WO2014017890A1

WO2014017890A1 - Waste-processing system and gas production method using same

Info

Publication number: WO2014017890A1
Application number: PCT/KR2013/006801
Authority: WO
Inventors: 한상관
Original assignee: Han Sangkwan
Priority date: 2012-07-27
Filing date: 2013-07-29
Publication date: 2014-01-30
Also published as: KR20120090919A; KR20130091709A

Abstract

The present invention relates to a waste-processing system and to a gas production method using same, in which all types of waste, such as residential garbage, scraps, sludge, human feces, animal feces, food waste, and wastewater are processed in an eco-friendly manner, and gas for domestic-use or industrial gas can be produced during the processing of waste.

Description

Waste treatment system and gas production method using the same

The present invention relates to a waste disposal system and a gas production method using the same, and more particularly, in such a waste disposal process while treating all kinds of wastes such as household waste, waste, sludge, serving, livestock, food waste, and waste water. The present invention relates to a waste disposal system that can be used for living or industrial purposes and a gas method using the same.

The present invention is an improved version of Publication No. 10-2012-0095330, which was created and published by the present applicant.

This application has a problem that the treatment efficiency is low because it uses a method of stacking the sludge and waste in the treatment tank and then transfer the leachate generated from the sludge and waste to the upper portion of the treatment tank to spray again.

In addition, there is a disadvantage in that the gas production efficiency is low due to the drawback that the sludge and wastes stacked in the treatment tank cannot be stirred.

However, the present application is an invention in which the treatment tank is configured as a storage type so that sludge and garbage stacked in the storage cabinet can be immediately replaced and disposed of, thereby improving processing efficiency.

Most of the fuels used in daily life are fossil fuels such as petroleum or coal, and these fossil fuels have limited reserves, so it is urgent to develop alternative energy.

In some developed countries, various developments such as automobiles and combustible engines using alcohol fuels are being substituted for fossil fuels, and methane gas generated during organic fermentation is collected and used as fuel.

On the other hand, some of the wastes and wastes generated in daily life can be recycled, but most of them are put in a waste-based bag.The wastes thus discarded are buried in landfills, which are caused by harmful gas components emitted from the landfills. It causes air pollution and requires a lot of waste landfills each year.

Of course, food waste is collected and reprocessed separately and then recycled as fertilizer, but the large amount of salt in food waste causes harmful effects such as salt damage when used as fertilizer. There was a drawback too much.

In view of this, Korean Patent No. 1999-0046850: Garbage Disposal System and Garbage Disposal Method, Publication No. 10-2010-0128165: Garbage Disposal Control System and Its Control Method and Used Garbage Collection Device, Publication No. 2001-0048043: Food and Beverage Waste treatment apparatus and its method, Publication No. 2000-0026905: Waste landfill system and its treatment method, Publication No. 10-2005-0107191: Synthesis gas production apparatus and manufacturing method using liquid waste, Publication No. 10-2007-0061495: Apparatus and method for producing fuel while processing waste, Publication No. 1999-0036918: Various waste treatment systems and methods have been disclosed, including energy waste systems for organic waste, but household waste, waste, sludge, servings, livestock and food waste. It was not possible to process all kinds of wastes such as wastewater and wastewater in a batch, and its application was limited.

The present invention has been proposed in view of this point, and it is environmentally friendly to all kinds of waste such as household waste, all kinds of wastes including metal or concrete waste, all kinds of sludge, serving, livestock, food waste, and various waste water. It is to provide a waste treatment system and a gas production method using the same to produce gas for living or industrial use during such waste disposal process.

In order to solve this problem, the present invention, crushed all kinds of waste, all kinds of sludge, all kinds of wastewater and household waste, waste, water treatment plant sludge or sewage treatment plant sludge, food waste, etc. about 0.5mm ~ 5cm Then, coal, limestone, shaft powder, phosphate, waste water, etc. are mixed to layer the layers in the treatment tank, and then the waste mixture is reprocessed using a chemical reaction generated by meeting the leachate continuously supplied through the nonwoven fabric. The gas is collected and used as fuel.

The present invention can be used for living or industrial purposes at the same time, while reprocessing all kinds of garbage such as household waste, waste, sludge, serving, livestock, food waste, waste water that can be discarded or recycled only after a separate treatment process. Since it is possible to produce a gas that can be used to minimize the environmental pollution by using the treatment system proposed in the present invention as well as the advantages of producing high-efficiency fuel without a large cost and adverse effects on the environment It has the effect of treating all kinds of wastes in an environmentally friendly manner without incurring chemicals and high costs. Especially, at the present time when fossil fuel is gradually being depleted, it can be used as an alternative energy. There is an advantage.

1 is a cross-sectional view of a gas generating induction tank used to produce gas while reprocessing waste according to a first embodiment of the present invention.

2 is a cross-sectional view of a treatment tank used to produce gas while reprocessing waste according to a second embodiment of the present invention.

According to the present invention, after grinding all kinds of waste, all kinds of sludge, all kinds of wastewater and household waste, waste, water treatment plant sludge or sewage treatment plant sludge, food waste, etc., about 0.5 mm to 5 cm, coal, limestone, , Wastewater, etc. by mixing the layered layer in the treatment tank and then using the chemical reaction generated by meeting the leachate continuously supplied through the nonwoven fabric to reprocess the waste mixture, and to collect the gas generated in this process to fuel It is intended to be used.

Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.

[First Embodiment]

1 is a cross-sectional view of a gas generating induction tank used to produce gas while reprocessing garbage according to a first embodiment of the present invention.

According to a first embodiment of the present invention, a leachate collection tank and a treatment tank are provided, and an injector for injecting leachate collected at a lower end of the treatment tank is installed at an upper end of the treatment tank, and a gas collecting device is used at the upper end of the treatment tank. It was to implement a system that produces gas.

First, all kinds of wastes on the earth, such as household waste, waste, sludge, serving, livestock, food waste, and wastewater, are crushed to about 0.001mm ~ 5cm by using a crusher, and the waste mixture is 20wt% ~ 35wt% of the total content. Preparing at a rate;

Preparing 0.1 wt% to 5 wt% of limestone composed of liquid or powder;

Preparing a food waste mixture by diluting about 0.001 wt% to 2 wt% of microorganisms and about 0.1 wt% to 5 wt% of soil in the food waste;

Preparing 1 wt% to 5 wt% of soil;

Preparing 0.1 wt% to 5 wt% of magnesium;

Preparing hydrogen peroxide at 0.1 wt% to 5 wt%;

Preparing 0.1 wt% to 5 wt% of wastewater generated in a beverage, liquor or food factory or any kind of industrial site for producing products;

Preparing 0.1 wt% to 5 wt% of waste oil generated from an engine such as an automobile or a ship, or waste oil generated from an industrial machine;

Preparing 0.1 wt% to 10 wt% of the fluid waste generated at a site such as a water purification plant or a sewage treatment plant;

Preparing 1wt% to 10wt% of a low grade coal such as a barrel generated from a coal mine;

A waste mixture for gas generation is prepared by preparing 0.01 wt% to 5 wt% of leachate generated from a metal or non-metal mine.

A gas generating induction tank 500 is provided for generating gas while treating the contents of the waste mixture. The gas generating induction tank 500 includes a material generating gas such as a waste mixture in the middle thereof. The waste mixture hanger 10 is composed of a layered layer so that the waste mixture storage box 100 can be stacked in layers. The lower end portion is configured with a liquid collecting port 600, and a heating line 106 is provided at the liquid collecting hole 600. do.

A photovoltaic generator support 107 is mounted to the outside of the gas generation induction tank 500, and a photovoltaic generator 100 is installed at the photovoltaic device support 107 to generate the photovoltaic electricity. The electricity generated in the device 105 is continuously transmitted to the heating line 106 is configured in the liquid collecting port 600 to raise the temperature of the liquid collecting port 600 to the gas generating induction tank 500 It is configured to increase the production efficiency of the gas of the various materials laminated on the).

Opening and closing device 700 is configured at the end of the liquid collecting port 600 is configured to discharge the leachate to the liquid collecting port 600.

The submersible motor 800 is installed in the liquid collecting port 600, and the liquid injector 200 is installed at an upper layer of the gas generating induction tank 500, and the submersible motor 800 and the liquid injector 200 are installed. The jet pipe 900 is connected between the leachate collected in the liquid collecting port 600 is forcibly moved to the upper layer of the gas generating induction tank 500 is configured to induce the gas again.

Communication 300 is formed in the layered layer of the gas generation induction tank 500, the heat generating device 400 is connected to the lower end of the communication 300, the layered layer of the gas generation induction tank 500 It is configured to transfer heat to it. At this time, the heat generating device 400 may be composed of a burner or the like, it is also possible to apply a device capable of generating heat through the power applied from the solar electric generating device 105 is applied thereto.

In addition, a rectangular or rectangular box shape is provided in the lower end of the waste mixture storage cabinet 100 is formed through the through hole 101 to pass through the leachate, the waste mixture storage cabinet 100 in the upper surface of the through hole 101 of the cloth or By installing the non-woven fabric 102 is configured to pass only the liquid while preventing the passage of solids, such a waste mixture cabinet 100 may be placed on the waste mixture hanger 10, respectively.

In addition, the upper end of the gas generation induction tank 500 is configured to form a gas collecting port 900 in a closed manner, and to the gas collecting port 900 to configure a gas collecting port 908.

In this state, all kinds of waste, all kinds of sludge, and all kinds of waste are mixed in the ratio of 20wt% to 35wt% at the upper end of the nonwoven fabric 102 configured in the waste mixture storage cabinet 100, and then crushed. Stacking the waste mixture 80 wt% to 95wt%;

Depositing 0.1 wt% to 5 wt% of limestone composed of a liquid or powder prepared in advance on an upper end of the waste mixture; and installing 1 wt% to 10 wt% of low coal generated in a coal mine at an upper end of the limestone;

Depositing 0.01% by weight to 5% by weight of leachate prepared in advance on the upper end of the lower coal such as the barrel;

Laying 1wt% to 5wt% of soil prepared in advance on the upper part of the leachate;

Depositing 0.1 wt% to 5 wt% of magnesium at the upper end of the soil;

Depositing 0.1 wt% to 5 wt% of hydrogen peroxide on the upper end of the magnesium;

Putting 25 wt% to 35 wt% of the food waste mixture prepared in advance on the upper end of the hydrogen peroxide;

Placing 0.1 wt% to 10 wt% of the fluid waste prepared in advance on the upper end of the food waste mixture;

Installing 0.1 wt% to 5 wt% of wastewater prepared in advance on an upper end of the fluid waste;

Disposing 0.1 wt% to 5 wt% of the waste oil prepared in advance on the upper end of the waste water;

Stacking the garbage mixture storage cabinet (100) in the gas generating induction tank (500) in layers after finishing lamination;

After stacking the garbage mixture storage box 100 in the gas generating induction tank 500

The gas generation induction tank through the process of raising the internal temperature of the gas generation induction tank 500 to 20 degrees to 300 degrees by using the heat generating device 400 configured at the lower end of the gas generation induction tank 500 All kinds of rubbish and all kinds of wastes characterized by an eco-friendly process for producing gas using the fermentation of the waste mixture stacked inside the 500 and a method of promoting the material explosive action and the catalytic reaction between the waste mixtures. We propose a gas-producing system that produces gas by using various kinds of sludge, all kinds of nutrients and livestock, all kinds of food waste and all kinds of wastewater, and an eco-friendly method for producing gas.

Although not shown in the drawing about the inlet for injecting the waste mixture, the waste mixture storage cabinet 100 can be easily put into the waste mixture storage cabinet 100 by configuring a variety of ways, such as a slide method.

Second Embodiment

The following describes a second embodiment of the present invention.

First, 20 wt% to 35 wt% of all kinds of waste existing on the earth, 20 wt% to 35 wt% of all kinds of sludge, and 20 wt% to 35 wt% of all kinds of waste are put together in a mixer and mixed together. Preparing a waste mixture by crushing the powder into a crusher and then smashing about 100 nm to 5 mm;

Put food waste 95wt% ~ 99.9wt%, soil 1wt% ~ 5wt%, microorganism 0.1wt% ~ 1wt% together in the mixer, put the mixed food waste into the grinder and grind it to 100nm ~ 5mm Making a mixture;

Putting condensate or phosphorus together in a mixer to form a liquid mixture;

Preparing 0.1 wt% to 5 wt% of limestone composed of liquid or powder;

By preparing 0.1wt% ~ 5wt% of wastewater from beverages, liquor, food factories, plating factories or all kinds of industrial sites producing products, the contents of waste mixtures for gas generation are prepared.

The treatment tank 1000 may be configured to stack the waste mixture and various materials generating the gas.

First, the liquid collecting port 600 is configured at the lower end of the processing tank 1000, and the heating line 106 is configured at the liquid collecting port 600 configured at the lower end of the processing tank 1000. The outside of the photovoltaic generator support 107 is configured, the photovoltaic device support 107 is configured with a photovoltaic electricity generating device 105 is the electricity generated by the photovoltaic generating device 105 It is continuously delivered to the heating line 106 is configured in the liquid collecting port 600 to increase the temperature of the liquid collecting port 600 to the gas of various materials stacked in the gas generating induction tank 500 It will be configured to increase the production efficiency of.

The upper end of the liquid collecting port 600 is configured with a waste support stand 102 is formed, the through hole 101, the non-woven fabric 103 is formed on the upper end of the waste support stand 102.

The submersible motor 800 is installed in the liquid collecting port 600, and a liquid injector 200 is installed at an upper layer of the treatment tank 1000, and the submerged motor 800 and the liquid injector 200 are disposed between the submersible motor 600. Blowing pipe 900 is coupled to.

The liquid collecting port 600 is configured with a communication 300 which is provided with a heat injection port 301 to transfer heat to the treatment tank 1000, the heat generating device 400 on the side of the communication 300 ) Is configured. In this case, the heat generator 400 may be configured as a burner using fossil fuel, or may be configured to be connected to the photovoltaic generator 105 so as to generate heat by a power applied thereto.

A rotating shaft 1002 is installed across the inner side and the other side of the treatment tank 1000, and a plurality of stirring vanes 1003 are formed on the rotating shaft 1002.

In addition, a reduction gear 1001 coupled to a motor is installed in a layered layer in the treatment tank 1000, and one side of the reduction gear 1001 and the rotation shaft 1002 are coupled to each other.

A gas collecting port 900 is hermetically configured at an upper end of the processing tank 1000, and a gas collecting hole 908 is formed at one side of the gas collecting port 900.

35wt% of the waste mixture made by mixing all kinds of waste, all kinds of sludge, and all kinds of waste together at the upper end of the waste restraint 102 configured in the treatment tank 1000 in this state. Stacking ˜45 wt%;

Installing 1 wt% to 5 wt% of soil at an upper end of the waste mixture;

Stacking 30 wt% to 40 wt% of a liquid mixture made of phosphorus and axial powder at the upper end of the soil;

Laying 1wt% to 5wt% of soil on the upper end of the liquid mixture;

Placing 0.1 wt% to 5 wt% of limestone composed of a liquid or powder prepared in advance on the upper end of the soil;

Depositing 1 wt% to 10 wt% of a low coal pulverized product generated in a coal mine at the upper end of the limestone;

Depositing 0.01 wt% to 5 wt% of magnesium at the upper end of the soil;

Stacking 25 wt% to 35 wt% of the food waste mixture prepared in advance on the upper end of the magnesium;

Laying 1wt% to 5wt% of soil on the upper end of the food waste;

Installing 0.1 wt% to 5 wt% of wastewater prepared in advance at the upper end of the soil;

After the treatment tank (1000) a layered layer of various waste mixtures and various mixtures are laminated

The leachate collected in the liquid collecting port 600 is collected by the underwater motor 800 and transferred to the upper end of the processing tank 600, and then continuously to the processing tank 1000 through the spraying device 200. While simultaneously spraying leachate

While simultaneously performing a process of increasing the internal temperature of the treatment tank 1000 to about 20 degrees to 300 degrees using the heat generating device 400 configured at the lower end of the treatment tank 1000.

By operating the speed reducer 1001 to rotate the stirring blades 1003 coupled with the speed reducer 1001, various materials stacked in the treatment tank 1000, various food waste mixtures, various servings and condensation mixtures. All kinds of wastes and all kinds of wastes characterized by eco-friendly process of producing gas by using materials fermentation, material exploding and material catalysis which are produced by contacting various components contained in wastes and various waste mixtures We propose an eco-friendly process for producing gas using sludge, all kinds of nutrients and livestock, all kinds of food waste and all kinds of wastewater, and a gas production system using gas treatment.

In addition, in a modified embodiment of the present invention, a method of injecting 1 wt% to 10 wt% of second iron oxide into the upper end of the gas generating induction tank and the treatment tank may be used to promote the production of gas.

In addition, a method of promoting the production of gas by injecting 0.1 wt% to 10 wt% of hydrochloric acid in the upper end of the gas generation induction tank and the treatment tank may be used.

In addition, a method of injecting 0.1 wt% to 10 wt% of liquid sulfur into the upper end of the gas generation induction tank and the treatment tank may be used to promote the production of gas.

In addition, a method of accelerating the production of gas by spraying 0.1wt% to 10wt% sulfuric acid in the upper end of the gas generating induction tank and the treatment tank can be used.

In addition, by spraying 0.1wt% to 10wt% of plating plant wastewater on the upper end of the gas generation induction tank and the treatment tank can be used to promote the production of gas.

In addition, it is possible to use a method of promoting the production of gas by spraying the liquid salt 0.1wt% ~ 10wt% in the upper end of the gas generating induction tank and the treatment tank.

In addition, 0.1wt% to 10wt% of a pulverized product made by pulverizing a gas hydride 1mm to 5cm in the middle of the waste mixture storage cabinet 100 configured in the gas generating induction tank and the processing tank in the middle of a substance such as a waste mixture It is possible to use a method in which layers are stacked in the middle to promote the production of gas.

In addition, a method of accelerating the production of the gas by spraying 0.1wt% to 10wt% of the calcium carbonate pulverized product converted into liquid at the upper end of the gas generating induction tank and the treatment tank can be used.

In addition, in the liquid collection port formed in the gas generating induction tank and the lower end of the treatment tank, carbon dioxide gas is volatilized to the gas generating induction tank and the upper end of the treatment tank to decompose various wastes and various materials stacked in the gas generating induction tank and the treatment tank. A method of promoting the production of gas can be used by means of promoting the process.

In addition, the production of gas by using a method of promoting the production of gas by spraying the weight of 0.1wt% to 10wt% of the total weight of the various kinds of substances introduced into the gas generating induction tank and the treatment tank to the upper end of the gas generating induction tank and the treatment tank There is a way to promote this.

In addition, the gas generation induction tank and the upper end of the treatment tank by spraying the weight of coal powder 0.1wt% ~ 10wt% of the total weight of the various substances put into the gas generation induction tank and the treatment tank by using the method of promoting the production of gas There are ways to promote production.

In addition, a method of accelerating the production of the gas by spraying 0.1wt% to 10wt% of the weight of the carbide powder relative to the total weight of the gas generating induction tank and the various substances put into the treatment tank at the upper end of the gas generating induction tank and the treatment tank. have.

In addition, a method of accelerating the production of the gas by spraying 0.1wt% to 10wt% of the iron oxide weight relative to the total weight of the gas generating induction tank and the various substances put into the treatment tank at the upper end of the gas generating induction tank and the treatment tank. .

The reason for putting soil into each layer in the gas generating induction tank and the treatment tank applied to the present invention is to neutralize the toxic properties generated during gas generation by exerting the neutralization action, which is the basic property of the soil.

The inventors of the present invention, in the early 1970s, when drying tobacco leaf, kneaded coal made by diluting powdered coal with water was burned in the oven of tobacco leaf drying chamber and used as tobacco leaf dry fuel. Covering the soil with kneaded soil and water on the top, I observed the phenomenon of poisonous gas smells. The present inventors cannot explain the action of the soil deposited in the treatment tank because there are no scientific studies on the effect of covering soil on top of coal and the principle of toxic gas components.

However, it is a fact of knowledge that when soil meets other components, it exerts another action, such as mass explosion and mass catalysis.

Therefore, even if the indication of the component according to the type and type of soil applied to the present invention is omitted, and the description of the action of the soil is omitted, it will be described that there is no obstacle to the action of the present invention.

In addition, microorganisms such as EM and microorganisms that can be produced in various materials stacked in layers in the gas generation induction tank of the present invention are properly diluted with other materials in the gas generation induction tank and then put together to promote gas production. It is explained that this modified embodiment can be used to promote the production of gas because it can be.

In addition, the plating wastewater generated in the plating plant belongs to industrial wastewater, that is, all wastewater, and the wastewater generated in the plating plant can be properly diluted with other materials, and layers can be laminated to promote gas production.

It is a matter of course that all of the methods for producing gas using the microbial method and the plating waste water listed above belong to the scope of the present invention.

In addition, induction of gas generation, which is applied to the present invention, waste metal waste obtained by crushing low-grade coal, such as coal-buffer sludge, which is low in coal mines, and waste-rock slurry, which is discarded in metal mines and nonferrous metal mines, has a size of about 1 cm to 10 cm. This design change is also within the scope of the present invention as it is possible to use a method of producing a gas by properly diluting with other materials in the tank and laminating them in layers.

In addition, all foods and foods, including liquor and other foods such as liquor, food, sweets, and ramen, all of which are consumed, eaten, or consumed by humans, such as waste from leather processing plants and oil refineries. As shown in the present invention, the wastes generated during the production process in all factories, including people and machines operated by humans and machines operated by humans and automobiles, are properly diluted with other substances in the gas generating induction tank of the present invention, and then the layers are laminated. It is natural that such a design change is also within the scope of the present invention as it can produce gas.

In addition, it is possible to produce gas by using a method in which the waste oil generated when exchanging the engine oil of machinery, ships or automobiles is properly diluted with other substances in the gas generation induction tank of the present invention, and then layered. As such, such design changes are also within the scope of the present invention.

In addition, the gas generating induction tank applied to the present invention may be configured to observe the inside of the treatment tank by installing a sight glass using a material such as glass.

The gas generating system configured as described above is produced by the heat generated by the heat generating apparatus while the gas production is promoted by the material catalysis, the material oxidation and the material explosive action generated when the physical properties of the materials are in contact with each other. As the internal temperature of the gas generating induction tank rises, the action of gas generation is promoted, and all kinds of waste, all kinds of sludge, and all kinds of wastes are naturally decomposed to generate gas.

In addition, the method of promoting the generation of gas by injecting various gaseous substances or gaseous gas into the gas generating induction tank and the treatment tank can be changed as much as possible by using the gas generating induction tank and the treatment tank proposed in the present invention. Naturally, they also belong to the scope of the present invention.

The present invention is applicable to all fields of producing gas for living or industrial use while treating all kinds of garbage existing on the earth.

Claims

In the middle part, the waste mixture hanger is composed of a layered layer so that the waste mixture cabinet containing the gas generating material is stacked in layers, the liquid collecting port is formed at the lower end, and the heating line is provided at the liquid collecting port;

A photovoltaic generator support is mounted to the outside, and a photovoltaic generator is installed at the photovoltaic apparatus support member to continuously apply power generated through the photovoltaic generator to the heating line;

An opening and closing device is configured at an end of the liquid collecting port to discharge the leachate into the liquid collecting port;

The liquid collecting port is equipped with an underwater motor, and an upper portion of the gas generating induction tank is provided with a liquid injector, and a jet pipe is connected between the underwater motor and the liquid injector, and the leachate collected in the liquid collecting port is returned to the upper layer. Configured to be forced to move;

Communication is installed in the middle layer to transfer heat, and a heat generating device is connected to the lower end of the communication;

A waste mixture storage box having a through hole formed on a lower surface thereof, and the waste mixture storage box mounted on the waste mixture hanger, respectively, with a cloth or a non-woven fabric installed on an upper surface of the through hole of the waste mixture storage box;

A gas collecting port is formed in a closed upper end portion, and a gas collecting hole is formed at one side of the gas collecting hole.
Preparing a waste mixture by mixing all kinds of waste existing on the earth, all kinds of sludge and all kinds of waste at a ratio of 20wt% to 35wt%, and then crushing the waste to about 0.001mm ~ 5cm using a grinder;

Preparing 0.1 wt% to 5 wt% of limestone composed of liquid or powder;

Preparing food waste mixture by diluting about 0.001 wt% to 2 wt% of microorganisms and about 0.1 wt% to 5 wt% of soil in food waste;

Preparing 1 wt% to 5 wt% of soil;

Preparing 0.1 wt% to 5 wt% of magnesium;

Preparing hydrogen peroxide at 0.1 wt% to 5 wt%;

Preparing 0.1 wt% to 5 wt% of wastewater generated in a beverage, liquor or food factory or any kind of industrial site for producing products;

Preparing 0.1 wt% to 5 wt% of waste oil generated from an engine such as an automobile or a ship, or waste oil generated from an industrial machine;

Preparing 0.1 wt% to 10 wt% of the fluid waste generated at a site such as a water purification plant or a sewage treatment plant;

Preparing 1wt% to 10wt% of a low grade coal such as a barrel generated from a coal mine;

Preparing a waste mixture for gas generation by preparing 0.01 wt% to 5 wt% of leachate generated by flowing out of a metal or non-metal mine;

After the waste mixture is put into the waste mixture storage box of claim 1, the heating wire is heated by electricity generated from the solar power generator to heat the waste mixture while communicating 200-300 ° heat generated through the heat generator. The waste mixture storage layer layer transfers heat to promote fermentation of the waste mixture and thereby generate gas;

The leachate collected in the liquid collecting port is pumped to the liquid injector of the upper layer through the underwater motor to induce continuous gas generation;

The generated gas is a gas production method using a garbage disposal system, characterized in that the collection by collecting the gas collection port through the gas collecting port formed in a closed manner.
A liquid collecting port is formed at a lower end, a heating line is configured at the liquid collecting hole, a solar electric generator support is configured at the outside, and a solar electric generator is installed at the solar electric device support to generate the solar electricity. Is configured to continuously apply electricity generated from the device to the heating wire;

The upper end of the liquid collecting port is configured with a waste restraint configured to be through, the non-woven fabric is installed on the upper end of the waste restraint;

An underwater motor is installed in the liquid collecting port, a liquid injector is installed in an upper layer, and a jet pipe is connected between the underwater motor and the liquid injector;

The liquid collecting port is configured to communicate with the heat injection port is provided, the side of the communication is configured with a heat generating device,

A rotating shaft is installed across one inner side and the other side, and a plurality of stirring vanes are formed on the rotating shaft, and a reducer coupled to the motor is installed in a layered layer, and one side and the rotating shaft of the reducer are coupled to each other;

A gas collecting port is formed in an upper end portion in a hermetic type, and a gas collecting hole is connected to one side of the gas collecting hole.
20 wt% to 35 wt% of all kinds of waste on the earth, 20 wt% to 35 wt% of all kinds of sludge, and 20 wt% to 35 wt% of all kinds of waste are put together in a mixer, mixed together, and then the mixed mixture is placed in a grinder. Preparing a waste mixture by grinding about 100 nm to 5 mm;

Put food waste 95wt% ~ 99.9wt%, soil 1wt% ~ 5wt% and microorganism 0.1wt% ~ 1wt% together in the mixer, and then put the mixed food waste into the grinder and grind the food waste mixture by about 100nm ~ 5mm. Making process;

Putting condensate or phosphorus together in a mixer to form a liquid mixture;

Preparing 0.1 wt% to 5 wt% of limestone composed of liquid or powder;

Preparing waste mixtures for gas generation by preparing 0.1wt% ~ 5wt% of wastewater from beverage, liquor, food factory, plating factory or all kinds of industrial sites producing products;

The waste mixture is placed in the waste mixture support of claim 3 and heats the heating mixture through the electricity generated from the photovoltaic electricity generating device to heat the waste mixture while heating the waste mixture 200 ~ 300 ° Communicating with the waste mixture settle through communication to promote fermentation of the waste mixture and thereby generate gas;

Rotating a plurality of rotating shafts to continuously stir the waste mixture placed on the waste mixture setter through stirring blades installed on each rotating shaft to induce gas generation;

The leachate collected at the liquid collection port is pumped to the liquid injector of the upper layer through the underwater motor to induce continuous gas generation;

The generated gas is collected in a gas collecting port through a gas collecting port formed in a closed type at the upper end of the gas production method using a waste disposal system, characterized in that the collection
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 1wt% to 10wt% of the second iron oxide relative to the total weight of the waste mixture for gas generation
The method according to claim 2 or 4,

Gas production method using a waste treatment system, characterized in that to promote the production of gas by further spraying 0.1wt% ~ 10wt% hydrochloric acid to the top of the waste mixture to the total weight of the waste mixture for gas generation
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% to 10wt% of liquid sulfur relative to the total weight of the waste mixture for gas generation to the top of the waste mixture
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% to 10wt% sulfuric acid relative to the total weight of the waste mixture for gas generation to the top of the waste mixture
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% ~ 10wt% of the plating plant wastewater to the waste mixture relative to the total weight of the waste mixture for gas generation.
The method according to claim 2 or 4,

Gas production method using a waste treatment system characterized in that to promote the production of gas by further spraying the liquid salt 0.1wt% ~ 10wt% relative to the total weight of the waste mixture for gas generation
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% to 10wt% of calcium carbonate pulverized to the total weight of the waste mixture for gas generation.
The method according to claim 2 or 4,

Garbage, characterized in that the production of gas by promoting the production of the gas layer by laminating 0.1wt% ~ 10wt% of the pulverized product by grinding the gas hydride 0.1mm ~ 5cm relative to the total weight of the waste mixture for gas generation Gas production method using treatment system
The method according to claim 2 or 4,

Gas production method using a waste treatment system to promote the production of gas by injecting carbon dioxide gas into the gas generating induction tank or the upper end of the treatment tank in the liquid collection port to promote decomposition of the waste mixture
The method according to claim 2 or 4,

Gas production method using a garbage disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% ~ 10wt% alcohol to the top of the waste mixture to the total weight of the waste mixture for gas generation
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% ~ 10wt% magnesium solution to the top of the waste mixture to the total weight of the waste mixture for gas generation.
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying the liquid coal powder solution 0.1wt% ~ 10wt% relative to the total weight of the waste mixture for gas generation.
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of the gas by further spraying 0.1wt% ~ 10wt% of liquid carbide solution relative to the total weight of the waste mixture for gas generation to the top of the waste mixture.
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by further spraying 0.1wt% ~ 10wt% iron oxide solution to the top of the waste mixture to the total weight of the waste mixture for gas generation
The method according to claim 2 or 4,

The gas production method using a waste disposal system, characterized in that to promote the production of gas by injecting carbon dioxide gas into the upper end of the gas generating induction tank and the treatment tank in the liquid collection port.
The method according to claim 2 or 4,

Gas production method using a waste treatment system to promote the production of gas by injecting nitrogen gas into the upper end of the gas generating induction tank and the treatment tank in the liquid collection port to promote decomposition of the waste mixture
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the production of gas by introducing hydrogen gas into the upper end of the gas generating induction tank and the treatment tank in the liquid collection port.
The method according to claim 2 or 4,

Gas production method using a waste disposal system, characterized in that to promote the decomposition of the waste mixture by introducing the sulfurous acid gas into the upper end of the gas generating induction tank and the treatment tank in the liquid collecting port.