TECHNICAL FIELD OF THE INVENTION:

[001] The present invention generally relates to a system and method for the treatment of MSW and other organic waste materials. More particularly, the present invention relates to treatment of MSW organic waste - hospital waste, pharmaceutical waste with mixed chemicals and mixed waste which can be destroyed without creating or producing harmful emissions.

BACKGROUND OF THE INVENTION:

[002] Most of the waste produced from the Industries, homes and some private organizations are generally released into small nullahs, canals, rivers and seas without treatment, otherwise, dumped in ground; which result in the environmental pollution which is a serious Hazard to the ecosystem. Most of the materials used for the preparation of any pharmaceutical products or any chemical residue or medicinal waste or routine household items are non-bio-degradable in the soil, which is serious threat to the ecological balance of the environment. The treatment of such waste from industries or homes or any organizations, needs to be done, prevent damage to the ecosystem. The treatment should be in such a way that it should not produce harmful emissions resultants and it has to achieve in economical way and also has to achieve by using low amount of resources.

[003] In daily household waste comprises mostly of the organic waste and dry organic & inorganic materials which are simply dumped in aforesaid routes without processing it in a safe way. The Pharmaceutical industries for the manufacture of drugs or pharmaceutical products not limited to any category requires more no of Chemicals along with many additives which results in to an API or a formulation. But the resultants or by products are released directly in to aforesaid routes without processing them in a safe way and not converting them in to a safe products and most of these released materials are annihilate the environment. Not limited to above cases most of the materials used in daily life, whether related to domestic or in any organizations are simply dumping without processing them in safe ways.

[004] Waste material or garbage is also destroyed by incineration, which too, results in the generation of harmful gases released to cause air pollution. Incinerators also it requires large space which in space starved cities or towns is not feasible. [005] In the present scenario the growth of industries in any field is unstoppable as it is required to improve the standards of human beings.

[006] Even though government might be taking the steps to decrease the waste generated in all industries and to divide the waste in to different types, but all these measures are not sufficient to put an end to the pollution caused by the waste to ecosystem. And also the processing of waste burning without releasing harmful effluents is not achieved by the present available processes.

[007] Most of the nations are simply burying the waste, where the degradation will not be achieved accurately. Many nations are recycling the waste but the percentage of recycling very low and the remaining amount of waste is simply burnt or used as landfill, which results in the pollution of the environment.

[008] So as to overcome the above problems, the government stopped burying food wastes namely, according to the regulations, only residuals produced after incineration, compost treatment or extermination could be buried, so that the organic materials can be treated based on incineration and recycling methods.

[009] The proposed recycling methods are may not be economical and they may produce different pollutants.

[010] W02004/072208 relates to a method and a device for continuous conversion of organic waste into sin gases like H2 and CO. More specifically, it relates to treating highly contaminated waste products and worn-out vehicle tires in which the charge is liquefied and then cracked giving a product in the gaseous phase, wherein the charge is introduced in to a hot bath, comprising liquid inorganic medium, displaced through the melting zone and the decomposition zone and then the gaseous products of the decomposition are collected at the top and the impurities are removed by means of at least one conveyer. The decomposition reactions are carried out catalytically in the liquefied layer of the charge formed on the surface of the hot bath comprising liquid inorganic medium.

[Oil] US9518733B1 discloses a furnace apparatus to incinerate solid waste comprising a chamber, a solid waste feed inlet, air inlet pipes and air outlet pipes. The air inlet pipes receive air for combustion of the solid waste within the lower combustion section. The air outlet pipes exhaust combusted air from the lower combustion section, where multiple wigglers are operably attached on the air inlet pipes and the air outlet pipes. The paramagnetic oxygen present in the received air is concentrated via the wigglers, and the concentrated oxygen is introduced into plasma generated within the combustion section to accelerate the combustion process, and to oxidize toxic matter present in the solid waste. A dry scrubber used to remove toxins from flue gases is used.

[012] The methods and systems presently available in the market for thermal decomposition treatment of waste materials, but all are limiting some extent and producing harmful materials in to the environment and also they are expensive and require high amounts of power supply.

[013] Hence in the light of the aforementioned discussion, there is a need of a system and a method for treatment of waste material to decompose such as garbage, inert waste and Pharma waste, without producing harmful chemicals in to the environment.

OBJECTS OF THE INVENTION:

[014] The main object of the present invention is to provide a safe system and method for treatment of waste to decompose the waste material such as garbage, inert waste and Pharma waste, without producing harmful effects to the environment.

[015] It is another object of the present invention to provide the method and system for thermal decomposition treatment waste to decompose of waste material such as garbage, inert waste and Pharma waste completely, in affordable price and in different sizes based up on the need and also using very low amounts of power supply.

SUMMARY OF THE INVENTION:

[016] According to an aspect of the present invention, a system for treatment of waste materials, said system comprising at least one chamber provided with a charge feed door for feeding unsegregated waste materials into said chamber through chute at a predetermined time interval for treating waste materials, where the resident heat aids the magnetized ionized air to react with the hydrocarbons in the waste materials, a resultant exothermic reaction boosts the temperature to 350 - 400°C. The waste in the absence of air or free oxygen starts by splitting the molecules into atoms and is de-hydrated & reduced to Ceramic Ash. The heat induced by exothermic reaction phenomenon is retained in the system through a plurality of heating coils to generate heat and retain it to said chamber and waste heat is recycled through a tubular heat sink, where the recycled heat is supplied to wet waste material to reduce the moisture content, thereby increasing the efficiency or productivity of the machine. A separate chamber for collecting and separating ash deposited after the treatment of waste material, where at the upper layer of said radiator said heat sink is arranged at a hearth center section of said chamber to attain uniform heat transfer throughout the process of waste material treatment; a flue gas exhaust from said chamber is relayed through a dual or triple stage scrubber to remove toxic elements by spraying water or dilute solution and then released through a chimney into the atmosphere. The exhaust gases are actually heated in a separate area to 900 degrees centigrade to remove all toxins and dioxins from flue gas during scrubbing process. This processing of exhaust gas helps in reducing formation within the machine greatly, whereas multi-stage process of said scrubber removes toxins & dioxins from flue gas. This is to increase efficiency of the system & availability of the machine during practical application. The machine thus uses electricity back up only for the recirculation pump & heaters used for gas cleaning. This is entirely to confirm to the Air Pollutions norms; the waste reduction process is completely self-sustaining does not require any fuel or electricity support, therefore the operating cost is extremely low, therefore can be easily deployed in remote areas.

[017] Further machine efficiency & productivity, can be enhanced by use of an Air Cyclone in the exhaust gas line to induce remove gases which also aids rate of reaction within the reaction chamber. Accordingly varying the position of said exhaust pipe, atomized water spray by using multiple jets results in better cleansing of Flue gases.

[018] Another aspect of the present invention, wherein combustion chamber is double insulated to save the heat energy.

[019] It is another aspect of the present invention, wherein number of combustion chamber can be increased as per requirement.

[020] It is another aspect of the present invention, wherein a control panel is provided to monitor the process.

[021] It is another aspect of the present invention, wherein a ceramic coating of pipe and chimney pipe are provided for smooth functioning of the process.

[022] It is another aspect of the present invention, wherein the system is used for treating waste materials includes organic waste and inert waste such as hospital waste, pharmaceutical waste with mixed chemicals, mixed waste and organic waste can be well decomposed without creating or producing harmful materials or gases in to the environment.

[023] It is another aspect of the present invention, wherein the system used to treat inert waste such as Thermocol sheet, plastic materials, rubber, animal poultry waste, non-vegetarian waste, waste hydrocarbon material etc. BRIEF DESCRIPTION OF DRAWINGS:

[024] FIG. 1 illustrates schematic flow of the system for waste material treatment comprising all embodiments according to the present invention.

[025] FIG. 2 illustrates a projected view of the system for waste material treatment having feed door, preheating chamber, thermostat, tumbling rods, wiggleric valves, water pump, scrubbing cylinders and chimney pipe according to the present invention.

[026] FIG. 3 illustrates a projected view of the combustion chamber of system for waste material treatment having feed door, preheating chamber, collapsible doors, thermostat, tumbling rods, wiggleric valves, ash removal door, auto ignition heater, tar collector according to the present invention.

[027] FIG. 4 illustrates a perspective view of the system for waste material treatment having scrubbers, heaters, chimney according to the present invention.

[028] FIG. 5a - 5b illustrates a perspective view of second heaters of a scrubber of the system according to the present invention.

[029] FIG. 6 illustrates a projected Tumbling view of the system for waste material treatment having combustion chamber, control panel, ceramic coating pipe and chimney pipe according to the present invention.

DETAIFED DESCRIPTION OF THE INVENTION:

[030] Referring now to figures relates to a system and a method for treatment of waste material, where the system does not use any power or fuel for treatment of waste materials such as garbage, inert waste and Pharma waste completely, without producing harmful chemicals in to the environment.

[031] FIG. 1 of the present invention illustrates schematic flow of a system for treatment of waste materials comprising at least one combustion chamber, a plurality of heating coils, charge feed, chute, preheating chamber containing at least one tubular radiator, thermostat, a plurality of tumbling rods, flue gas exhaust, a plurality of wiggleric valves, tar collector, ash removal door, air inlet, vapour cooler with a multi-stage scrubber, a first heater, absorption tank, tar separator, knockout tank, , at least one pump, a second heater, gas analyzer and a chimney. The system does not require power or fuel for treatment of waste materials.

[032] The system as shown in FIG. 1 comprises at least one combustion chamber for decomposing or treating waste materials. Combustion chamber is provided with a feed door for feeding waste materials into said chamber through chute at a predetermined time interval for treating waste materials. Initially, the process of treatments starts when igniting an initial fire by a means. The means for igniting initial fire include camphor or cardboard by which treating of waste materials starts, thereafter splitting the molecules into atoms and further ionizing the atoms as electrons, protons and neutrons, and separated electrons energizes as accelerated electrons with strong energy.

[033] The air inlets allow atmospheric air to pass through a strong wiggleric field by using a plurality of wiggleric valves, where oxygen molecules of the atmospheric air split into exothermal oxygen with negative charge and this atomized oxygen oxidizes the organic surface and changes the waste materials to desperate organic oxide and thereby a reaction is induced by exothermic phenomenon. The wiggleric valves are provided in the middle of said chamber to generate strong wiggleric field for ionizing the molecules. These wiggleric valves can also be placed at the bottom of said chamber.

[034] The heating coils generate heat and retain it to said chamber. The waste heat from the chamber is recycled through a tubular heat sink and the recycled heat is supplied to wet waste material to reduce the moisture content, thereby increasing the amount of waste material to be feed into said chamber. The tumbling rods to tumble the waste materials feed into said chamber to mix and fast treatment of waste materials.

[035] The tubular radiator arranged at the lower layer of said chamber collects and separates ash deposited after the treatment of waste material. A vapour cooler with a multistage scrubber connected to a heat sink, said heat sink is arranged at a hearth center section of said chamber to attain uniform heat transfer throughout the process of waste material treatment of the system.

[036] The flue gas exhaust from said chamber is released into a vapour cooler and then to a chimney through an exhaust flue gas outlet, to release clean air into the atmosphere, where said chimney is fixed to said chamber. The toxic components from the flue gas exhaust are destroyed by using said water cooler by reducing temperature.

[037] The hopper is provided at the top of said chamber and at the bottom of said hopper is provided with chute, through which waste material is dumped into said chamber for treatment. Charge feed chute with safety airlock drop door and slide cover on top, chute mounted on the top of combustion chamber. Chute suitable for evenly distributing in the chamber-CS welded construction. The waste material is preheated using heat transfer through said doors when dumping waste material into said chamber through said hopper.

[038] In some embodiments, a plurality of insulated pipes is provided in said hopper to supply hot water for pre-heating the waste material.

[039] In one embodiment, load bumpers having suitable width is provided to accommodate waste material for pre-heating by providing one additional door in top.

[040] The tumbling rods are provided inside said chamber, where said tumbling rods are heated. The first heater provided at the bottom of said chamber for continuous cooling. When said chamber is cooled said heater ignites automatically to continue the waste material treatment process.

[041] FIG. 2 illustrates a projected view of the system for waste material treatment having feed door to receive the waste in to the combustion chamber. And the received waste is preheated in preheating chamber. A thermostat is placed to monitor the temperature of the system. Tumbling rods are provided to mix the waste homogeneously. A plurality of wiggleric valves are provided to pass atmospheric air through a strong wiggleric field, where oxygen molecules of the atmospheric air split into exothermal oxygen with negative charge and this atomized oxygen oxidizes the organic surface and changes the waste materials to desperate organic oxide and thereby a reaction is induced by exothermic phenomenon. The wiggleric valves are provided in the middle of said chamber to generate strong wiggleric field for ionizing the molecules. These wiggleric valves can also be placed at the bottom of said chamber. A water pump is provided to give cooling effect to the gases to condensate. Scrubbing cylinders are provided to remove of flue gases and chimney pipe according to the present invention.

[042] FIG. 3 illustrates a projected view of the combustion chamber of system for waste material treatment having feed door to receive the waste in to the combustion chamber. And the received waste is preheated in preheating chamber. And for smooth and timely flow of waste collapsible doors are provided. A thermostat is placed to monitor the temperature of the system. Tumbling rods are provided to mix the waste homogeneously. A plurality of wiggleric valves are provided to pass atmospheric air through a strong wiggleric field, where oxygen molecules of the atmospheric air split into exothermal oxygen with negative charge and this atomized oxygen oxidizes the organic surface and changes the waste materials to desperate organic oxide and thereby a reaction is induced by exothermic phenomenon. The wiggleric valves are provided in the middle of said chamber to generate strong wiggleric field for ionizing the molecules. These wiggleric valves can also be placed at the bottom of said chamber. To remove ash collected provision of ash removal door is placed. An auto ignition heater is provided for the ignition. A tar collector is provided to collect tar according to the present invention.

[043] Referring to FIG. 4, a multi-stage scrubber is provided with a plurality of tubes for cleaning said flue gas exhaust. Water is prayed through said tubes of said scrubber during cleaning of flue gases and removing tar accumulated on the walls of said scrubber.

[044] In some embodiments, the multi-stage scrubber is of two-stage or three-stage scrubber.

[045] The scrubber further comprises of a blower and a drip line. The blower is provided in a second pass circuit of said scrubber for removal of flue gases. The drip line is provided at said scrubber to remove tar accumulated on walls of said scrubber. The height of said scrubber is raised or lowered and accordingly varying the position of said exhaust pipe. The water pressure in said scrubber is increased by incorporating atomized water valves with multiple jets. The size and height of said exhaust pipe and said scrubber is variable to increase water pressure and flue gas pressure. The scrubber is provided with one or more doors for accessing said scrubber for maintenance. The pump mounted with a water tank for multi stage scrubbing and circulation.

[046] In some embodiments, the outlet pipe diameter of the flue gas from scrubber can be increased to improve the efficiency of the system.

[047] Referring now to FIG. 5a & 5b, a second heater provided at said exhaust pipe heats flue gases up to 900 degrees centigrade to remove all toxins and dioxins from flue gas during scrubbing in said scrubber. The multi-stage process of said scrubber also reduces production of tar content on walls of said scrubber which is produced during removal of toxins and dioxins from flue gas.

[048] In one embodiment, a manually operated screw-conveyor is also provided at the bottom of said chamber to remove ash. Also, a clinker breaker is also used to remove ash.

[049] The length of said exhaust pipe is varied with respect to the external environment and arranged in the proximity of preheating area of waste material. Also, the bends of said exhaust pipe can also be varied with respect to the external environment, and arranged in the proximity of preheating area of the waste material. [050] In one embodiment, a jacket is also provided for said exhaust pipe before said second heater can also be incorporated.

[051] Also, a plurality of micro water filters are arranged at inlet of water in said scrubber. A plurality of temperature sensors are incorporated in said system to measure temperature of said chamber and said scrubber. A plurality of non-return valves is incorporated at water inlet tubes.

[052] FIG. 6 illustrates a projected Tumbling view of the system for waste material treatment having combustion chamber where the degradation of waste occurs. A control panel is provided to monitor the process. A ceramic coating pipe and chimney pipe are provided for smooth functioning of the said system according to the present invention.

[053] The system is thermally shielded and pre -heated for operating at cold temperatures and capable of using solar power for operating the heaters alone.

[054] The system of the present invention for treating waste materials includes organic waste and inert waste such as hospital waste, pharmaceutical waste with mixed chemicals, mixed waste and organic waste can be well decomposed without creating or producing harmful materials or gases in to the environment.

[055] Also, the system can also be useful to treat inert waste such as Thermocol sheet, aluminium foil, plastic materials, rubber, animal poultry waste, non-vegetarian waste, waste carbon material which is retaining in automobile Industries.

[056] In some embodiments, the system is capable of using solar power by placing solar panels on top of the instrument so as to save electric power.

[057] It is to be understood that the invention described in the above paragraphs relates to specific embodiments and the present invention is not limited to the preferred embodiments shown. It is intended to cover various modifications and equivalent arrangements included within the scope of the appended claims.