is not limited to, singular as well as the plural form of the term.
Fig.1 illustrates side and section view of a system(100). The system(100) includes a canopy type structure(104), an auto shredder unit(110), a plasma gasification chamber(108), a screw conveyor system(116), a gas turbo rotation system(118), a turbo water cool gasket(148), a high-velocity air cooling fan(150), a fin-type aluminium condenser(152), a syngas cycloner(120), a heat exchanger(122), a wet scrubber(124), a syngas dry filtration chamber(136), a turbine blower(138), and a electricity generation unit(140). The canopy type structure(104) encloses the whole plasma gasification system(100). The auto shredder unit(110) includes a gear box(112). The plasma gasification chamber(108) is connected to the auto shredder unit(110). The plasma gasification chamber(108) includes a filling electrode(142), a ignition electrode(144), and a earthing electrode(146). The screw conveyor system(116) connects the auto shredder unit(110) to the plasma gasification chamber(108). The gas turbo rotation system(118) is mounted on top of the plasma gasification chamber(108). The turbo water cool gasket(148) is attached on outer surface of the gas turbo rotation system(118). The high-velocity air cooling fan(150) are present inside the gas turbo rotation system(118). The fin-type aluminium condenser(152) are installed in pipes that passes cooled syngas to the syngas cycloner(120). The syngas cycloner(120) is connected to the gas turbo rotation system(118). The heat exchanger(122) is connected to the syngas cycloner(120). The wet scrubber(124) is connected to the heat exchanger(122). The heat exchanger(122) is connected to the syngas cycloner(120). The turbine blower(138) is connected to the syngas dry filtration chamber(136). The electricity generation unit(140) is connected to the turbine blower(138).

Fig. 2 shows roof top view of canopy type structure(104)
Fig. 3 shows the gas turbo rotation system(118)

The present invention relates to a system to generate electricity from waste material without pollution and incineration. The system includes a canopy type structure, a magnetic roller, an auto shredder unit, a plasma gasification chamber, a turbo water cool gasket, a high-velocity air cooling fan, a fin-type aluminium condenser, a screw conveyor system, a gas turbo rotation system, a syngas cycloner, a heat exchanger, a wet scrubber, a first fan, a second fan, a third fan, a fourth fan, a syngas dry filtration chamber, a turbine blower, and an electricity generation unit. The canopy type structure encloses the whole plasma gasification system. The magnetic roller segregates heavy iron metals from waste material. The auto shredder unit is connected to the magnetic roller to receive and shred the extracted heavy iron metals into small pieces. The auto shredder unit includes a gear box. In an embodiment, herein in case of any choking & blocking of any type of the hard shredded waste, the auto shredder unit will auto detect the same and will work for 4 seconds in reverse position to clear the blockage and come back to normal working. The plasma gasification chamber is connected to the auto shredder unit for receiving the shredded small pieces and converting shredded small pieces into syngas using arc electrodes. The plasma gasification chamber includes a filling electrode, an ignition electrode, and one earthing electrode. In an embodiment, six arc electrodes are present in the plasma gasification chamber having three filling electrodes, two ignition electrodes, one earthing electrode and are designed to achieve a temperature up to 10,000 ?. In an embodiment, herein the plasma gasification chamber includes a four-layer construction, an outer main shell cover made from mild steel that provides structural support, a second asbestos-insulated layer for retaining heat and enhancing energy efficiency, a third stainless steel layer that withstands temperatures up to 2,600 ? for durability, an inner ceramic layer having boiling point of 2,977 ?, ensures thermal insulation and durability. The screw conveyor system connects the auto shredder unit to the plasma gasification chamber to transfer shredded small pieces from the auto shredder unit to the plasma gasification chamber. The gas turbo rotation system is mounted on top of the plasma gasification chamber for cooling the syngas using a high-velocity air cooling fan. The turbo water cool gasket is attached to the outer surface of the gas turbo rotation system. The turbo water cool gasket is supplied with cool water that helps in cooling the gas flowing in the gas turbo rotation system. The high-velocity air cooling fan are present inside the gas turbo rotation system, syngas rotates the high velocity air cooling fan, gas passes through the high velocity air cooling fan cools down by expansion. The fin-type aluminium condenser seamless, facilitate temperature control of the syngas, and are installed in pipes that passes cooled syngas to the syngas cycloner. The syngas cycloner is connected to the gas turbo rotation system. The syngas cycloner separates carbon residues from the cooled syngas to obtain clean syngas. The heat exchanger is connected to the syngas cycloner for reducing the temperature of the clean syngas. The wet scrubber is connected to the heat exchanger. The wet scrubber is fitted with water nozzles to remove ash and pollutants from the cooled syngas. The first fan is mounted on the top surface of the canopy type structure. The first fan cools the plasma gasification chamber. The second fan is mounted on the top surface of the canopy type structure. The second fan cools the heat exchanger. The third fan is mounted on the top surface of the canopy type structure. The fourth fan is mounted on the top surface of the canopy type structure the third fan and the fourth fan cool the syngas dry filtration chamber. The syngas dry filtration chamber cleans the syngas. Herein the syngas dry filtration chamber has the ability to remove fine micro particles from syngas and makes the syngas moisture free & dry. In the preferred embodiment, syngas dry filtration chamber cleans the syngas and removes fine microparticles and make syngas dry and moisture-free. The turbine blower is connected to the syngas dry filtration chamber. The electricity generation unit is connected to the turbine blower. The turbine blower compress the filtered and dried syngas to a high pressure for efficient delivery of high-pressure syngas to the electricity generation unit to produce the electricity and distributes the produced electricity to grid connection. Herein, the high-velocity air cooling fan are present inside the gas turbo rotation system that makes the system compact hence space requirement is less. Herein, the turbo water cool gasket cools water easily that facilitates the cooling of syngas.
Herein, the system is a fully automated control system for managing the waste conversion process, including automatic segregation, shredding, and blockage clearance. Herein, the waste material is processed in the plasma gasification chamber in the absence of oxygen to prevent burning and reduce emissions. Herein, the system has two booster pumps designed for separate handling of liquid and dry slag. Herein, the system has a unique gas separation valve to maintain the separation of incoming environmental oxygen and reactor gas. In the preferred embodiment, herein the system is designed to be dismantled into two parts for ease of transport and installation without requiring a reinforced concrete building.
In an embodiment, the present invention relates to a system to generate electricity from waste material without pollution and incineration. The system includes one or more canopy type structures, one or more magnetic rollers, one or more auto shredder units, one or more plasma gasification chambers, one or more turbo water cool gasket, one or more high-velocity air cooling fan, one or more fin-type aluminium condenser, one or more screw conveyor systems, one or more gas turbo rotation systems, one or more syngas cycloners, one or more heat exchangers, one or more wet scrubbers, one or more first fans, one or more second fans, one or more third fans, one or more fourth fans, one or more syngas dry filtration chambers, one or more turbine blowers, and one or more electricity generation units. The one or more canopy type structures enclose the whole plasma gasification system. The one or more magnetic rollers segregate heavy iron metals from waste material. The one or more auto shredder units are connected to the one or more magnetic rollers to receive and shred the extracted heavy iron metals into small pieces. The one or more auto shredder units include one or more gear boxes. In an embodiment, herein in case of any choking & blocking of any type of the hard shredded waste, the one or more auto shredder unit will auto detect the same and will work for 4 seconds in reverse position to clear the blockage and come back to normal working. The one or more plasma gasification chambers are connected to the one or more auto shredder units for receiving the shredded small pieces and converting shredded small pieces into syngas using one or more arc electrodes. The one or more plasma gasification chambers include one or more filling electrodes, one or more ignition electrodes, and one or more earthing electrodes. In an embodiment, six arc electrodes are present in the one or more plasma gasification chambers having three filling electrodes, two ignition electrodes, one earthing electrode and are designed to achieve a temperature up to 10,000 ?. In an embodiment, herein the one or more plasma gasification chambers include a four-layer construction, an outer main shell cover made from mild steel that provides structural support, a second asbestos-insulated layer for retaining heat and enhancing energy efficiency, a third stainless steel layer that withstands temperatures up to 2,600 ? for durability, an inner ceramic layer having boiling point of 2,977 ?, ensures thermal insulation and durability. The one or more screw conveyor systems connect the one or more auto shredder units to the one or more plasma gasification chambers to transfer shredded small pieces from the one or more auto shredder units to the one or more plasma gasification chambers. The one or more gas turbo rotation systems are mounted on top of the one or more plasma gasification chambers for cooling the syngas using one or more high-velocity air cooling fan. The one or more turbo water cool gasket is attached on outer surface of the one or more gas turbo rotation system. The one or more turbo water cool gasket is supplied with cool water that helps in cooling the gas flowing in the gas turbo rotation system. The one or more high-velocity air cooling fan are present inside the one or more gas turbo rotation system, syngas rotates the one or more high velocity air cooling fan, gas passes through the one or more high velocity air cooling fan cools down by expansion. The one or more fin-type aluminium condenser seamless, facilitate temperature control of the syngas, and are installed in pipes that passes cooled syngas to the one or more syngas cycloner. The one or more syngas cycloners are connected to the one or more gas turbo rotation systems. The one or more syngas cycloners separate carbon residues from the cooled syngas to obtain clean syngas. The one or more heat exchangers are connected to the one or more syngas cycloners for reducing the temperature of the clean syngas. The one or more wet scrubber is connected to the one or more heat exchangers. The one or more wet scrubbers are fitted with water nozzles to remove ash and pollutants from the cooled syngas. The one or more first fans are mounted on the top surface of the one or more canopy type structures. The one or more first fans cool the one or more plasma gasification chambers. The one or more second fans are mounted on the top surface of the one or more canopy type structures. The one or more second fans cool the one or more heat exchanger. The one or more third fans are mounted on the top surface of the one or more canopy type structures. The one or more fourth fans are mounted on the top surface of the one or more canopy type structures the one or more third fans and the one or more fourth fans cool the one or more syngas dry filtration chambers. The one or more syngas dry filtration chambers clean the syngas. Herein the one or more syngas dry filtration chambers have the ability to remove fine micro particles from syngas and make the syngas moisture free & dry. In the preferred embodiment, syngas dry filtration chamber clean the syngas and remove fine microparticles and make syngas dry and moisture-free. The one or more turbine blowers are connected to the one or more syngas dry filtration chambers. The one or more electricity generation units are connected to the one or more turbine blowers. The one or more turbine blowers compress the filtered and dried syngas to a high pressure for efficient delivery of high-pressure syngas to the one or more electricity generation units to produce the electricity and distributes the produced electricity to grid connection. Herein, the one or more high-velocity air cooling fan are present inside the one or more gas turbo rotation system that makes system compact hence space requirement is less. Herein, the one or more turbo water cool gasket cools water easily that facilitates cooling of syngas. Herein, the plasma gasification system is a fully automated control system for managing the waste conversion process, including automatic segregation, shredding, and blockage clearance. Herein, the waste material is processed in the one or more plasma gasification chambers in the absence of oxygen to prevent burning and reduce emissions. Herein, the system has two booster pumps designed for separate handling of liquid and dry slag. Herein, the system has a unique gas separation valve to maintain separation of incoming environmental oxygen and reactor gas. In the preferred embodiment, herein the one or more plasma gasification system is designed to be dismantled into two parts for ease of transport and installation without requiring a reinforced concrete building.
In an embodiment, the present invention related to a method for electricity generation from waste material. The method includes:
the waste material is treated with the magnetic roller to extract heavy iron metals;
extracted heavy iron metals are fed into the auto shredder unit to shred extracted heavy iron metals into small pieces;
shredded small pieces are fed into the plasma gasification chamber with the help of the screw conveyor system;
in the plasma gasification chamber 6 arc electrodes are present to start the plasma gasification process that converts the shredded material into syngas having temperature 10,000 ?;
the generated syngas is then directed to the gas turbo rotation system that circulates the gas through layout pipes and cools the syngas using high-velocity air cooling fan;
after cooling, the syngas is passed through the syngas cycloner, that separates carbon residues from the gas to obtain clean syngas;
the cleaned syngas is then processed through the heat exchanger to reduce the syngas input temperature of syngas to around 1600 ?;
the syngas with reduced temperature of 1600 ?, flows through the wet scrubber that removes ash and pollutants from the syngas using high water pressure to further clean the syngas;
the cleaned and cooled syngas is then directed to the syngas dry filtration chamber to make syngas dry and moisture free;
the filtered and dried syngas is then delivered to the turbine blower, that compresses the syngas to very high pressure (4 Bar) for efficient delivery to the generator engine;
the high-pressure syngas is supplied to the electricity generation unit where high pressure syngas is used to generate electricity; and
the produced electricity is then fed into the grid for distribution.
In an embodiment, the present invention related to a method for electricity generation from waste material. The method includes:
the waste materials are treated with the one or more magnetic rollers to extract heavy iron metals;
extracted heavy iron metals are fed into the one or more auto shredder units to shred extracted heavy iron metals into small pieces;
shredded small pieces are fed into the one or more plasma gasification chambers with the help of the one or more screw conveyor systems;
in the one or more plasma gasification chambers 6 arc electrodes are present to start the plasma gasification process that converts the shredded material into syngas having temperature 10,000 ?;
the generated syngas is then directed to the one or more gas turbo rotation systems that circulates the gas through layout pipes and cools the syngas using one or more high-velocity air cooling fan;
after cooling, the syngas is passed through the one or more syngas cycloners, that separates carbon residues from the gas to obtain clean syngas;
the cleaned syngas is then processed through the one or more heat exchangers to reduce the syngas input temperature of syngas to around 1600 ?;
the syngas with reduced temperature of 1600 ?, flows through the one or more wet scrubbers that removes ash and pollutants from the syngas using high water pressure to further clean the syngas;
the cleaned and cooled syngas is then directed to the one or more syngas dry filtration chambers to make syngas dry and moisture free;
the filtered and dried syngas is then delivered to the one or more turbine blowers, that compresses the syngas to very high pressure (4 Bar) for efficient delivery to the generator engine;
the high-pressure syngas is supplied to the one or more electricity generation units where high pressure syngas is used to generate electricity; and
the produced electricity is then fed into the grid for distribution. , C , Claims:1. A system(100) to generate electricity from waste material(102) without pollution and incineration, the system(100) comprising:
an at least one canopy type structure(104), the at least one canopy type structure(104) encloses the whole plasma gasification system(100);
an at least one magnetic roller(106), the at least one magnetic roller(106) is present in front of the at least one auto shredder unit(110), the at least one magnetic roller(106) segregate heavy iron metals from waste material(102);
an at least one auto shredder unit(110), the at least one auto shredder unit(110) is connected to the at least one magnetic roller(106) to receive and shred the extracted heavy iron metals into small pieces, the at least one auto shredder unit(110) having:
an at least one gear box(112);
an at least one plasma gasification chamber(108), the at least one plasma gasification chamber(108) is connected to the at least one auto shredder unit(110) for receiving the shredded small pieces and converting shredded small pieces into syngas using arc electrodes, the at least one plasma gasification chamber(108) having:
an at least one filling electrodes(142),
an at least one ignition electrodes(144), and
an at least one earthing electrode(146);
an at least one screw conveyor system(116), the at least one screw conveyor system(116) connects the at least one auto shredder unit(110) to the at least one plasma gasification chamber(108) to transfer shredded small pieces from the at least one auto shredder unit(110) to plasma gasification chamber(108);
an at least one gas turbo rotation system(118), the at least one gas turbo rotation system(118) is mounted on top of the at least one plasma gasification chamber(108) for cooling the syngas, the at least one gas turbo rotation system(118) having:
an at least one turbo water cool gasket(148),the at least one turbo water cool gasket(148) is attached on outer surface of the at least one gas turbo rotation system(118), the at least one turbo water cool gasket(148) is supplied with cool water that helps in cooling the gas flowing in the at least one gas turbo rotation system(118);
an at least one high-velocity air cooling fan(150), the at least one high velocity air cooling fan(150) are present inside the at least one gas turbo rotation system(118), syngas rotates the at least one high velocity air cooling fan(150), gas passes through the at least one high velocity air cooling fan(150) cools down by expansion;
an at least one fin-type aluminium condenser(152), the at least one fin-type aluminium condenser(152) are seamless, facilitate temperature control of the syngas, the at least one fin-type aluminium condenser(152) are installed in pipes that passes cooled syngas to the at least one syngas cycloner(120);
an at least one syngas cycloner(120), the at least one syngas cycloner(120) is connected to the at least one gas turbo rotation system(118), the at least one syngas cycloner(120) separates carbon residues from the cooled syngas to obtain clean syngas;
an at least one heat exchanger(122), the at least one heat exchanger(122) is connected to the at least one syngas cycloner(120) for reducing the temperature of the clean syngas;
an at least one wet scrubber(124), the at least one wet scrubber(124) is connected to the at least one heat exchanger(122), the at least one wet scrubber(124) is fitted with water nozzles to remove ash and pollutants from the cooled syngas;
an at least one first fan(128), the at least one first fan(128) is mounted on the top surface of the at least one canopy type structure(104), and the at least one first fan(128) cools the plasma gasification chamber(108);
an at least one second fan(130), the at least one second fan(130) is mounted on the top surface of the at least one canopy type structure(104) and the at least one second fan(130) cools the heat exchanger(122);
an at least one third fan(132), the at least one third fan(132) is mounted on the top surface of the at least one canopy type structure(104);
an at least one fourth fan(134), the at least one fourth fan(134) is mounted on the top surface of the at least one canopy type structure(104), and the at least one third fan(132) and an at least one fourth fan(134) cool the at least one syngas dry filtration chamber(136);
an at least one syngas dry filtration chamber(136), the at least one syngas dry filtration chamber(136) is connected to the at least one syngas dry filtration chamber(136) cleans the syngas, wherein the at least one syngas dry filtration chamber(136) has the ability to remove fine micro particles from syngas and makes the syngas moisture free & dry;
an at least one turbine blower(138), the at least one turbine blower(138) is connected to the at least one syngas dry filtration chamber(136);
an at least one electricity generation unit(140), the at least one electricity generation unit(140) is connected to the at least one turbine blower(138), the at least one turbine blower(138) compress the filtered and dried syngas to a high pressure for efficient delivery of high-pressure syngas to the at least one electricity generation unit(140) to produce the electricity, and distributes the produced electricity to grid connection;
characterized in that, the at least one high-velocity air cooling fan(144) are present inside the at least one gas turbo rotation system(118) that cools down the syngas quickly and the at least one gas turbo rotation system(118) mitigate need of large sized heat exchanger thus make the system(100) compact, the at least one turbo water cool gasket(142) uses water that facilitates cooling of syngas thus reduces the cost of coolant;
wherein, plasma gasification system(100) is a fully automated control system for managing the waste conversion process, including automatic segregation, shredding, and blockage clearance;
wherein, the waste material is processed in the plasma gasification chamber(108) in the absence of oxygen to prevent burning and reduce emissions;
wherein, the system(100) has two booster pumps designed for separate handling of liquid and dry slag; and
wherein, the system(100) has a unique gas separation valve to maintain separation of incoming environmental oxygen and reactor gas.
2. The system(100) as claimed in claim 1, wherein in case of any choking & blocking of any type of the hard shredded waste, the auto shredder unit(110) will auto detect the same and will work for 4 seconds in reverse position to clear the blockage and come back to normal working.

3. The system(100) as claimed in claim 1, wherein six arc electrodes are present in plasma gasification chamber(108) having three filling electrodes(142), two ignition electrodes(144), one earthing electrode(146) that are designed to achieve a temperature up to 10,000 ?.
4. The system(100) as claimed in claim 1, wherein the plasma gasification chamber(108) comprises a four-layer construction, an outer main shell cover made from mild steel that provides structural support, a second asbestos-insulated layer for retaining heat and enhancing energy efficiency, a third stainless steel layer that withstands temperatures up to 2,600 ? for durability, an inner ceramic layer having boiling point of 2,977 ?, ensures thermal insulation and durability.
5. The system(100) as claimed in claim 1, wherein, the at least one heat exchanger(122) is made of stainless steel with coolant volume capacity of 780 Lt and withstand high temperatures, and reduces the temperature of the clean syngas to around 1600°C.
6. The system(100) as claimed in claim 1, wherein the system(100) is designed to be dismantled into two parts for ease of transport and installation without requiring a reinforced concrete building.
7. The system(100) as claimed in claim 1, wherein gas turbo rotation system(118), circulates gas by rotating through layout pipes, ensures smooth gas flow and effective condensation.
8. The system(100) as claimed in claim 1, wherein syngas dry filtration chamber(136) cleans the syngas and removes fine microparticles and make syngas dry and moisture-free, the syngas dry filtration chamber(136) have 4 high air velocity cooling fans, the first fan cools the reactor, the second cools the pipe shell condenser, and the third and fourth fans manage the coolant exchanger condenser.
9. The method for electricity generation from waste material(102) as claimed in claim1, the method comprising:
the at least one waste material(102) is treated with the at least one magnetic roller(106) to extract heavy iron metals;
extracted heavy iron metals are fed into the at least one auto shredder unit(110) to shred extracted heavy iron metals into small pieces;
shredded small pieces are fed into the at least one plasma gasification chamber(108) with the help of the at least one screw conveyor system(116);
in the at least one plasma gasification chamber(108) six arc electrodes are present to start the plasma gasification process that converts the shredded material into syngas having temperature 10,000 ?;
the generated syngas is then directed to the at least one gas turbo rotation system(118) that circulates the gas through layout pipes and cools the syngas using high-velocity air cooling fan;
after cooling, the syngas is passed through the at least one syngas cycloner(120), that separates carbon residues from the gas to obtain clean syngas;
the cleaned syngas is then processed through the at least one heat exchanger(122) to reduce the syngas input temperature of syngas to around 1600 ?;
the syngas with reduced temperature of 1600 ?, flows through the at least one wet scrubber(124) that removes ash and pollutants from the syngas using high water pressure to further clean the syngas;
the cleaned and cooled syngas is then directed to the at least one syngas dry filtration chamber(136) to make syngas dry and moisture free;
the filtered and dried syngas is then delivered to the at least one turbine blower(138), that compresses the syngas to very high pressure (4 Bar) for efficient delivery to the generator engine;
the high-pressure syngas is supplied to the at least one electricity generation unit(140) where high pressure syngas is used to generate electricity;
the produced electricity is then fed into the grid for distribution.